model.lst Thu Apr 05 21:29:03 2018 1newton.cheme.cmu.edu/interfaces/steam/model.pdfmodel.lst Thu Apr...

model.lst Wed May 30 15:17:17 2018 1

model.lst Wed May 30 15:17:17 2018 2

GAMS 24.4.1 r50296 Released Dec 20, 2014 LEX-LEG x86 64bit/Linux

05/30/18 15:17:15 Page 1

G e n e r a l A l g e b r a i c M o d e l i n g S y s t e m

C o m p i l a t i o n

INCLUDE /var/www/html/interfaces/cgi-bin/steam/ex3.dat

2 Scalars

3

4 AmbT Ambient temperature /298.15/

5 AmbP Ambient Pressure /1.01325/

6 R Universal gas const (J per mol K) /8.314/

7 gamma Ratio of Cp to Cv /1.33/

8 Tref Reference temperature for Enthalpy calculations /298.15/

9 EMAT Exchanger minimum approach temperature /10/

10 EpsP2 Epsilon for 2 phase utility cycle /1.0E-4/

11 BigMforT Big M for Temperature /500/

12 BigMforTurbFlow Big M for Turbine Flow /1.0E8 /

13 DumPrice Dummy price for binary variables /1.0E-3/

14 ElecDmd Electricity Demand (MW) /30/

15 UBMD Upper boound for mechanical demand /100/

16 UBED Upper bound for electrical demand /800/

17 CWCost Cooling Water cost ($ per Ton) /0.0269/

18 DWCost Demineralized Water cost ($ per Ton) /0.32/

19 FCost Fuel Cost ($ per MBtu) /12/

20 DeaerP Operating pressure Deaerator(MPa) /0.02/

21

22

23

24 Sets

25

26 Comp1 chemical components in IGCC /

27 C Carbon (solid)

28 H2 Hydrogen

29 O2 Oxygen

30 N2 Nitrogen

31 S Sulfur

32 CH4 Methane

33 CO Carbon monoxide

34 CO2 Carbon dioxide

35 H2O Water

36 H2S Hydrogen sulfide

37 COS Carbonyl sulfide

38 NH3 Ammonia

39 ASH Ash (inert solid) /

40

41

42

43

44 Str process streams /1*65/

45 Phase2Str(Str) possibility of 2 phase /1*7,12,25,26,31*36,47*51,55*65/

46 SatVapStr(Str) Saturated vapour stream /16/

47 VapStr(Str) Vapour streams /21,22,23,24,27,28,29,30,39*46/

48 SatLiqStr(Str) SAturated Liquid streams /8,10,11,13,14,15,37,38,52*54/

49 LiqStr(Str) Subcooled liquid stream /9,17,18,19,20/

50 AirStr(Str) Air streams /27,29,39/

51 SyngasStr(Str) Syngas Stream /28,30,41,44/

52 WatStr(Str) Water Stream /1*20,25,26,31*38,47,48*65/

53

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54

55 * for convenience in giving fixes and bounds

56 HPStr(Str) HP streams /1,26,31,34,37,47,48,53,54,58,62/

57 MPStr(Str) MP streams /2,5,10,25,32,35,50,52,55,59,63/

58 LPStr(Str) LP streams /3,6,12,33,36,38,56,60,64/

59 CDPStr(Str) codensate deaerator stream /11,13,14,15,16/

60 VPStr(Str) VP streams /4,7,8,57,61,65/

61 TfDeAertr(Str) Temperature of aerator /11,13,14,15,16,18,19,20/

62 GasStr(Str) Gas streams for boiler /27,28,29,30,21,22,23,24/

63 Gas2Str(Str) Gas streams for turbine /39*46/

64 P2P1Str(Str) 2 phase streams sure of no wet /1,31,34,25,26,47,48,58,62/

65 P2P2Str(Str) 2 phase streams sure of wet /4,7,57,61,65/

66

67

68 STR_DYN(Str) Dynamic set - streams

69

70

71

72

73

74

75 HPStmTurb HP Steam turbine /1*3/

76 MPStmTurb MP Steam turbine /1*2/

77

78 VacCondTurb Vacuum condensor for turbine /1/

79

80 Pump Liquid Pumps /VP,MP,HP,HRSG/

81

82 DeAertr Deaerator /1/

83

84 CondHdr Condensate header /1/

85

86 Blr Boilers (Steam generators) /HP,MP,HRSG/

87 BlrCmbtr BlrCombuster /HP,MP,GT,GTSF/

88

89 StmDmd Steam Demand /HP,MP,LP/

90 MechDmd Mechanical Power Demand /1*2/

91

92

93 **GAS turbine part

94 GTCmpr Compressor of gas turbine /1/

95 GTExpdr Expander of Turbine /1/

96

97 Vlv Throttle Valve /HPMP, MPLP/

98

99

100

101

102

103

104 Comp(Comp1) Components in utility /

105 H2 Hydrogen

106 O2 Oxygen

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107 N2 Nitrogen

108 CH4 Methane

109 CO Carbon monoxide

110 CO2 Carbon dioxide

111 H2O Water/

112

113 WatComp(Comp) /H2O/

114

115 NonWatComp(Comp) /H2,O2,N2,CH4,CO,CO2/

116

117 AirComp(Comp) /O2,N2/

118

119 NonAirComp(Comp) /H2,CH4,CO,CO2,H2O/

120

121 SyngasComp(Comp) /H2,CO,CH4,CO2/

122

123 NonSyngasComp(Comp) /O2,N2,H2O/

124

125

126 CombRxns Combustion Reactions /

127 H2Comb H2 burns forms H2O

128 COComb CO forms CO2

129 CH4Comb CH4 forms CO2 and H2O

130 /

131

132

133 BurnComp(CombRxns,Comp) Component that burns in a reaction /

134 H2Comb.H2 , COComb.CO , CH4Comb.CH4 /

135

136

137 ModeHPStmTurb Mode of operation of HP steam turbine/

138 MPBkPr MP Backpressure

139 MPExt MP Extraction

140 LPBkPr LP Backpressure

141 LPExt LP Extraction

142 VPCond Condensing to Vacuum pressure /

143

144

145 ModeMPStmTurb Mode of operation of HP steam turbine/

146 LPBkPr LP Backpressure

147 LPExt LP Extraction

148 VPCond Condensing to Vacuum pressure /

149

150 PLev1 Universal set of Pressure levels /HP,MP,LP,CDP,VP/

151

152 PLev(PLev1) Steam Pressure Levels /HP,MP,LP/

153

154

155 *************************************

156 ** Flowsheet topology

157 ************************************

158

159 ** HP steam turbine

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160 InHPStmTurb(HPStmTurb,Str) Input stream to HP Steam turbine /

161 1.1 , 2.58 , 3.62 /

162

163 OutMPHPStmTurb(HPStmTurb,Str) Output MP stream of HP Steam turbine /

164 1.2 , 2.59 , 3.63/

165

166 OutLPHPStmTurb(HPStmTurb,Str) Output LP stream of HP Steam turbine /

167 1.3 , 2.60 , 3.64/

168

169 OutVPHPStmTurb(HPStmTurb,Str) Output VP stream of HP Steam turbine /

170 1.4 , 2.61 , 3.65/

171

172 ** MP steam turbine

173 InMPStmTurb(MPStmTurb,Str) Input stream to MP Steam turbine /

174 1.5 , 2.55 /

175

176 OutLPMPStmTurb(MPStmTurb,Str) Output LP stream of MP Steam turbine /

177 1.6 , 2.56 /

178

179 OutVPMPStmTurb(MPStmTurb,Str) Output VP stream of MP Steam turbine /

180 1.7 , 2.57 /

181

182

183 ** Vacuum condensor

184 InVacCondTurb(VacCondTurb,Str) Input streams to vacuum condensor /1.(4,7,57,61,

65)/

185 OutVacCondTurb Output streams of vacuum condensor /1.8/

186

187 ** Liquid Pumps

188 InPump(Pump,Str) Inlet stream of pump /

189 VP.8 , MP.13 , HP.14 , HRSG.15 /

190

191 OutPump(Pump,Str) Outlet stream of pump /

192 VP.9 , MP.18 , HP.19 , HRSG.20 /

193

194 ** Deaerator

195 InDeAertr(DeAertr,Str) inlet stream of deaerator /1.(9,11,12,17)/

196 OutLDeAertr(DeAertr,Str) outlet liquid streams of deaerator /1.(13,14,1

5)/

197 OutVDeAertr(DeAertr,Str) outlet vapour stream of deaerator /1.(16)/

198

199 ** Condensate header

200 InCondHdr(CondHdr,Str) inlet stream to condensate header /1.(10,37,38)/

201 OutCondHdr(CondHdr,Str) outlet stream of condensate header /1.11/

202

203

204 *** Boiler with combuster

205 InGasBlr (Blr,Str) Inlet gas stream for Boiler /

206 HP.21, MP.23, HRSG.45 /

207

208 OutGasBlr(Blr,Str) Outlet gas stream for Boiler /

209 HP.22, MP.24 , HRSG.46 /

210

211 InWtrBlr(Blr,Str) Inlet water stream for Boiler /

212 HP.19, MP.18 , HRSG.20 /

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213

214 OutStmBlr(Blr,Str) Outlet steam stream for Boiler /

215 HP.26, MP.25 , HRSG.47 /

216

217 OutWtrBlr(Blr,Str) Outlet blowdwon stream for Boiler /

218 HP.53, MP.52 , HRSG.54 /

219

220

221 InBlrCmbtr(BlrCmbtr,Str) Input stream to Combuster /

222 HP.(27,28) , MP.(29,30), GT.(40,41), GTSF.(43,44) /

223

224 OutBlrCmbtr(BlrCmbtr,Str) Output stream of Combuster /

225 HP.21 , MP.23 , GT.42, GTSF.45/

226

227 *** Pressure headers

228 InPLev(PLev,Str) Input stream to header /

229 HP.(31,26,47) , MP.(2,32,25,49,59,63) , LP.(3,6,33,51,56,60,64)

/

230

231 OutPLev(PLev,Str) Outlet stream of header /

232 HP.(1,34,48,58,62) , MP.(5,35,50,55) , LP.(12,36) /

233

234

235

236 InStmDmd(StmDmd,Str) Input stream to steam demand /

237 HP.34 , MP.35 , LP.36 /

238

239 OutStmDmd(StmDmd,Str) Output stream to steam demand /

240 HP.37 , MP.10 , LP.38 /

241

242

243 InGTCmpr(GTCmpr,Str) Input stream to compressor /1.39/

244 OutGTCmpr(GTCmpr,Str) Output stream of compressor /1.40/

245

246 InGTExpdr(GTExpdr,Str) Input stream to expander /1.42/

247 OutGTExpdr(GTExpdr,Str) Output stream of expander /1.43/

248

249 InVlv(Vlv,Str) Input stream to throttle valve /

250 HPMP.48, MPLP.50 /

251 OutVlv(Vlv,Str) Output stream of throttle valve /

252 HPMP.49, MPLP.51 /

253

254 ;

255

256

257 Alias (Comp , Comp2), (Str , Str2) ;

258

259

260 Parameters

261

262

263 UBPL(PLev1) Upper bounds for pressure level /

264 HP = 80 , MP = 40 , LP = 10, CDP = 1.41, VP = 0.21 /

265

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266 LBPL(PLev1) Lower bounds for pressure level /

267 HP = 45 , MP = 15 , LP = 4 , CDP = 1.39, VP = 0.19 /

268

269 MaxSupHt(PLev1) Maximum superheat /

270 HP = 225, MP = 175, LP = 125/

271

272 UBTSat(PLev1) Upper bounds for Tsat of pressure level /

273 HP = 570.0, MP = 526, LP = 456.0, CDP = 383.0, VP = 334.0 /

274

275 LBTSat(PLev1) Upper bounds for Tsat of pressure level /

276 HP = 528.0, MP = 469.0, LP = 414.0, CDP = 382.0, VP = 333.0 /

277

278

279 UBT(PLev1) Upper bounds for Tsat of pressure level /

280 HP = 795.0, MP = 701, LP = 581.0, CDP = 383.0, VP = 334.0 /

281

282 LBT(PLev1) Upper bounds for Tsat of pressure level /

283 HP = 528.0, MP = 469.0, LP = 414.0, CDP = 382.0, VP = 333.0 /

284

285 FxPL(PLev1) Fixed values for pressure level /

286 HP = 45 , MP = 20 , LP = 7, CDP = 1.4, VP = 0.2/

287

288 HtReq(StmDmd) Heating demand of individual steam levels/

289 HP = 5 , MP =20 , LP = 8 /

290

291 HHV(Comp) Heating value (MBtu per kmol) /

292 H2 = 0.269258, O2 = 0.0, N2 = 0.0, CH4 = 0.839671, CO = 0.269558,

CO2 = 0.0, H2O = 0.0/

293

294

295 MDReq(MechDmd) Mechanical demand required /

296 1 = 10.0 , 2 = 20.0/

INCLUDE /var/www/html/interfaces/cgi-bin/steam/model.inc

298

299

300 StdHtFormGas(Comp1) Heat of formation as gas at Tref (MJ per kmol) /

301 C = 0.0, H2 = 0.0, O2 = 0.0, N2 = 0.0, S = 0.0, CH4 = -

74.52, CO = -110.53, CO2 = -393.51,

302 H2O = -241.814, H2S = -20.63, COS = -142.0, NH3 = -45.8

98, ASH = 0.0/

303

304

305 CpIGConstA(Comp1) Constant A for calculating ideal gas heat capcity /

306 C = -2.0194E-011, H2 = -8.72413588824715E-012, O2 = 1.00321

110903601e-011, N2 = 6.4863934487993e-013, S = 0.0,

307 CH4 = 4.31711266220667e-011, CO = 2.88987617653835e-012, C

O2 = 9.08521151389437e-012,

308 H2O = 4.19683964610337e-012, H2S = 9.15376273994147e-012, C

OS = -1.70813985811133e-011,

309 NH3 = 1.73243144182674e-011, ASH = 0.0 /

310

311

312 CpIGConstB(Comp1) Constant B for calculating ideal gas heat capcity /

313 C = 8.5342E-08, H2 = 3.13062251644783e-008, O2 = -3.6329587

575635e-008, N2 = -6.96486792964864e-009, S = 0.0,

314 CH4 = -1.65108811145229e-007, CO = -1.4576789091584e-008,

model.lst Wed May 30 15:17:17 2018 8

CO2 = -2.1697313637398e-008,

315 H2O = -1.9470098998775e-008, H2S = -3.86650374047016e-008,

COS = 7.35597253373221e-008,

316 NH3 = -6.59890687065529e-008, ASH = 0.0/

317

318

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319 CpIGConstC(Comp1) Constant C for calculating ideal gas heat capcity /

320 C = -0.00013353, H2 = -3.7212402373867e-005, O2 = 4.2050264

4993578e-005, N2 = 1.50552864518556e-005, S = 0.0,

321 CH4 = 0.000204704210929332, CO = 2.31148304821567e-005, CO

2 = -2.33498744756968e-006,

322 H2O = 3.17592869409794e-005, H2S = 5.27009560659823e-005, C

OS = -0.000124372692200708,

323 NH3 = 8.03116337357631e-005, ASH = 0.0/

324

325

326 CpIGConstD(Comp1) Constant D for calculating ideal gas heat capcity /

327 C = 0.099493, H2 = 0.0191413559523374, O2 = -0.010547270342

9208, N2 = -0.00566985412879804, S = 0.0,

328 CH4 = -0.0452545153691324, CO = -0.00805228138930104, CO2

= 0.0446793224837683,

329 H2O = -0.00925060124457646, H2S = -0.0111860932347389, COS

= 0.105986561099127,

330 NH3 = -0.00774915657425819, ASH = 0.0/

331

332 CpIGConstE(Comp1) Constant E for calculating ideal gas heat capcity /

333 C = -10.789, H2 = 25.6468302684313, O2 = 29.7351909214832,

N2 = 29.5810529469761, S = 35.0,

334 CH4 = 35.6024511978605, CO = 29.7785323815701, CO2 = 24.59

80359335846,

335 H2O = 34.0544739123994, H2S = 33.8617361686317, COS = 18.86

47808687915,

336 NH3 = 32.7756279074386, ASH = 0.0/

337

338 FracConv(Comp) Fractional conversion of a component in its association combusti

on reaction /

339 H2 = 1.0 , CO = 1.0, CH4 = 1.0/

340

341

342 ExtAnt1(Comp) Extended Antoine constants 1 (T in K and P in bar)/

343 H2O = 61.03707454 /

344


346 H2O = -7206.7 /

347


349 H2O = 0.0 /

350


352 H2O = 0.0 /

353


355 H2O = -7.1385 /

356


358 H2O = 4.046E-06 /

359


361 H2O = 2 /

362

363

364

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365 LatHt1(Comp) Constant 1 for Latent heat of vaporization /

366 H2O = 52.053 /

367


369 H2O = 0.3199 /

370


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372 H2O = -0.212 /

373


375 H2O = 0.25795 /

376


378 H2O = 0.0 /

379

380

381

382 Tc(Comp) Critical temperature /

383 H2O = 647.13 /

384

385

386 ;

387

388

389

390 Table

391 CombRxnsStoicMtrx(CombRxns,Comp) gasifier stoichiometric matrix (only reacting compo

nents)

392 H2 O2 N2 CH4 CO CO2 H2O

393 H2Comb -1 -0.5 1

394 COComb -0.5 -1 1

395 CH4Comb -2 -1 1 2 ;

396

397

398

399

400 ***************************************

401 * Now declaration of Variables start

402 ***************************************

403

404

405 ******************************

406 ** Variables for STREAMS

407 ******************************

408 Positive Variables

409 F(Str) Flowrate of Stream (kmol per hr)

410 Fc(Str,Comp) Component flowrate of stream

411 T(Str) Temperature of stream

412 P(Str) Pressure of stream

413

414 ** Variables for 2 phase streams in utility system

415 TrP2(Str)

416 LatHtVapP2(Str,Comp)

417 Wetns(Str)

418 TSat(Str)

419

420 ** Variables for subcooled liquid in utility system

421 TrLiq(Str)

422 LatHtVapLiq(Str,Comp)

423

424 ;

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425

426 Binary variables

427 Y(Str) Binary variable

428 * yp(Str) Binary variable for stream pressure

429 YP2(Str) binary variable for 2 phase water streams

430 ;

431

432

433 Variables

434 H(Str) Enthalpy of stream

435

436 ** Variables for 2 phase streams in utility system

437 HVap(Str)

438 HSatLiq(Str)

439 HSatVap(Str)

440 Hc(Str,Comp)

441

442

443 ;

444

445

446

447

448

449

450

451 **********************************

452 * Variables for HP Steam Turbine

453 **********************************


455 InHPPHPStmTurb(HPStmTurb) Inlet HP Pressure for expander of HP Steam turbine

456 InHPTHPStmTurb(HPStmTurb) Inlet HP Temperature for expander of HP Steam turbine

457

458 OutMPPHPStmTurb(HPStmTurb) Outlet MP Pressure for expander of HP Steam turbine

459 OutLPPHPStmTurb(HPStmTurb) Outlet LP Pressure for expander of HP Steam turbine

460

461 OutMPTHPStmTurb(HPStmTurb) Outlet MP Temperature for expander of HP Steam turbine

462 OutLPTHPStmTurb(HPStmTurb) Outlet LP Temperature for expander of HP Steam turbine

463

464 MPWorkHPStmTurb(HPStmTurb) MP expnasion work of HP Steam turbine

465 LPWorkHPStmTurb(HPStmTurb) LP expnasion work of HP Steam turbine

466 VPWorkHPStmTurb(HPStmTurb) VP expnasion work of HP Steam turbine

467 TotWorkHPStmTurb(HPStmTurb) Total work of HP Steam turbine

468

469 Dum1HPStmTurb(HPStmTurb)






475



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482

483 ;

484

485 Binary Variables

486 YModeHPStmTurb(HPStmTurb,ModeHPStmTurb)

487 YLP(HPStmTurb) ;

488

489

490

491

492

493 **********************************

494 * Variables for MP Steam Turbine

495 **********************************


497 InMPPMPStmTurb(MPStmTurb) Inlet MP Pressure for expander of MP Steam turbine

498 InMPTMPStmTurb(MPStmTurb) Inlet MP Temperature for expander of MP Steam turbine

499

500

501

502 OutLPPMPStmTurb(MPStmTurb) Outlet LP Pressure for expander of MP Steam turbine

503 OutVPPMPStmTurb(MPStmTurb) Outlet vacuum Pressure for expander of HP Steam turbine

504

505 OutMPTMPStmTurb(MPStmTurb) Outlet MP Temperature for expander of HP Steam turbine

506 OutLPTMPStmTurb(MPStmTurb) Outlet LP Temperature for expander of HP Steam turbine

507

508

509 LPWorkMPStmTurb(MPStmTurb) LP expnasion work of MP Steam turbine

510 VPWorkMPStmTurb(MPStmTurb) VP expnasion work of HP Steam turbine

511 TotWorkMPStmTurb(MPStmTurb) Total work of HP Steam turbine

512

513 Dum11MPStmTurb(MPStmTurb)






519

520 ;

521

522 Binary Variables

523 YModeMPStmTurb(MPStmTurb,ModeMPStmTurb) ;

524

525

526

527 **********************************

528 * Variables for Vacuum condensor

529 **********************************


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531 HtLdVacCondTurb(VacCondTurb)

532 MassFCW

533 WorkPumpVCT ;

534

535

536 **********************************

537 * Variables for Pump

538 **********************************


540 WorkPump(Pump) ;

541

542

543

544 **********************************

545 *** Variables for Combuster

546 **********************************

547


549 Dum1BlrCmbtr(BlrCmbtr,Comp);

550

551

552

553 **********************************

554 * Variables for Boilers

555 **********************************


557 QBlr(Blr) Heat exchanged ;

558

559

560

561 **********************************

562 * Variables for Header

563 **********************************


565 POpr(PLev) operating pressure of header

566 TOpr(PLev) operating temperature of header

567 TSatOpr(PLev) Heat exchanged

568 ;

569

570

571 *****************************************************

572 * Variables for Steam Demand

573 *****************************************************


575 WasteH(StmDmd)

576 MassFCW1(StmDmd) ;

577

578

579

580

581 *****************************************

582 ** Variables for Air and syngas streams

583 *****************************************

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585 WorkFan ;

586

587

588

589

590 *********************************************

591 *** Variables for Compressor of gas turbine

592 *********************************************


594 InPGTCmpr(GTCmpr) Inlet Pressure for compressor

595 OutPGTCmpr(GTCmpr) Outlet Pressure for compressor

596 InTGTCmpr(GTCmpr) Inlet Temperature for compressor

597 OutTGTCmpr(GTCmpr) Outlet Temperature for compressor

598 WorkGTCmpr(GTCmpr) Ideal compressor work ;

599

600

601

602 **********************************

603 * Variables for Exapnder of gas turbine

604 **********************************


606 InPGTExpdr(GTExpdr) Inlet Pressure for expander

607 OutPGTExpdr(GTExpdr) Outlet Pressure for expander

608 InTGTExpdr(GTExpdr) Inlet Temperature for expander

609 OutTGTExpdr(GTExpdr) Outlet Temperature for expander

610 WorkGTExpdr(GTExpdr) Ideal expander work

611 WorkGT ;

612

613

614

615 *****************************************

616 ** Variables to be changed later

617 *****************************************

618 Positive variables

619 MDE(MechDmd)

620 WHPTE(HPStmTurb)

621 MDC(MechDmd)

622 WHPTM(HPStmTurb,MechDmd)

623 WMPTM(MPStmTurb,MechDmd)

624 ;

625

626 Binary variables

627 YMD(MechDmd)

628 YWHPTE(HPStmTurb)

629 YWHPTM(HPStmTurb,MechDmd)

630 YWMPTM(MPStmTurb,MechDmd)

631 ;

632

633

634

635 *********************************

636 * Dummy variables

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637 *********************************

638 Variables

639 Z ;

640

641

642

643

644

645

646

647 ***************************************

648 * Now declaration of Equations start

649 ***************************************

650

651

652 *****************************************************

653 * Equations for streams

654 *****************************************************

655 Equations

656 * solo para este problema. ec de abajo

657 EqTotMolStr(Str) Total mass balance for stream (Total Mole flow = sum of component Mole

flow)

658 EqEnthpyGasStr1(Str,Comp)

659 EqEnthVapStr2(Str)

660 EqEnthSatLiq(Str)

661 EqTSat(Str)

662 EqEnthP2Str(Str) Enthalpy of 2 phase stream

663 EqTP2(Str)

664 EqLogP21(Str)

665 EqLogP22(Str)

666 EqLogP23(Str)

667 EqTrP2(Str)

668 EqLatHtVapP2(Str,Comp)

669

670 EqEnthSatLiq1(Str)

671 EqnTfSatLiqVap(Str)

672

673 EqEnthLiqStr(Str)

674 EqTrLiq(Str)

675 EqLatHtVapLiq(Str,Comp)

676

677 EqEnthSatVap(Str)

678 EqEnthSatVap1(Str)

679

680 ;

681

682 EqTotMolStr(Str)..

683 F(Str) =E= Sum(Comp, Fc(Str,Comp)) ;

684 **solo para este ejemplo

685 EqEnthpyGasStr1(Str,Comp)$VapStr(Str)..

686 Hc(Str,Comp) =E= (StdHtFormGas(Comp) + 1.0E-3*(CpIGConstA(Comp)/5*(T(Str)**5 - Tref

**5)

687 + CpIGConstB(Comp)/4*(T(Str)**4 - Tref**4) + CpIGConstC(Comp)/3*(T(Str)*

*3 - Tref**3)

688 + CpIGConstD(Comp)/2*(T(Str)**2 - Tref**2) + CpIGConstE(Comp)*(T(Str) -

Tref)))/3600 ;

model.lst Wed May 30 15:17:17 2018 17

689

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690

691 EqEnthVapStr2(Str)$Phase2Str(Str)..

692 HVap(Str) =E= (StdHtFormGas(’H2O’) + 1.0E-3*(CpIGConstA(’H2O’)/5*(T(Str)**5 - Tref

**5)

693 + CpIGConstB(’H2O’)/4*(T(Str)**4 - Tref**4) + CpIGConstC(’H2O’)/3*(T(Str

)**3 - Tref**3)

694 + CpIGConstD(’H2O’)/2*(T(Str)**2 - Tref**2) + CpIGConstE(’H2O’)*(T(Str)

- Tref)))/3600 ;

695

696 EqEnthSatLiq(Str)$(Phase2Str(Str) OR SatLiqStr(Str))..

697 HSatLiq(Str) =E= (StdHtFormGas(’H2O’) + 1.0E-3*(CpIGConstA(’H2O’)/5*(TSat(Str)**5 -

Tref**5)

698 + CpIGConstB(’H2O’)/4*(TSat(Str)**4 - Tref**4) + CpIGConstC(’H2O’)/3*(TSat(Str)**3 -

Tref**3)

699 + CpIGConstD(’H2O’)/2*(TSat(Str)**2 - Tref**2) + CpIGConstE(’H2O’)*(TSat(Str) - Tref

)) - LatHtVapP2(Str,’H2O’))/3600 ;

700

701 EqEnthSatVap(Str)$SatVapStr(Str)..

702 HSatVap(Str) =E= (StdHtFormGas(’H2O’) + 1.0E-3*(CpIGConstA(’H2O’)/5*(TSat(Str)**5 -

Tref**5)

703 + CpIGConstB(’H2O’)/4*(TSat(Str)**4 - Tref**4) + CpIGConstC(’H2O’)/3*(TSat(Str)**3 -

Tref**3)

704 + CpIGConstD(’H2O’)/2*(TSat(Str)**2 - Tref**2) + CpIGConstE(’H2O’)*(TSat(Str) - Tref

)))/3600 ;

705

706

707 EqTSat(Str)$(Phase2Str(Str) OR SatLiqStr(Str) OR SatVapStr(Str))..

708 P(Str) =E= exp(ExtAnt1(’H2O’) + ExtAnt2(’H2O’)/(TSat(Str) + ExtAnt3(’H2O’)) + ExtAnt

4(’H2O’)*TSat(Str)

709 + ExtAnt5(’H2O’)*log(TSat(Str)) + ExtAnt6(’H2O’)*TSat(Str)**ExtAnt7(’H2O’)) ;

710

711

712 EqEnthP2Str(Str)$Phase2Str(Str)..

713 H(Str) =E= (1-Wetns(Str))*HVap(Str) + Wetns(Str)*HSatLiq(Str) ;

714

715

716 EqTP2(Str)$Phase2Str(Str)..

717 T(Str) =G= TSat(Str) ;

718

719 EqLogP21(Str)$Phase2Str(Str)..

720 Wetns(Str) =L= YP2(Str) ;

721


723 Wetns(Str) =G= EpsP2*YP2(Str) ;

724


726 T(Str) =L= TSat(Str) + BigMforT*(1-YP2(Str)) ;

727

728 EqTrP2(Str)$(Phase2Str(Str) OR SatLiqStr(Str))..

729 TrP2(Str) =E= TSat(Str)/Tc(’H2O’) ;

730

731

732 EqLatHtVapP2(Str,’H2O’)$(Phase2Str(Str) OR SatLiqStr(Str))..

733 LatHtVapP2(Str,’H2O’) =E= LatHt1(’H2O’)*(1 - TrP2(Str))**(LatHt2(’H2O’) + LatHt3(’H2O

’)*TrP2(Str)

734 + LatHt4(’H2O’)*TrP2(Str)**2 + LatHt5(’H2O’)*TrP2(Str)**3) ;

model.lst Wed May 30 15:17:17 2018 19

735

736

737

738 *** equation for H of saturated liquid stream

739

740 EqEnthSatLiq1(Str)$SatLiqStr(Str)..

741 H(Str) =E= HSatLiq(Str) ;

742

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743 EqnTfSatLiqVap(Str)$(SatLiqStr(Str) OR SatVapStr(Str))..

744 T(Str) =E= TSat(Str) ;

745

746

747 *** equations for H of (subcooled) liquid streams

748

749 EqEnthLiqStr(Str)$LiqStr(Str)..

750 H(Str) =E= (StdHtFormGas(’H2O’) + 1.0E-3*(CpIGConstA(’H2O’)/5*(T(Str)**5 - Tref**5)

751 + CpIGConstB(’H2O’)/4*(T(Str)**4 - Tref**4) + CpIGConstC(’H2O’)/3*(T(Str

)**3 - Tref**3)

752 + CpIGConstD(’H2O’)/2*(T(Str)**2 - Tref**2) + CpIGConstE(’H2O’)*(T(Str)

- Tref)) - LatHtVapLiq(Str,’H2O’))/3600 ;

753

754 EqTrLiq(Str)$LiqStr(Str)..

755 TrLiq(Str) =E= T(Str)/Tc(’H2O’) ;

756

757

758 EqLatHtVapLiq(Str,’H2O’)$LiqStr(Str)..

759 LatHtVapLiq(Str,’H2O’) =E= LatHt1(’H2O’)*(1 - TrLiq(Str))**(LatHt2(’H2O’) + LatHt3(’H

2O’)*TrLiq(Str)

760 + LatHt4(’H2O’)*TrLiq(Str)**2 + LatHt5(’H2O’)*TrLiq(Str)**3)

;

761

762

763 *** equations for H of saturated vapour streams

764 EqEnthSatVap1(Str)$SatVapStr(Str)..

765 H(Str) =E= HSatVap(Str) ;

766

767

768

769

770 *****************************************************

771 * Equations for HP Steam Turbine

772 *****************************************************

773 Equations

774 EqCompMolBalHPStmTurb(HPStmTurb,Comp) Component mol balance

775

776 EqInHPPHPStmTurb(HPStmTurb) Equating inlet HP Pressure to that of corresponding HP str

eam

777 EqInHPTHPStmTurb(HPStmTurb) Equating inlet HP temperature to that of corresponding HP

stream

778

779 EqOutMPPHPStmTurb(HPStmTurb) Equatiing outlet MP Pressure to that of corresponding MP

stream

780 EqOutLPPHPStmTurb(HPStmTurb) Equatiing outlet LP Pressure to that of corresponding LP

stream

781

782 EqPTRel1HPStmTurb(HPStmTurb) P T relationship for compression from high to medium pres

sure

783

784 EqPTRel1aHPStmTurb(HPStmTurb)

785 EqPTRel1bHPStmTurb(HPStmTurb)

786 EqPTRel1cHPStmTurb(HPStmTurb)

787 EqPTRel1dHPStmTurb(HPStmTurb)

788 EqPTRel1eHPStmTurb(HPStmTurb)

789 EqPTRel1fHPStmTurb(HPStmTurb)

model.lst Wed May 30 15:17:17 2018 21

790 EqPTRel1gHPStmTurb(HPStmTurb)

791 EqPTRel1hHPStmTurb(HPStmTurb)

792 EqPTRel1iHPStmTurb(HPStmTurb)

793 EqPTRel1jHPStmTurb(HPStmTurb)

794 EqPTRel1kHPStmTurb(HPStmTurb)

795

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796

797 EqPTRel2HPStmTurb(HPStmTurb)

798

799 EqPTRel2aHPStmTurb(HPStmTurb)

800 EqPTRel2bHPStmTurb(HPStmTurb)

801 EqPTRel2cHPStmTurb(HPStmTurb)

802 EqPTRel2dHPStmTurb(HPStmTurb)

803 EqPTRel2eHPStmTurb(HPStmTurb)

804 EqPTRel2fHPStmTurb(HPStmTurb)

805 EqPTRel2gHPStmTurb(HPStmTurb)

806 EqPTRel2hHPStmTurb(HPStmTurb)

807 EqPTRel2iHPStmTurb(HPStmTurb)

808 EqPTRel2jHPStmTurb(HPStmTurb)

809 EqPTRel2kHPStmTurb(HPStmTurb)

810 EqPTRel2lHPStmTurb(HPStmTurb)

811 EqPTRel2mHPStmTurb(HPStmTurb)

812 EqPTRel2nHPStmTurb(HPStmTurb)

813

814

815

816

817 EqPTRel3HPStmTurb(HPStmTurb)

818 EqMPWorkHPStmTurb(HPStmTurb)

819 EqLPWorkHPStmTurb(HPStmTurb)

820 EqVPWorkHPStmTurb(HPStmTurb)

821 EqTotWorkHPStmTurb(HPStmTurb)

822 EqWetCnst1HPStmTurb(HPStmTurb)

823 EqWetCnst2HPStmTurb(HPStmTurb)

824 EqLogMode1HPStmTurb(HPStmTurb)







831 EqLogMode8HPStmTurb(HPStmTurb,ModeHPStmTurb)

832

833 EqLogBnd1HPStmTurb(HPStmTurb)



836 EqLogBnd4HPStmTurb(HPStmTurb,Str) ;

837

838 EqCompMolBalHPStmTurb(HPStmTurb,Comp)..

839 Sum(Str $InHPStmTurb(HPStmTurb,Str), Fc(Str,Comp) ) =E=

840 Sum(Str $OutMPHPStmTurb(HPStmTurb,Str), Fc(Str,Comp) ) +

841 Sum(Str $OutLPHPStmTurb(HPStmTurb,Str), Fc(Str,Comp) ) +

842 Sum(Str $OutVPHPStmTurb(HPStmTurb,Str), Fc(Str,Comp) ) ;

843

844 *****

845 EqInHPPHPStmTurb(HPStmTurb)..

846 Sum(Str $InHPStmTurb(HPStmTurb,Str), P(str)) =E= InHPPHPStmTurb(HPStmTurb) ;

847

848 EqInHPTHPStmTurb(HPStmTurb)..

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849 Sum(Str $InHPStmTurb(HPStmTurb,Str), T(str)) =E= InHPTHPStmTurb(HPStmTurb) ;

850

851 *****

852 EqOutMPPHPStmTurb(HPStmTurb)..

853 Sum(Str $OutMPHPStmTurb(HPStmTurb,Str), P(str)) =E= OutMPPHPStmTurb(HPStmTurb) ;

854

855 EqOutLPPHPStmTurb(HPStmTurb)..

856 Sum(Str $OutLPHPStmTurb(HPStmTurb,Str), P(str)) =E= OutLPPHPStmTurb(HPStmTurb) ;

857

858

859 EqPTRel1HPStmTurb(HPStmTurb)..

860 OutMPTHPStmTurb(HPStmTurb) =E= InHPTHPStmTurb(HPStmTurb)*((OutMPPHPStmTurb(HPStmTur

b)/InHPPHPStmTurb(HPStmTurb))**((gamma - 1.0)/gamma)) ;

861

862

863 EqPTRel1aHPStmTurb(HPStmTurb)..

864 OutMPTHPStmTurb(HPStmTurb) =E= Dum11HPStmTurb(HPStmTurb) + Dum22HPStmTurb(HPStmTur

b) ;

865

866 EqPTRel1bHPStmTurb(HPStmTurb)..

867 530.0 =E= Dum33HPStmTurb(HPStmTurb) + Dum44HPStmTurb(HPStmTurb) ;

868

869 EqPTRel1cHPStmTurb(HPStmTurb)..

870 Sum(Str $OutMPHPStmTurb(HPStmTurb,Str), T(str)) =E= Dum55HPStmTurb(HPStmTurb) + Du

m66HPStmTurb(HPStmTurb) ;

871

872 EqPTRel1dHPStmTurb(HPStmTurb)..

873 Dum55HPStmTurb(HPStmTurb) =E= Dum11HPStmTurb(HPStmTurb) ;

874

875 EqPTRel1eHPStmTurb(HPStmTurb)..


877

878

879 EqPTRel1fHPStmTurb(HPStmTurb)..

880 Dum55HPStmTurb(HPStmTurb) =L= UBT(’MP’)*SUM(Str $InHPStmTurb(HPStmTurb,Str), Y(Str))

;

881

882

883 EqPTRel1gHPStmTurb(HPStmTurb)..

884 Dum66HPStmTurb(HPStmTurb) =L= UBT(’MP’)*(1 - SUM(Str $InHPStmTurb(HPStmTurb,Str), Y(S

tr))) ;

885

886

887 EqPTRel1hHPStmTurb(HPStmTurb)..


;

889

890 EqPTRel1iHPStmTurb(HPStmTurb)..


tr))) ;

892

893 EqPTRel1jHPStmTurb(HPStmTurb)..


tr))) ;

895

896 EqPTRel1kHPStmTurb(HPStmTurb)..

model.lst Wed May 30 15:17:17 2018 24


;

898


900 OutLPTHPStmTurb(HPStmTurb) =E= OutMPTHPStmTurb(HPStmTurb)*((OutLPPHPStmTurb(HPStmTu

rb)/OutMPPHPStmTurb(HPStmTurb))**((gamma - 1.0)/gamma)) ;

901

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902 EqPTRel2aHPStmTurb(HPStmTurb)..

903 OutLPTHPStmTurb(HPStmTurb) =E= Dum1HPStmTurb(HPStmTurb) + Dum2HPStmTurb(HPStmTurb)

;

904

905 EqPTRel2bHPStmTurb(HPStmTurb)..

906 460.0 =E= Dum3HPStmTurb(HPStmTurb) + Dum4HPStmTurb(HPStmTurb) ;

907

908 EqPTRel2cHPStmTurb(HPStmTurb)..

909 Sum(Str $OutLPHPStmTurb(HPStmTurb,Str), T(str)) =E= Dum5HPStmTurb(HPStmTurb) + Dum

6HPStmTurb(HPStmTurb) ;

910

911 EqPTRel2dHPStmTurb(HPStmTurb)..


913

914 EqPTRel2eHPStmTurb(HPStmTurb)..


916

917 EqPTRel2fHPStmTurb(HPStmTurb)..

918 Dum5HPStmTurb(HPStmTurb) =L= UBT(’LP’)*YLP(HPStmTurb) ;

919

920 EqPTRel2gHPStmTurb(HPStmTurb)..

921 Dum6HPStmTurb(HPStmTurb) =L= UBT(’LP’)*(1 - YLP(HPStmTurb)) ;

922

923 EqPTRel2hHPStmTurb(HPStmTurb)..


925

926 EqPTRel2iHPStmTurb(HPStmTurb)..


928

929 EqPTRel2jHPStmTurb(HPStmTurb)..


931

932 EqPTRel2kHPStmTurb(HPStmTurb)..


934

935 EqPTRel2lHPStmTurb(HPStmTurb)..

936 (1 - YModeHPStmTurb(HPStmTurb,’LPExt’)) + YLP(HPStmTurb) =G= 1 ;

937

938 EqPTRel2mHPStmTurb(HPStmTurb)..

939 (1 - YModeHPStmTurb(HPStmTurb,’LPBkPr’)) + YLP(HPStmTurb) =G= 1 ;

940

941 EqPTRel2nHPStmTurb(HPStmTurb)..

942 (1 - YModeHPStmTurb(HPStmTurb,’VPCond’)) + YLP(HPStmTurb) =G= 1 ;

943


945 Sum(Str $OutVPHPStmTurb(HPStmTurb,Str), Wetns(str)) =E= 0.15 ;

946

947 *****

948

949 EqMPWorkHPStmTurb(HPStmTurb)..

950 MPWorkHPStmTurb(HPStmTurb) =E= Sum( Str $InHPStmTurb(HPStmTurb,Str), Fc(Str,’H2O’)

)*(

951 Sum( Str $InHPStmTurb(HPStmTurb,Str), H(Str)) - Sum( Str $OutMPHPStmTurb(HPStmTurb,

Str), H(Str))) ;

952

953 EqLPWorkHPStmTurb(HPStmTurb)..

model.lst Wed May 30 15:17:17 2018 26

954 LPWorkHPStmTurb(HPStmTurb) =E= (Sum(Str $InHPStmTurb(HPStmTurb,Str), Fc(Str,’H2O’)

)

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955 - Sum(Str $OutMPHPStmTurb(HPStmTurb,Str), Fc(Str,’H2O’)))

956 *(Sum( Str $OutMPHPStmTurb(HPStmTurb,Str), H(Str))

957 - Sum( Str $OutLPHPStmTurb(HPStmTurb,Str), H(Str))) ;

958

959 EqVPWorkHPStmTurb(HPStmTurb)..

960 VPWorkHPStmTurb(HPStmTurb) =E= (Sum(Str $InHPStmTurb(HPStmTurb,Str), Fc(Str,’H2O’)

)

961 - Sum(Str $OutMPHPStmTurb(HPStmTurb,Str), Fc(Str,’H2O’))

962 - Sum(Str $OutLPHPStmTurb(HPStmTurb,Str), Fc(Str,’H2O’)))

963 *(Sum( Str $OutLPHPStmTurb(HPStmTurb,Str), H(Str))

964 - Sum( Str $OutVPHPStmTurb(HPStmTurb,Str), H(Str))) ;

965

966 EqTotWorkHPStmTurb(HPStmTurb)..

967 TotWorkHPStmTurb(HPStmTurb) =E= MPWorkHPStmTurb(HPStmTurb) + LPWorkHPStmTurb(HPStm

Turb) + VPWorkHPStmTurb(HPStmTurb) ;

968

969

970 EqWetCnst1HPStmTurb(HPStmTurb)..

971 Sum( Str $OutMPHPStmTurb(HPStmTurb,Str), Wetns(Str)) =L= 0.15 ;

972

973 EqWetCnst2HPStmTurb(HPStmTurb)..

974 Sum( Str $OutLPHPStmTurb(HPStmTurb,Str), Wetns(Str)) =L= 0.15 ;

975

976 EqLogMode1HPStmTurb(HPStmTurb)..

977 (1 - YModeHPStmTurb(HPStmTurb,’MPExt’)) + YModeHPStmTurb(HPStmTurb,’LPBkPr’) + YMo

deHPStmTurb(HPStmTurb,’VPCond’) =G= 1 ;

978


980 (1 - YModeHPStmTurb(HPStmTurb,’LPExt’)) + YModeHPStmTurb(HPStmTurb,’VPCond’) =G= 1

;

981


983 YModeHPStmTurb(HPStmTurb,’LPExt’) + YModeHPStmTurb(HPStmTurb,’LPBkPr’) =L= 1 ;

984


986 YModeHPStmTurb(HPStmTurb,’MPExt’) + YModeHPStmTurb(HPStmTurb,’MPBkPr’) =L= 1 ;

987


989 YModeHPStmTurb(HPStmTurb,’LPBkPr’) + YModeHPStmTurb(HPStmTurb,’MPBkPr’) + YModeHPS

tmTurb(HPStmTurb,’VPCond’) =L= 1 ;

990

991 * extraction wet


993 Sum( Str $OutMPHPStmTurb(HPStmTurb,Str), Wetns(Str)) =L= 1 - YModeHPStmTurb(HPStmTu

rb,’MPExt’) ;

994


996 Sum( Str $OutLPHPStmTurb(HPStmTurb,Str), Wetns(Str)) =L= 1 - YModeHPStmTurb(HPStmTu

rb,’LPExt’) ;

997 *****

998

999 EqLogMode8HPStmTurb(HPStmTurb,ModeHPStmTurb)..

1000 (1 - YModeHPStmTurb(HPStmTurb,ModeHPStmTurb)) + Sum(Str $InHPStmTurb(HPStmTurb,Str)

, Y(Str)) =G= 1 ;

1001

1002 EqLogBnd1HPStmTurb(HPStmTurb)..

model.lst Wed May 30 15:17:17 2018 28

1003 Sum(Str $OutMPHPStmTurb(HPStmTurb,Str), F(Str)) =L= BigMforTurbFlow*

1004 (YModeHPStmTurb(HPStmTurb,’MPExt’) + YModeHPStmTurb(HPStmTurb,’MPBkPr’)) ;

1005


1007 Sum(Str $OutLPHPStmTurb(HPStmTurb,Str), F(Str)) =L= BigMforTurbFlow*

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1008 (YModeHPStmTurb(HPStmTurb,’LPExt’) + YModeHPStmTurb(HPStmTurb,’LPBkPr’)) ;

1009


1011 Sum(Str $OutVPHPStmTurb(HPStmTurb,Str), F(Str)) =L= BigMforTurbFlow*YModeHPStmTurb(

HPStmTurb,’VPCond’) ;

1012

1013 EqLogBnd4HPStmTurb(HPStmTurb,Str)$InHPStmTurb(HPStmTurb,Str)..

1014 F(str) =L= BigMforTurbFlow*Y(Str) ;

1015

1016

1017

1018

1019 *****************************************************

1020 * Equations for MP Steam Turbine

1021 *****************************************************

1022 Equations

1023 EqCompMolBalMPStmTurb(MPStmTurb,Comp) Component mol balance

1024

1025 EqInMPPMPStmTurb(MPStmTurb) Equating inlet HP Pressure to that of corresponding HP str

eam

1026 EqInMPTMPStmTurb(MPStmTurb) Equating inlet HP temperature to that of corresponding HP

stream

1027

1028 EqOutLPPMPStmTurb(MPStmTurb) Equatiing outlet LP Pressure to that of corresponding LP

stream

1029

1030

1031

1032

1033

1034 EqPTRel1MPStmTurb(MPStmTurb)

1035

1036 EqPTRel1aMPStmTurb(MPStmTurb)

1037 EqPTRel1bMPStmTurb(MPStmTurb)

1038 EqPTRel1cMPStmTurb(MPStmTurb)

1039 EqPTRel1dMPStmTurb(MPStmTurb)

1040 EqPTRel1eMPStmTurb(MPStmTurb)

1041 EqPTRel1fMPStmTurb(MPStmTurb)

1042 EqPTRel1gMPStmTurb(MPStmTurb)

1043 EqPTRel1hMPStmTurb(MPStmTurb)

1044 EqPTRel1iMPStmTurb(MPStmTurb)

1045 EqPTRel1jMPStmTurb(MPStmTurb)

1046 EqPTRel1kMPStmTurb(MPStmTurb)

1047

1048 EqPTRel2MPStmTurb(MPStmTurb)

1049

1050 EqLPWorkMPStmTurb(MPStmTurb)

1051 EqVPWorkMPStmTurb(MPStmTurb)

1052 EqTotWorkMPStmTurb(MPStmTurb)

1053

1054 EqWetCnst1MPStmTurb(MPStmTurb)

1055

1056 EqLogMode1MPStmTurb(MPStmTurb)




model.lst Wed May 30 15:17:17 2018 30

1060 EqLogMode5MPStmTurb(MPStmTurb,ModeMPStmTurb)

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1061

1062 EqLogBnd1MPStmTurb(MPStmTurb)

1063 EqLogBnd2MPStmTurb(MPStmTurb)

1064 EqLogBnd3MPStmTurb(MPStmTurb,Str) ;

1065

1066 EqCompMolBalMPStmTurb(MPStmTurb,Comp)..

1067 Sum(Str $InMPStmTurb(MPStmTurb,Str), Fc(Str,Comp) ) =E=

1068 Sum(Str $OutLPMPStmTurb(MPStmTurb,Str), Fc(Str,Comp) ) +

1069 Sum(Str $OutVPMPStmTurb(MPStmTurb,Str), Fc(Str,Comp) ) ;

1070

1071 *****

1072 EqInMPPMPStmTurb(MPStmTurb)..

1073 Sum(Str $InMPStmTurb(MPStmTurb,Str), P(str)) =E= InMPPMPStmTurb(MPStmTurb) ;

1074

1075 EqInMPTMPStmTurb(MPStmTurb)..

1076 Sum(Str $InMPStmTurb(MPStmTurb,Str), T(str)) =E= InMPTMPStmTurb(MPStmTurb) ;

1077

1078 *****

1079

1080 EqOutLPPMPStmTurb(MPStmTurb)..

1081 Sum(Str $OutLPMPStmTurb(MPStmTurb,Str), P(str)) =E= OutLPPMPStmTurb(MPStmTurb) ;

1082

1083

1084

1085 *****

1086

1087 EqPTRel1MPStmTurb(MPStmTurb)..

1088 OutLPTMPStmTurb(MPStmTurb) =E= InMPTMPStmTurb(MPStmTurb)*((OutLPPMPStmTurb(MPStmTur

b)/InMPPMPStmTurb(MPStmTurb))**((gamma - 1.0)/gamma)) ;

1089

1090 EqPTRel1aMPStmTurb(MPStmTurb)..

1091 OutLPTMPStmTurb(MPStmTurb) =E= Dum11MPStmTurb(MPStmTurb) + Dum22MPStmTurb(MPStmTur

b) ;

1092

1093 EqPTRel1bMPStmTurb(MPStmTurb)..

1094 460.0 =E= Dum33MPStmTurb(MPStmTurb) + Dum44MPStmTurb(MPStmTurb) ;

1095

1096 EqPTRel1cMPStmTurb(MPStmTurb)..

1097 Sum(Str $OutLPMPStmTurb(MPStmTurb,Str), T(str)) =E= Dum55MPStmTurb(MPStmTurb) + Du

m66MPStmTurb(MPStmTurb) ;

1098

1099 EqPTRel1dMPStmTurb(MPStmTurb)..

1100 Dum55MPStmTurb(MPStmTurb) =E= Dum11MPStmTurb(MPStmTurb) ;

1101

1102 EqPTRel1eMPStmTurb(MPStmTurb)..

1103 Dum66MPStmTurb(MPStmTurb) =E= Dum44MPStmTurb(MPStmTurb) ;

1104

1105

1106 EqPTRel1fMPStmTurb(MPStmTurb)..

1107 Dum55MPStmTurb(MPStmTurb) =L= UBT(’LP’)*SUM(Str $InMPStmTurb(MPStmTurb,Str), Y(Str))

;

1108

1109

1110 EqPTRel1gMPStmTurb(MPStmTurb)..

1111 Dum66MPStmTurb(MPStmTurb) =L= UBT(’LP’)*(1 - SUM(Str $InMPStmTurb(MPStmTurb,Str), Y(S

tr))) ;

model.lst Wed May 30 15:17:17 2018 32

1112

1113

model.lst Wed May 30 15:17:17 2018 33


05/30/18 15:17:15 Page 22



1114 EqPTRel1hMPStmTurb(MPStmTurb)..


;

1116

1117 EqPTRel1iMPStmTurb(MPStmTurb)..


tr))) ;

1119

1120 EqPTRel1jMPStmTurb(MPStmTurb)..


tr))) ;

1122

1123 EqPTRel1kMPStmTurb(MPStmTurb)..


;

1125

1126

1127 *****

1128

1129 EqPTRel2MPStmTurb(MPStmTurb)..

1130 Sum(Str $OutVPMPStmTurb(MPStmTurb,Str), Wetns(Str)) =E= 0.15 ;

1131

1132 *****

1133

1134 EqLPWorkMPStmTurb(MPStmTurb)..

1135 LPWorkMPStmTurb(MPStmTurb) =E= Sum(Str $InMPStmTurb(MPStmTurb,Str), Fc(Str,’H2O’))

1136 *(Sum( Str $InMPStmTurb(MPStmTurb,Str), H(Str))

1137 - Sum( Str $OutLPMPStmTurb(MPStmTurb,Str), H(Str))) ;

1138

1139 EqVPWorkMPStmTurb(MPStmTurb)..

1140 VPWorkMPStmTurb(MPStmTurb) =E= (Sum(Str $InMPStmTurb(MPStmTurb,Str), Fc(Str,’H2O’)

)

1141 - Sum(Str $OutLPMPStmTurb(MPStmTurb,Str), Fc(Str,’H2O’)))

1142 *(Sum( Str $OutLPMPStmTurb(MPStmTurb,Str), H(Str))

1143 - Sum( Str $OutVPMPStmTurb(MPStmTurb,Str), H(Str))) ;

1144

1145 EqTotWorkMPStmTurb(MPStmTurb)..

1146 TotWorkMPStmTurb(MPStmTurb) =E= LPWorkMPStmTurb(MPStmTurb) + VPWorkMPStmTurb(MPSt

mTurb) ;

1147

1148

1149 EqWetCnst1MPStmTurb(MPStmTurb)..

1150 Sum( Str $OutLPMPStmTurb(MPStmTurb,Str), Wetns(Str)) =L= 0.15 ;

1151

1152 EqLogMode1MPStmTurb(MPStmTurb)..

1153 (1 - YModeMPStmTurb(MPStmTurb,’LPExt’)) + YModeMPStmTurb(MPStmTurb,’VPCond’) =G= 1

;

1154


1156 YModeMPStmTurb(MPStmTurb,’LPExt’) + YModeMPStmTurb(MPStmTurb,’LPBkPr’) =L= 1 ;

1157


1159 YModeMPStmTurb(MPStmTurb,’LPBkPr’) + YModeMPStmTurb(MPStmTurb,’VPCond’) =L= 1 ;

1160

1161


model.lst Wed May 30 15:17:17 2018 34

1163 Sum( Str $OutLPMPStmTurb(MPStmTurb,Str), Wetns(Str)) =L= 1 - YModeMPStmTurb(MPStmTu

rb,’LPExt’) ;

1164

1165 EqLogMode5MPStmTurb(MPStmTurb,ModeMPStmTurb)..

1166 (1 - YModeMPStmTurb(MPStmTurb,ModeMPStmTurb)) + Sum(Str $InMPStmTurb(MPStmTurb,Str)

, Y(Str)) =G= 1 ;

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1167

1168

1169 EqLogBnd1MPStmTurb(MPStmTurb)..

1170 Sum(Str $OutLPMPStmTurb(MPStmTurb,Str), F(Str)) =L= BigMforTurbFlow*

1171 (YModeMPStmTurb(MPStmTurb,’LPExt’) + YModeMPStmTurb(MPStmTurb,’LPBkPr’)) ;

1172

1173 EqLogBnd2MPStmTurb(MPStmTurb)..

1174 Sum(Str $OutVPMPStmTurb(MPStmTurb,Str), F(Str)) =L= BigMforTurbFlow*YModeMPStmTurb(

MPStmTurb,’VPCond’) ;

1175

1176 EqLogBnd3MPStmTurb(MPStmTurb,Str)$InMPStmTurb(MPStmTurb,Str)..

1177 F(str) =L= BigMforTurbFlow*Y(Str) ;

1178

1179

1180

1181 *****************************************

1182 ** Equation for vacuum condensor

1183 *****************************************

1184 Equations

1185

1186 EqCompMolBalVacCondTurb(VacCondTurb,Comp) Component mass bal

1187 EqEnthBalVacCondTurb(VacCondTurb) Energy balance

1188 EqMassFCW(VacCondTurb) calculate mass flowrate of cooling water (

kg per s)

1189 EqPr1VacCondTurb(VacCondTurb,Str) equates Vacuum pressure to pressure of inl

et stream

1190 EqPr2VacCondTurb(VacCondTurb,Str) equates Vacuum pressure to pressure of out

let stream

1191 EqWorkPumpVCT(VacCondTurb) Work for vacuum pump in MW (mass is kg pe

r s)

1192

1193 ;

1194

1195

1196 EqCompMolBalVacCondTurb(VacCondTurb,Comp)..

1197 Sum(Str $InVacCondTurb(VacCondTurb,Str), Fc(Str,Comp)) =E= Sum(Str $OutVacCondTurb(Va

cCondTurb,Str), Fc(Str,Comp)) ;

1198

1199

1200 EqEnthBalVacCondTurb(VacCondTurb)..

1201 HtLdVacCondTurb(VacCondTurb) =E= Sum(Str $InVacCondTurb(VacCondTurb,Str), F(Str)*H(St

r)) -

1202 Sum(Str $OutVacCondTurb(VacCondTurb,Str), F(Str)*H(S

tr)) ;

1203

1204 EqMassFCW(VacCondTurb)..

1205 HtLdVacCondTurb(VacCondTurb) =E= MassFCW*4.184E-03*20 ;

1206

1207 EqPr1VacCondTurb(VacCondTurb,Str)$InVacCondTurb(VacCondTurb,Str)..

1208 P(Str) =E= FxPL(’VP’) ;

1209

1210 EqPr2VacCondTurb(VacCondTurb,Str)$OutVacCondTurb(VacCondTurb,Str)..

1211 P(Str) =E= FxPL(’VP’) ;

1212

1213 EqWorkPumpVCT(VacCondTurb)..

1214 WorkPumpVCT =E= MassFCW*0.69/1000 ;

model.lst Wed May 30 15:17:17 2018 36

1215

1216

1217

1218

1219 *****************************************

model.lst Wed May 30 15:17:17 2018 37


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1220 ** Equation for pumps

1221 *****************************************

1222

1223 Equations

1224

1225 EqCompMolBalPump(Pump,Comp) Component mass bal

1226 EqTEqPump(Pump) Tin = Tout

1227 EqPgePump(Pump) Pout >= Pin

1228 EqWorkPump(Pump) Work done by pump

1229

1230 ;

1231

1232 EqCompMolBalPump(Pump,Comp)..

1233 Sum(Str $InPump(Pump,Str), Fc(Str,Comp)) =E= Sum(Str $OutPump(Pump,Str), Fc(Str,Co

mp)) ;

1234

1235 EqTEqPump(Pump)..

1236 Sum(Str $InPump(Pump,Str), T(Str)) =E= Sum(Str $OutPump(Pump,Str), T(Str)) ;

1237

1238 EqPgePump(Pump)..

1239 Sum(Str $OutPump(Pump,Str), P(Str)) =G= Sum(Str $InPump(Pump,Str), P(Str)) ;

1240

1241

1242 EqWorkPump(Pump)..

1243 WorkPump(Pump) =E= Sum(Str $InPump(Pump,Str), F(Str) )*(

1244 Sum(Str $OutPump(Pump,Str), P(Str)) -

1245 Sum(Str $InPump(Pump,Str), P(Str)))*0.1*18/(3600*1000) ;

1246

1247

1248

1249 *****************************************

1250 ** Equation for condensate header

1251 *****************************************

1252 Equations

1253

1254 EqCompMolBalCondHdr(CondHdr,Comp) Component mass bal

1255 EqPRel1CondHdr(CondHdr) Pressure of outlet stream equals the pressure of header

1256

1257 ;

1258

1259 EqCompMolBalCondHdr(CondHdr,Comp)..

1260 Sum(Str $InCondHdr(CondHdr,Str), Fc(Str,Comp)) =E= Sum(Str $OutCondHdr(CondHdr,Str),

Fc(Str,Comp)) ;

1261

1262 EqPRel1CondHdr(CondHdr)..

1263 Sum(Str $OutCondHdr(CondHdr,Str), P(Str)) =E= FxPL(’CDP’) ;

1264

1265

1266

1267

1268

1269

1270

1271 *****************************************

1272 ** Equation for Deaerator

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1273 *****************************************

1274 Equations

1275 EqCompMolBalDeAertr(DeAertr,Comp)

1276 EqEnthBalDeAertr(DeAertr)

1277 EqVentVapDeAertr(DeAertr)

1278 EqPRel1DeAertr(DeAertr,Str)

1279 EqPRel2DeAertr(DeAertr,Str)

1280 ;

1281

1282

1283 EqCompMolBalDeAertr(DeAertr,Comp)..

1284 Sum(Str $InDeAertr(DeAertr,Str), Fc(Str,Comp)) =E=

1285 Sum(Str $OutLDeAertr(DeAertr,Str), Fc(Str,Comp)) +

1286 Sum(Str $OutVDeAertr(DeAertr,Str), Fc(Str,Comp)) ;

1287

1288 EqEnthBalDeAertr(DeAertr)..

1289 Sum(Str $InDeAertr(DeAertr,Str), F(Str)*H(Str)) =E=

1290 Sum(Str $OutLDeAertr(DeAertr,Str), F(Str)*H(Str)) +

1291 Sum(Str $OutVDeAertr(DeAertr,Str), F(Str)*H(Str)) ;

1292

1293 EqVentVapDeAertr(DeAertr)..

1294 Sum(Str $OutVDeAertr(DeAertr,Str), Fc(Str,’H2O’)) =E= 0.005*Sum(Str $InDeAertr(DeAert

r,Str), Fc(Str,’H2O’)) ;

1295

1296 EqPRel1DeAertr(DeAertr,Str)$OutVDeAertr(DeAertr,Str)..

1297 P(Str) =E= FxPL(’CDP’) ;

1298

1299 EqPRel2DeAertr(DeAertr,Str)$OutLDeAertr(DeAertr,Str)..

1300 P(Str) =E= FxPL(’CDP’) ;

1301

1302

1303

1304 *****************************************************

1305 * Equations for Combuster

1306 *****************************************************

1307 Equations

1308 EqCompMolBalBlrCmbtr(BlrCmbtr,Comp) Component mol balance

1309 EqDum1BlrCmbtr(BlrCmbtr,Comp) Dummy (calculates inlet flow for particular component

)

1310 EqEgyBalBlrCmbtr(BlrCmbtr) Energy balance for combustor

1311 EqOutPBlrCmbtr1(BlrCmbtr,Str) Equality of pressure

1312

1313 EqExcessO2BlrCmbtr(BlrCmbtr) constraint for excess O2

1314 EqTCnstrtBlrCmbtr(BlrCmbtr) Constraint for maximum allowable temperature

1315

1316 ;

1317

1318

1319

1320 EqDum1BlrCmbtr(BlrCmbtr,Comp)..

1321 Dum1BlrCmbtr(BlrCmbtr,Comp) =E= Sum(Str $InBlrCmbtr(BlrCmbtr,Str),Fc(Str,Comp))

;

1322

1323 EqCompMolBalBlrCmbtr(BlrCmbtr,Comp)..

1324 Dum1BlrCmbtr(BlrCmbtr,Comp) +

1325 Sum(CombRxns,Sum(Comp2$BurnComp(CombRxns,Comp2),FracConv(Comp2)*Dum1BlrCmbtr(BlrCmb

model.lst Wed May 30 15:17:17 2018 39

tr,Comp2)*CombRxnsStoicMtrx(CombRxns,Comp)))

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1326 =E= Sum(Str $OutBlrCmbtr(BlrCmbtr,Str),Fc(Str,Comp)) ;

1327

1328

1329 EqEgyBalBlrCmbtr(BlrCmbtr)..

1330 Sum(Str $InBlrCmbtr(BlrCmbtr,Str), SUM(Comp, Fc(Str,Comp)*Hc(Str,Comp)))

1331 =E= Sum(Str $OutBlrCmbtr(BlrCmbtr,Str), SUM(Comp, Fc(Str,Comp)*Hc(Str,Comp))) ;

1332

1333 EqOutPBlrCmbtr1(BlrCmbtr,Str)$InBlrCmbtr(BlrCmbtr,Str)..

1334 Sum(Str2 $OutBlrCmbtr(BlrCmbtr,Str2), P(Str2)) =E= P(Str) ;

1335

1336 EqExcessO2BlrCmbtr(BlrCmbtr)..

1337 Dum1BlrCmbtr(BlrCmbtr,’O2’) =G= 1.15*

1338 Sum(CombRxns,Sum(Comp2$BurnComp(CombRxns,Comp2),Dum1BlrCmbtr(BlrCmbtr,Comp2)*CombRx

nsStoicMtrx(CombRxns,’O2’))) ;

1339

1340 EqTCnstrtBlrCmbtr(BlrCmbtr)..

1341 Sum(Str $OutBlrCmbtr(BlrCmbtr,Str),T(Str)) =L= 1500 ;

1342

1343

1344

1345

1346 *****************************************

1347 ** Equation for Air and syngas streams

1348 *****************************************

1349 Equations

1350 Eq1AirStr(Str)

1351 Eq2AirStr(Str)

1352 Eq3AirStr(Str)

1353 Eq1SyngasStr(Str)

1354 Eq1aSyngasStr(Str)

1355 Eq1bSyngasStr(Str)

1356

1357 Eq2SyngasStr(Str)

1358 EqWorkFan

1359 ;

1360 Eq1AirStr(Str)$AirStr(Str)..

1361 Fc(Str,’N2’) =E= 79/21 * Fc(Str,’O2’) ;

1362


1364 P(Str) =E= AmbP ;

1365


1367 T(Str) =E= AmbT ;

1368

1369 Eq1SyngasStr(Str)$SyngasStr(Str)..

1370 Fc(Str,’H2’) =E= 11.0 * Fc(Str,’CO2’) ;

1371

1372 Eq1aSyngasStr(Str)$SyngasStr(Str)..

1373 Fc(Str,’CO’) =E= 6.0 * Fc(Str,’CO2’) ;

1374

1375 Eq1bSyngasStr(Str)$SyngasStr(Str)..

1376 Fc(Str,’CH4’) =E= 2.0 * Fc(Str,’CO2’) ;

1377

1378 Eq2SyngasStr(Str)$SyngasStr(Str)..

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1379 T(Str) =E= AmbT ;

1380

1381 EqWorkFan..

1382 WorkFan =E= (F(’27’)+F(’29’))*29*0.012/(3600*1.186) ;

1383

1384

1385

1386

1387

1388

1389

1390

1391

1392

1393

1394

1395

1396 **********************************

1397 * Euqation for Header

1398 **********************************

1399 Equations

1400

1401 EqTSat2(PLev)

1402 EqUBTOpr(PLev)

1403 EqLBTOpr(PLev)

1404 EqCompMolBalPLev(PLev,Comp)

1405 EqEgyBalPLev(PLev)

1406 EqPRel1PLev(PLev,Str)

1407 EqPRel2PLev(PLev,Str)

1408 EqTRel1PLev(PLev,Str)

1409

1410 ;

1411

1412

1413 EqCompMolBalPLev(PLev,Comp)..

1414 Sum( Str $InPLev(PLev,Str), Fc(Str,Comp)) =E=

1415 Sum( Str $OutPLev(PLev,Str), Fc(Str,Comp)) ;

1416

1417 EqEgyBalPLev(PLev)..

1418 Sum( Str $InPLev(PLev,Str), F(Str)* H(Str)) =E=

1419 Sum( Str $OutPLev(PLev,Str), F(Str)* H(Str)) ;

1420

1421 EqPRel1PLev(PLev,Str)$InPLev(PLev,Str)..

1422 P(Str) =E= POpr(PLev) ;

1423

1424 EqPRel2PLev(PLev,Str)$OutPLev(PLev,Str)..

1425 P(Str) =E= POpr(PLev) ;

1426

1427 EqTRel1PLev(PLev,Str)$OutPLev(PLev,Str)..

1428 T(Str) =E= TOpr(PLev) ;

1429

1430 EqTSat2(PLev)..

1431 POpr(PLev) =E= exp(ExtAnt1(’H2O’) + ExtAnt2(’H2O’)/(TSatOpr(PLev) + ExtAnt3(’H2O’))

+ ExtAnt4(’H2O’)*TSatOpr(PLev)

model.lst Wed May 30 15:17:17 2018 42


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1432 + ExtAnt5(’H2O’)*log(TSatOpr(PLev)) + ExtAnt6(’H2O’)*TSatOpr(PLev)**ExtAnt7(’H2O’))

;

1433

1434 EqUBTOpr(PLev)..

1435 TOpr(PLev) =L= TSatOpr(PLev) + MaxSupHt(PLev) ;

1436

1437 EqLBTOpr(PLev)..

1438 TOpr(PLev) =G= TSatOpr(PLev) ;

1439

1440

1441

1442 *****************************************************

1443 * Equations for Boilers

1444 *****************************************************

1445 Equations

1446 EqGasMolBalBlr(Blr,Comp)

1447 EqWtrMolBalBlr(Blr,Comp)

1448 EqGasEgyBalBlr(Blr)

1449 EqWtrEgyBalBlr(Blr)

1450 EqBlowdown(Blr)

1451

1452 EqRel2Blr(Blr)

1453 EqRel3Blr(Blr)

1454 EqRel4Blr(Blr)

1455 EqRel5Blr(Blr)

1456 EqRel6Blr(Blr)

1457

1458 *EqP1

1459 *EqP2

1460 *EqP3

1461 EqT1

1462 EqT2

1463 EqT3

1464 ;

1465

1466 EqGasMolBalBlr(Blr,Comp)..

1467 Sum(Str $InGasBlr(Blr,Str), Fc(Str,Comp)) =E=

1468 Sum(Str $OutGasBlr(Blr,Str), Fc(Str,Comp)) ;

1469

1470 EqWtrMolBalBlr(Blr,Comp)..

1471 Sum(Str $InWtrBlr(Blr,Str), Fc(Str,Comp)) =E=

1472 Sum(Str $OutStmBlr(Blr,Str), Fc(Str,Comp)) + Sum(Str $OutWtrBlr(Blr,Str), Fc(Str,Com

p)) ;

1473

1474 EqGasEgyBalBlr(Blr)..

1475 Sum(Str $InGasBlr(Blr,Str), SUM(Comp, Fc(Str,Comp)*Hc(Str,Comp))) - QBlr(Blr) =E=

1476 Sum(Str $OutGasBlr(Blr,Str), SUM(Comp, Fc(Str,Comp)*Hc(Str,Comp))) ;

1477

1478 EqWtrEgyBalBlr(Blr)..

1479 Sum(Str $InWtrBlr(Blr,Str), F(Str)*H(Str)) + QBlr(Blr) =E=

1480 Sum(Str $OutStmBlr(Blr,Str), F(Str)*H(Str)) + Sum(Str $OutWtrBlr(Blr,Str), F(Str)*H(

Str)) ;

1481

1482 EqBlowdown(Blr)..

1483 Sum(Str $OutWtrBlr(Blr,Str), F(Str)) =E= 0.03*Sum(Str $InWtrBlr(Blr,Str), F(Str)) ;

1484

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1485

1486 EqRel2Blr(Blr)..

1487 Sum(Str $InGasBlr(Blr,Str), T(Str)) =G= Sum(Str $OutStmBlr(Blr,Str), T(Str)) + EM

AT ;

1488


1490 Sum(Str $OutGasBlr(Blr,Str), T(Str)) =G= Sum(Str $InWtrBlr(Blr,Str), T(Str)) + EMA

T ;

1491


1493 Sum(Str $InGasBlr(Blr,Str), P(Str)) =E=

1494 Sum(Str $OutGasBlr(Blr,Str), P(Str)) ;

1495


1497 Sum(Str $InWtrBlr(Blr,Str), P(Str)) =E= Sum(Str $OutStmBlr(Blr,Str), P(Str)) ;

1498


1500 Sum(Str $OutWtrBlr(Blr,Str), P(Str)) =E= Sum(Str $OutStmBlr(Blr,Str), P(Str)) ;

1501

1502 EqT1..

1503 T(’25’) =L= TOpr(’MP’)+ MaxSupHt(’MP’) ;

1504

1505 EqT2..

1506 T(’26’) =L= TOpr(’HP’)+ MaxSupHt(’HP’) ;

1507

1508 EqT3..

1509 T(’47’) =L= TOpr(’HP’)+ MaxSupHt(’HP’) ;

1510

1511

1512 *****************************************************

1513 * Equations for Steam Demand

1514 *****************************************************

1515 Equations

1516 EqCompMolBalStmDmd(StmDmd,Comp)

1517 EqEgyBalStmDmd(StmDmd)

1518 EqPRel1StmDmd(StmDmd)

1519 EqHtReqStmDmd(StmDmd)

1520 EqPen1StmDmd(StmDmd)

1521 ;

1522 EqCompMolBalStmDmd(StmDmd,Comp)..

1523 Sum(Str $InStmDmd(StmDmd,Str), Fc(Str,Comp)) =E=

1524 Sum(Str $OutStmDmd(StmDmd,Str), Fc(Str,Comp)) ;

1525

1526

1527 EqEgyBalStmDmd(StmDmd)..

1528 Sum(Str $InStmDmd(StmDmd,Str), F(Str)*H(Str)) - Sum(Str $OutStmDmd(StmDmd,Str), F(

Str)*H(Str)) =E=

1529 0.9999*Sum(Str $OutStmDmd(StmDmd,Str), F(Str)*LatHtVapP2(Str,’H2O’))/3600 + WasteH(S

tmDmd) ;

1530

1531 EqPRel1StmDmd(StmDmd)..

1532 Sum(Str $InStmDmd(StmDmd,Str), P(Str)) =E=

1533 Sum(Str $OutStmDmd(StmDmd,Str), P(Str)) ;

1534

1535 EqHtReqStmDmd(StmDmd)..

1536 0.9999*Sum(Str $OutStmDmd(StmDmd,Str), F(Str)*LatHtVapP2(Str,’H2O’))/3600 =G= HtReq(

model.lst Wed May 30 15:17:17 2018 45

StmDmd) ;

1537

model.lst Wed May 30 15:17:17 2018 46


05/30/18 15:17:15 Page 30



1538 EqPen1StmDmd(StmDmd)..

1539 WasteH(StmDmd) =E= MassFCW1(StmDmd)*4.184E-03*20 ;

1540

1541

1542

1543

1544

1545

1546 *****************************************************

1547 * Equations for Compressor

1548 *****************************************************

1549 Equations

1550 EqCompMolBalGTCmpr(GTCmpr,Comp) Component mol balance

1551 EqOutPGTCmpr(GTCmpr) Equate outlet P of compressor to that of outlet stream

1552 EqOutTGTCmpr(GTCmpr) Equate outlet T of compressor to that of outlet stream

1553 EqInPGTCmpr(GTCmpr) Equate inlet P of compressor to that of inlet stream

1554 EqInTGTCmpr(GTCmpr) Equate inlet T of compressor to that of inlet stream

1555 EqPTRelGTCmpr(GTCmpr) P-T relationship (adiabatic)

1556 EqWorkGTCmpr(GTCmpr) Calculation of work of compression (ideal) (MW)

1557 EqPRelGtCmpr(GTCmpr) Pout >= Pin ;

1558

1559

1560 EqCompMolBalGTCmpr(GTCmpr,Comp)..

1561 Sum( Str $InGTCmpr(GTCmpr,Str), Fc(Str,Comp) ) =E=

1562 Sum( Str $OutGTCmpr(GTCmpr,Str), Fc(Str,Comp) ) ;

1563

1564 EqOutPGTCmpr(GTCmpr)..

1565 Sum(Str $OutGTCmpr(GTCmpr,Str), P(str)) =E= OutPGTCmpr(GTCmpr) ;

1566

1567 EqOutTGTCmpr(GTCmpr)..

1568 Sum(Str $OutGTCmpr(GTCmpr,Str), T(str)) =E= OutTGTCmpr(GTCmpr) ;

1569

1570

1571 EqInPGTCmpr(GTCmpr)..

1572 Sum(Str $InGTCmpr(GTCmpr,Str), P(str)) =E= InPGTCmpr(GTCmpr) ;

1573

1574 EqInTGTCmpr(GTCmpr)..

1575 Sum(Str $InGTCmpr(GTCmpr,Str), T(str)) =E= InTGTCmpr(GTCmpr) ;

1576

1577 EqPTRelGTCmpr(GTCmpr)..

1578 OutTGTCmpr(GTCmpr) =E= InTGTCmpr(GTCmpr)* ((OutPGTCmpr(GTCmpr)/InPGTCmpr(GTCmpr))**

((gamma - 1.0)/gamma)) ;

1579

1580 EqWorkGTCmpr(GTCmpr)..

1581 WorkGTCmpr(GTCmpr) =E= Sum(Str $OutGTCmpr(GTCmpr,Str), SUM(Comp, Fc(Str,Comp)*Hc(

Str,Comp))) -

1582 Sum(Str $InGTCmpr(GTCmpr,Str), SUM(Comp, Fc(Str,Comp)*Hc(

Str,Comp))) ;

1583

1584

1585 EqPRelGTCmpr(GTCmpr)..

1586 OutPGTCmpr(GTCmpr) =G= InPGTCmpr(GTCmpr) ;

1587

1588

1589

1590

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1591 *****************************************************

1592 * Equations for Expander

1593 *****************************************************

1594

1595 Equations

1596 EqCompMolBalGTExpdr(GTExpdr,Comp) Component mol balance

1597 EqOutPGTExpdr(GTExpdr) Equate outlet P of compressor to that of outlet stream

1598 EqOutTGTExpdr(GTExpdr) Equate outlet T of compressor to that of outlet stream

1599 EqInPGTExpdr(GTExpdr) Equate inlet P of compressor to that of inlet stream

1600 EqInTGTExpdr(GTExpdr) Equate inlet T of compressor to that of inlet stream

1601 EqPTRelGTExpdr(GTExpdr) P-T relationship (adiabatic)

1602 EqWorkGTExpdr(GTExpdr) Calculation of work of compression (ideal) (MW)

1603 EqPRelGTExpdr(GTExpdr) Pout <= Pin

1604 EqWorkGT ;

1605

1606 EqCompMolBalGTExpdr(GTExpdr,Comp)..

1607 Sum( Str $InGTExpdr(GTExpdr,Str), Fc(Str,Comp) ) =E=

1608 Sum( Str $OutGTExpdr(GTExpdr,Str), Fc(Str,Comp) ) ;

1609

1610 EqOutPGTExpdr(GTExpdr)..

1611 Sum(Str $OutGTExpdr(GTExpdr,Str), P(str)) =E= OutPGTExpdr(GTExpdr) ;

1612

1613 EqOutTGTExpdr(GTExpdr)..

1614 Sum(Str $OutGTExpdr(GTExpdr,Str), T(str)) =E= OutTGTExpdr(GTExpdr) ;

1615

1616

1617 EqInPGTExpdr(GTExpdr)..

1618 Sum(Str $InGTExpdr(GTExpdr,Str), P(str)) =E= InPGTExpdr(GTExpdr) ;

1619

1620 EqInTGTExpdr(GTExpdr)..

1621 Sum(Str $InGTExpdr(GTExpdr,Str), T(str)) =E= InTGTExpdr(GTExpdr) ;

1622

1623 EqPTRelGTExpdr(GTExpdr)..

1624 OutTGTExpdr(GTExpdr) =E= InTGTExpdr(GTExpdr)* ((OutPGTExpdr(GTExpdr)/InPGTExpdr(GTE

xpdr))**((gamma - 1.0)/gamma)) ;

1625

1626 EqWorkGTExpdr(GTExpdr)..

1627 WorkGTExpdr(GTExpdr) =E= Sum(Str $InGTExpdr(GTExpdr,Str), SUM(Comp, Fc(Str,Comp)*

Hc(Str,Comp))) -

1628 Sum(Str $OutGTExpdr(GTExpdr,Str), SUM(Comp, Fc(Str,Comp)*

Hc(Str,Comp))) ;

1629

1630 EqPRelGTExpdr(GTExpdr)..

1631 OutPGTExpdr(GTExpdr) =L= InPGTExpdr(GTExpdr) ;

1632

1633 EqWorkGT..

1634 WorkGT =E= WorkGTExpdr(’1’) - 1.0*WorkGTCmpr(’1’) ;

1635

1636

1637

1638 *****************************************

1639 ** Equation for Valves

1640 *****************************************

1641 Equations

1642 EqMolBalVlv(Vlv,Comp)

1643 EqEgyBalVlv(Vlv);

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1644

1645 EqMolBalVlv(Vlv,Comp)..

1646 Sum(Str $InVlv(Vlv,Str), Fc(Str,Comp)) =E=

1647 Sum(Str $OutVlv(Vlv,Str), Fc(Str,Comp)) ;

1648

1649 EqEgyBalVlv(Vlv)..

1650 Sum(Str $InVlv(Vlv,Str), F(Str)* H(Str)) =E=

1651 Sum(Str $OutVlv(Vlv,Str), F(Str)* H(Str)) ;

1652

1653

1654 *****************************************

1655 ** Equation to be changed later

1656 *****************************************

1657 Equations

1658 Eqstpd2

1659 Eqstpd3

1660 Eqstpd3a

1661 Eqstpd4

1662 Eqstpd5(MechDmd)


1664 Eqstpd7(HPStmTurb)

1665 Eqstpd8(MPStmTurb)




1669 Eqstpd12(HPStmTurb,MechDmd)

1670 Eqstpd13(MPStmTurb,MechDmd)

1671 Eqstpd14



1674 Eqstpd17(MPStmTurb)

1675

1676 ;

1677

1678 *$ontext

1679 Eqstpd2..

1680 F(’39’) =L= 13*F(’41’) ;

1681

1682 Eqstpd3..

1683 F(’27’) =L= 13*F(’28’) ;

1684

1685 Eqstpd3a..

1686 F(’29’) =L= 13*F(’30’) ;

1687

1688 Eqstpd4..

1689 ElecDmd + WorkFan + SUM(Pump,WorkPump(Pump)) + WorkPumpVCT + SUM(MechDmd, MDE(MechDmd

)) =L=

1690 WorkGT + SUM(HPStmTurb,WHPTE(HPStmTurb)) ;

1691

1692 Eqstpd5(MechDmd)..

1693 MDReq(MechDmd) =E= MDE(MechDmd) + MDC(MechDmd) ;

1694


1696 MDC(MechDmd) =E= SUM(HPStmTurb,WHPTM(HPStmTurb,MechDmd)) + SUM(MPStmTurb,WMPTM(MPStmT

urb,MechDmd)) ;

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1697

1698 Eqstpd7(HPStmTurb)..

1699 TotWorkHPStmTurb(HPStmTurb) =E= SUM(MechDmd,WHPTM(HPStmTurb,MechDmd)) + WHPTE(HPStmTu

rb) ;

1700

1701 Eqstpd8(MPStmTurb)..

1702 TotWorkMPStmTurb(MPStmTurb) =E= SUM(MechDmd,WMPTM(MPStmTurb,MechDmd)) ;

1703


1705 MDC(MechDmd) =L= UBMD*YMD(MechDmd) ;

1706


1708 MDE(MechDmd) =L= UBMD*(1 - YMD(MechDmd)) ;

1709


1711 WHPTE(HPStmTurb) =L= UBED*YWHPTE(HPStmTurb) ;

1712

1713 Eqstpd12(HPStmTurb,MechDmd)..

1714 WHPTM(HPStmTurb,MechDmd) =L= UBMD*YWHPTM(HPStmTurb,MechDmd) ;

1715

1716 Eqstpd13(MPStmTurb,MechDmd)..

1717 WMPTM(MPStmTurb,MechDmd) =L= UBMD*YWMPTM(MPStmTurb,MechDmd) ;

1718

1719 * logical constraints start

1720 *atmost 1 HP turbine can produce electricity

1721 Eqstpd14..

1722 SUM(HPStmTurb,YWHPTE(HPStmTurb)) =L= 1 ;

1723

1724 * Each mechanical demand thro coupling can be met only by 1 turbine


1726 SUM(HPStmTurb,YWHPTM(HPStmTurb,MechDmd)) + SUM(MPStmTurb,YWMPTM(MPStmTurb,MechDmd)) =L

= 1 ;

1727

1728 * Each HP turbine can meet only 1 demand


1730 SUM(MechDmd,YWHPTM(HPStmTurb,MechDmd)) + YWHPTE(HPStmTurb) =L= 1 ;

1731

1732 * Each MP turbine can meet only 1 demand

1733 Eqstpd17(MPStmTurb)..

1734 SUM(MechDmd,YWMPTM(MPStmTurb,MechDmd)) =L= 1 ;

1735

1736

1737

1738

1739

1740

1741

1742

1743

1744

1745

1746

1747

1748 *$offtext

1749

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1750

1751

1752

1753

1754

1755

1756 *****************************************

1757 ** Equation for objective function

1758 *****************************************

1759

1760 Equations

1761 obj objective function cost in dollar per hr ;

1762

obj.. Z =E= DumPrice*(SUM(ModeHPStmTurb,YModeHPStmTurb(’1’,ModeHPStmTurb)) +

SUM(ModeMPStmTurb,YModeMPStmTurb(’1’,ModeMPStmTurb)) +

SUM(Phase2Str(Str),YP2(Str)) +

SUM(MPStmTurb,SUM(Str $InMPStmTurb(MPStmTurb,Str), Y(Str)))

+

SUM(HPStmTurb,SUM(Str $InHPStmTurb(HPStmTurb,Str), Y(Str)))

) +

SUM(SyngasStr, SUM(Comp, Fc(SyngasStr,Comp)*HHV(Comp)))*12 +

0.32*18*F(’17’)/1000 +

0.097*(MassFCW) ;

1774

1775

1776 obj.. Z =E= DumPrice*(SUM(ModeHPStmTurb,YModeHPStmTurb(’1’,ModeHPStmTurb)) +

1777 SUM(ModeMPStmTurb,YModeMPStmTurb(’1’,ModeMPStmTurb)) +

1778 SUM(Phase2Str(Str),YP2(Str)) +

1779 SUM(MPStmTurb,SUM(Str $InMPStmTurb(MPStmTurb,Str), Y(Str)))

+

1780 SUM(HPStmTurb,SUM(Str $InHPStmTurb(HPStmTurb,Str), Y(Str)))

1781 ) +

1782 SUM(SyngasStr, SUM(Comp, Fc(SyngasStr,Comp)*HHV(Comp)))*FCost

+

1783 DWCost*18*F(’17’)/1000 +

1784 0.0269*3.6*(MassFCW) ;

1785

1786

1787

1788

1789 *$ontext

1790 ********************

1791 * Bounds

1792 ********************

1793 * General upper bound for component and total flowrate

1794 Fc.up(Str,Comp) = 1.0E6 ;

1795 F.up(Str) = 1.0E6 ;

1796

1797

1798 * Bound for wetnes of 2 phase streams

1799 Wetns.lo(Phase2Str)= 0 ;

1800 Wetns.up(Phase2Str)= 1 ;

1801

1802

1803 * Bounds for 2 phase, saturated liquid and vapour streams of water

1804

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1805 * HP stream Temperature

1806 T.lo(HPStr) = LBT(’HP’) ;

1807 T.up(HPStr) = UBT(’HP’) ;

1808

1809 * HP stream Pressure

1810 P.lo(HPStr) = LBPL(’HP’) ;

1811 P.up(HPStr) = UBPL(’HP’) ;

1812

1813 * MP stream Temperature

1814 T.lo(MPStr) = LBT(’MP’) ;

1815 T.up(MPStr) = UBT(’MP’) ;

1816

1817 * MP stream Pressure

1818 P.lo(MPStr) = LBPL(’MP’) ;

1819 P.up(MPStr) = UBPL(’MP’) ;

1820

1821 * LP stream Temperature

1822 T.lo(LPStr) = LBT(’LP’) ;

1823 T.up(LPStr) = UBT(’LP’) ;

1824

1825 * LP stream Pressure

1826 P.lo(LPStr) = LBPL(’LP’) ;

1827 P.up(LPStr) = UBPL(’LP’) ;

1828

1829

1830

1831

1832 ** bounds for condensate streams

1833 * CDP stream Temperature

1834 T.lo(CDPStr) = LBT(’CDP’) ;

1835 T.up(CDPStr) = UBT(’CDP’) ;

1836

1837 * CDP stream Pressure

1838 P.lo(CDPStr) = LBPL(’CDP’) ;

1839 P.up(CDPStr) = UBPL(’CDP’) ;

1840

1841 ** bounds for vacuum streams

1842 * VP stream Temperature

1843 T.lo(VPStr) = LBT(’VP’) ;

1844 T.up(VPStr) = UBT(’VP’) ;

1845

1846 * VP stream Pressure

1847 P.lo(VPStr) = LBPL(’VP’) ;

1848 P.up(VPStr) = UBPL(’VP’) ;

1849

1850

1851

1852 * bounds for subcooled liquid streams

1853

1854 ** pumped stream from vacuum header

1855 T.lo(’9’) = LBT(’VP’) ;

1856 T.up(’9’) = UBT(’VP’) ;

1857

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1858

1859 ** pumped stream from deaerator to MP boiler (strteam 18)

1860 T.lo(’18’) = LBT(’CDP’) ;

1861 T.up(’18’) = UBT(’CDP’) ;

1862

1863 P.lo(’18’) = LBPL(’MP’) ;

1864 P.up(’18’) = UBPL(’MP’) ;

1865

1866

1867 ** pumped stream from deaerator to HP boiler (strteam 19)

1868 T.lo(’19’) = LBT(’CDP’) ;

1869 T.up(’19’) = UBT(’CDP’) ;

1870

1871 P.lo(’19’) = LBPL(’HP’) ;

1872 P.up(’19’) = UBPL(’HP’) ;

1873

1874 ** pumped stream from deaerator to HRSG (strteam 20)

1875 T.lo(’20’) = LBT(’CDP’) ;

1876 T.up(’20’) = UBT(’CDP’) ;

1877

1878 P.lo(’20’) = LBPL(’HP’) ;

1879 P.up(’20’) = UBPL(’HP’) ;

1880

1881

1882 * Fixing bounds for Temperature of gas streams for boiler

1883 T.lo(GasStr) = 297.0 ;

1884 T.up(GasStr) = 1501.0 ;

1885

1886 * Fixing bounds for Pressure of gas streams for boiler

1887 P.lo(GasStr) = 0.95 ;

1888 P.up(GasStr) = 1.15 ;

1889

1890

1891

1892

1893

1894

1895 ** Bounds for helping variables

1896

1897 * enthalpy of water streams

1898 H.lo(WatStr) = -0.09 ;

1899 H.up(WatStr) = 0.0 ;

1900

1901

1902 HVap.lo(Phase2Str) = -0.09 ;

1903 HVap.up(Phase2Str) = 0.0 ;

1904

1905 HSatLiq.lo(Phase2Str) = -0.09 ;

1906 HSatLiq.up(Phase2Str) = 0.0 ;

1907

1908 HSatLiq.lo(SatLiqStr) = -0.09 ;

1909 HSatLiq.up(SatLiqStr) = 0.0 ;

1910

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1911 HSatVap.lo(SatVapStr) = -0.09 ;

1912 HSatVap.up(SatVapStr) = 0.0 ;

1913

1914 * H bound for gases

1915 Hc.lo(GasStr,’H2’) = -0.001 ;

1916 Hc.lo(GasStr,’O2’) = -0.001 ;

1917 Hc.lo(GasStr,’N2’) = -0.001 ;

1918 Hc.lo(GasStr,’CH4’) = -0.022 ;

1919 Hc.lo(GasStr,’CO’) = -0.032 ;

1920 Hc.lo(GasStr,’CO2’) = -0.11 ;

1921 Hc.lo(GasStr,’H2O’) = -0.068 ;

1922

1923 Hc.up(GasStr,’H2’) = 0.011 ;

1924 Hc.up(GasStr,’O2’) = 0.012 ;

1925 Hc.up(GasStr,’N2’) = 0.012 ;

1926 Hc.up(GasStr,’CH4’) = 0.0026 ;

1927 Hc.up(GasStr,’CO’) = -0.0193 ;

1928 Hc.up(GasStr,’CO2’) = -0.0913 ;

1929 Hc.up(GasStr,’H2O’) = -0.053 ;

1930

1931 * H bound for turbine gases

1932 Hc.lo(Gas2Str,’H2’) = -0.001 ;

1933 Hc.lo(Gas2Str,’O2’) = -0.001 ;

1934 Hc.lo(Gas2Str,’N2’) = -0.001 ;

1935 Hc.lo(Gas2Str,’CH4’) = -0.022 ;

1936 Hc.lo(Gas2Str,’CO’) = -0.032 ;

1937 Hc.lo(Gas2Str,’CO2’) = -0.11 ;

1938 Hc.lo(Gas2Str,’H2O’) = -0.068 ;

1939

1940 Hc.up(Gas2Str,’H2’) = 0.011 ;

1941 Hc.up(Gas2Str,’O2’) = 0.012 ;

1942 Hc.up(Gas2Str,’N2’) = 0.012 ;

1943 Hc.up(Gas2Str,’CH4’) = 0.0026 ;

1944 Hc.up(Gas2Str,’CO’) = -0.0193 ;

1945 Hc.up(Gas2Str,’CO2’) = -0.0913 ;

1946 Hc.up(Gas2Str,’H2O’) = -0.053 ;

1947

1948

1949

1950 * latent heat for 2 phase and sat liq

1951 LatHtVapP2.lo(Phase2Str,’H2O’) = 25.0 ;

1952 LatHtVapP2.up(Phase2Str,’H2O’) = 50.0 ;

1953

1954 LatHtVapP2.lo(SatLiqStr,’H2O’) = 25.0 ;

1955 LatHtVapP2.up(SatLiqStr,’H2O’) = 50.0 ;

1956

1957

1958 LatHtVapLiq.lo(LiqStr,’H2O’) = 25.0 ;

1959 LatHtVapLiq.up(LiqStr,’H2O’) = 50.0 ;

1960

1961

1962

1963 * Saturation temperature of HP stream

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1964 TSat.lo(HPStr) = LBTSat(’HP’) ;

1965 TSat.up(HPStr) = UBTSat(’HP’) ;

1966

1967

1968 * Saturation temperature of MP stream

1969 TSat.lo(MPStr) = LBTSat(’MP’) ;

1970 TSat.up(MPStr) = UBTSat(’MP’) ;

1971

1972 * Saturation temperature of MP stream

1973 TSat.lo(LPStr) = LBTSat(’LP’) ;

1974 TSat.up(LPStr) = UBTSat(’LP’) ;

1975

1976 * Saturation temperature of VP stream

1977 TSat.lo(VPStr) = LBTSat(’VP’) ;

1978 TSat.up(VPStr) = UBTSat(’VP’) ;

1979

1980 **Saturation temperature for streams at Deaerator temperature

1981 TSat.lo(CDPStr) = LBTSat(’CDP’) ;

1982 TSat.up(CDPStr) = UBTSat(’CDP’) ;

1983

1984 * Fixing bounds for Tsat of pressure levels

1985 TSatOpr.up(PLev) = UBTSat(PLev) ;

1986 TSatOpr.lo(PLev) = LBTSat(PLev) ;

1987

1988

1989 * Fixing bounds for pressure levels

1990 POpr.up(PLev) = UBPL(PLev) ;

1991 POpr.lo(PLev) = LBPL(PLev) ;

1992

1993

1994 * Fixing bounds for T of pressure levels

1995 TOpr.up(PLev) = UBT(PLev) ;

1996 TOpr.lo(PLev) = LBT(PLev) ;

1997

1998

1999 * HP turbine isentropic expansion

2000 InHPTHPStmTurb.lo(HPStmTurb) = LBTSat(’HP’) ;

2001 InHPPHPStmTurb.lo(HPStmTurb) = LBPL(’HP’) ;

2002 OutMPPHPStmTurb.lo(HPStmTurb) = LBPL(’MP’) ;

2003 OutMPTHPStmTurb.lo(HPStmTurb) = 273.0 ;

2004 OutLPPHPStmTurb.lo(HPStmTurb) = LBPL(’LP’) ;

2005 OutLPTHPStmTurb.lo(HPStmTurb) = 273.0 ;

2006

2007

2008 InHPTHPStmTurb.up(HPStmTurb) = UBT(’HP’) ;

2009 InHPPHPStmTurb.up(HPStmTurb) = UBPL(’HP’) ;

2010 OutMPPHPStmTurb.up(HPStmTurb) = UBPL(’MP’) ;

2011 OutMPTHPStmTurb.up(HPStmTurb) = UBT(’MP’) ;

2012 OutLPPHPStmTurb.up(HPStmTurb) = UBPL(’LP’) ;

2013 OutLPTHPStmTurb.up(HPStmTurb) = UBT(’LP’) ;

2014

2015

2016 * MP turbine isentropic expansion

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2017 InMPTMPStmTurb.lo(MPStmTurb) = LBTSat(’MP’) ;

2018 InMPPMPStmTurb.lo(MPStmTurb) = LBPL(’MP’) ;

2019 OutLPPMPStmTurb.lo(MPStmTurb) = LBPL(’LP’) ;

2020 OutLPTMPStmTurb.lo(MPStmTurb) = 273.0 ;

2021

2022

2023 InMPTMPStmTurb.up(MPStmTurb) = UBT(’MP’) ;

2024 InMPPMPStmTurb.up(MPStmTurb) = UBPL(’MP’) ;

2025 OutLPPMPStmTurb.up(MPStmTurb) = UBPL(’LP’) ;

2026 OutLPTMPStmTurb.up(MPStmTurb) = UBT(’LP’) ;

2027

2028

2029

2030 * Bounds for T and P of Gas turbine variables

2031

2032 * Fixing bounds for air into compressor

2033 T.lo(’39’) = 298.0 ;

2034 T.up(’39’) = 299.0 ;

2035

2036 InTGTCmpr.lo(GTCmpr) = 298.0 ;

2037 InTGTCmpr.up(GTCmpr) = 299.0 ;

2038

2039 P.lo(’39’) = 0.99 ;

2040 P.up(’39’) = 1.1 ;

2041

2042 InPGTCmpr.lo(GTCmpr) = 0.99 ;

2043 InPGTCmpr.up(GTCmpr) = 1.1 ;

2044

2045

2046 * Fixing bounds for air exit from compressor

2047 T.lo(’40’) = 298.0 ;

2048 T.up(’40’) = 704.0 ;

2049

2050 OutTGTCmpr.lo(GTCmpr) = 298.0 ;

2051 OutTGTCmpr.up(GTCmpr) = 704.0 ;

2052

2053 P.lo(’40’) = 0.99 ;

2054 P.up(’40’) = 20.0 ;

2055

2056 OutPGTCmpr.lo(GTCmpr) = 0.99 ;

2057 OutPGTCmpr.up(GTCmpr) = 20.0 ;

2058

2059

2060

2061

2062 * Fixing bounds for air into exapnder

2063 T.lo(’42’) = 298.0 ;

2064 T.up(’42’) = 1510.0 ;

2065

2066 InTGTExpdr.lo(GTExpdr) = 298.0 ;

2067 InTGTExpdr.up(GTExpdr) = 1510.0 ;

2068

2069 P.lo(’42’) = 0.99 ;

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2070 P.up(’42’) = 20.0 ;

2071

2072 InPGTExpdr.lo(GTExpdr) = 0.99 ;

2073 InPGTExpdr.up(GTExpdr) = 20.0 ;

2074

2075

2076 * Fixing bounds for air exit from expander

2077 T.lo(’43’) = 298.0 ;

2078 T.up(’43’) = 1510.0 ;

2079

2080 OutTGTExpdr.lo(GTExpdr) = 298.0 ;

2081 OutTGTExpdr.up(GTExpdr) = 1510.0 ;

2082

2083 P.lo(’43’) = 1.3 ;

2084 P.up(’43’) = 20.0 ;

2085

2086 OutPGTExpdr.lo(GTExpdr) = 1.3 ;

2087 OutPGTExpdr.up(GTExpdr) = 20.0 ;

2088

2089

2090

2091 * fixing bounds for syngas streams to turbine

2092 T.lo(’41’) = 298.0 ;

2093 T.up(’41’) = 299.0 ;

2094

2095 T.lo(’44’) = 298.0 ;

2096 T.up(’44’) = 299.0 ;

2097

2098 P.lo(’41’) = 0.99 ;

2099 P.up(’41’) = 20.0 ;

2100

2101 P.lo(’44’) = 1.3 ;

2102 P.up(’44’) = 20.0 ;

2103

2104

2105 * fixing bounds for HRSG gases of turbine

2106 T.lo(’45’) = 298.0 ;

2107 T.up(’45’) = 1510.0 ;

2108

2109 T.lo(’46’) = 298.0 ;

2110 T.up(’46’) = 1510.0 ;

2111

2112 P.lo(’45’) = 1.3 ;

2113 P.up(’45’) = 20.0 ;

2114

2115 P.lo(’46’) = 1.3 ;

2116 P.up(’46’) = 20.0 ;

2117

2118

2119 * bounds for the odd valve streams (stream 49 and 51)

2120 T.lo(’49’) = LBT(’MP’) ;

2121 T.up(’49’) = UBT(’HP’) ;

2122

model.lst Wed May 30 15:17:17 2018 60


05/30/18 15:17:15 Page 41



2123

2124 TSat.lo(’49’) = LBTSat(’MP’) ;

2125 TSat.up(’49’) = UBTSat(’MP’) ;

2126

2127 P.lo(’49’) = LBPL(’MP’) ;

2128 P.up(’49’) = UBPL(’MP’) ;

2129

2130

2131 T.lo(’51’) = LBT(’LP’) ;

2132 T.up(’51’) = UBT(’MP’) ;

2133

2134

2135 TSat.lo(’51’) = LBTSat(’LP’) ;

2136 TSat.up(’51’) = UBTSat(’LP’) ;

2137

2138 P.lo(’51’) = LBPL(’LP’) ;

2139 P.up(’51’) = UBPL(’LP’) ;

2140

2141

2142

2143

2144

2145

2146

2147 *******************

2148 * Fixed

2149 *******************

2150

2151 * Fixing the pressure levels

2152 POpr.fx(PLev) = FxPL(PLev) ;

2153

2154

2155

2156 * component flowrates of non water components to zero

2157 Fc.fx(WatStr,NonWatComp) = 0.0 ;

2158

2159 * Fixing the other components of air stream to zero

2160 Fc.fx(AirStr,NonAirComp) = 0.0 ;

2161

2162 * Fixing the other components of syngas stream to zero

2163 Fc.fx(SyngasStr,NonSyngasComp) = 0.0 ;

2164

2165

2166

2167 * Fixing some bianries and wetnes to zero (for phase 2 streams that will never be wet

2168 YP2.fx(P2P1Str) = 0 ;

2169 * Wetnes cud be fixed but conopt3 creates problem, rest of solvers were fine

2170 *Wetns.fx(P2P1Str) = 0 ;

2171

2172

2173

2174 * Fixing some bianries to 1 (condensing turbine stream whcih is always wet)

2175 YP2.fx(P2P2Str) = 1 ;

model.lst Wed May 30 15:17:17 2018 61


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2176

2177

2178 * Fixing the pressure of pumped vacuum condensate to aerator

2179 P.fx(’9’) = FxPL(’CDP’) ;

2180

2181 * fixing conditions of subcoled dimineralised water

2182 P.fx(’17’) = FxPL(’CDP’) ;

2183 T.fx(’17’) = AmbT ;

2184

2185

2186

2187

2188 * To be changed

2189

2190

2191 *TotWorkMPStmTurb.fx(’1’) = 2.0 ;

2192 *F.fx(’41’) = 10.0 ;

2193

2194

2195 Fc.fx(’31’,’H2O’) = 0.0 ;

2196 Fc.fx(’32’,’H2O’) = 0.0 ;

2197 Fc.fx(’33’,’H2O’) = 0.0 ;

2198

2199

2200

2201

2202

2203

2204

2205

2206

2207

2208

2209

2210

2211 *******************

2212 * Initial point

2213 *******************

2214

2215 Fc.l(’1’,’H2O’) = 100.0 ;

2216 T.l(’25’) = 597;

2217 T.l(’26’) = 730 ;

2218 T.l(’1’) = 730.0 ;

2219 Fc.l(’5’,’H2O’) = 100.0 ;

2220 T.l(’5’) = 597.0 ;

2221

2222 *$offtext

2223

2224

2225

2226

2227

2228

model.lst Wed May 30 15:17:17 2018 62


05/30/18 15:17:15 Page 43



2229

2230

2231

2232

2233 MODEL TEST4a / ALL / ;

2234

2235 TEST4a.limrow =10000;

2236 TEST4a.limcol =10000;

2237

2238

2239 TEST4a.tolinfeas = 1.0E-9;

2240 TEST4a.Tolproj = 1.0E-9;

2241 TEST4a.Tolinfrep = 1.0E-9;

2242

2243 TEST4a.iterlim =20000;

2244 TEST4a.nodlim =10000;

2245

2246

2247 TEST4a.optfile = 1 ;

2248

2249 option optcr = 0 ;

2250 OPTION NLP = conopt ;

2251 option sysout = on ;

2252 option minlp = dicopt ;

2253 option decimals = 6 ;

2254

2255

2256

2257

2258 option savepoint = 1 ;

2259

2260 execute_loadpoint ’TEST7a1_p’ ;

2261 *execute_loadpoint ’TEST7a2_p’ ;






2267

2268






2274

2275

2276 SOLVE TEST4a USING MINLP MINIMIZING Z ;

2277

2278 *display h.l ;

2279 *display Fc.l ;

2280 *OPTION NLP = conopt3 ;

2281 *option minlp = sbb ;

model.lst Wed May 30 15:17:17 2018 63


05/30/18 15:17:15 Page 44



2282

2283 *SOLVE TEST4a USING MINLP MINIMIZING Z ;

2284

2285 **display OutVPHPStmTurb; mio

2286 display EqMolBalVlv.l;

2287

2288 Parameter

2289 SteamFDeaertr;

2290

2291

2292 SteamFDeaertr = Sum(str, F.l(Str)$(InDeAertr(’1’,str)));

INCLUDE /var/www/html/interfaces/cgi-bin/steam/sumres.inc

2294 ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** **

2295

2296 * sumres.inc file for the creation of the Summary of Results and

2297

2298 * data for the graphic display of solution.

2299

2300 ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** ** **

2301

2302

2303

2304 FIlE RES1 /"../../steam/output.html"/

2305

2306 PUT RES1 "<html><head><title>OUTPUT</title>"/;

2307

2308 PUT RES1 ’<style type="text/css">’/;

2309

2310 PUT RES1 " HR {"/;

2311

2312 *PUT RES1 " border : thick outset #800000;"/;

2313

2314 PUT RES1 " font-color: #800000;"/;

2315

2316 PUT RES1 " }"/;

2317

2318

2319

2320 PUT RES1 " TD.ref {"/;

2321

2322 PUT RES1 " border : thick outset #FFFF130;"/;

2323

2324 PUT RES1 " background-color : #C0C0C0;"/;

2325

2326 PUT RES1 " padding-left : 1ex;"/;

2327

2328 PUT RES1 " width : 50%;"/;

2329

2330 PUT RES1 " font-size : small;"/;

2331

2332 PUT RES1 " font-color: #800000;"/;

2333

2334 PUT RES1 " padding-top : 6px;"/;

model.lst Wed May 30 15:17:17 2018 64


05/30/18 15:17:15 Page 45



2335

2336 PUT RES1 " padding-right : 6px;"/;

2337

2338 PUT RES1 " padding-bottom : 6px;"/;

2339

2340 PUT RES1 " padding-left : 6px;"/;

2341

2342 PUT RES1 " text-align : 1em;"/;

2343

2344 PUT RES1 " vertical-align : top;"/;

2345

2346 PUT RES1 " font-weight : bold;"/;

2347

2348 PUT RES1 " }"/;

2349

2350 PUT RES1 "</style>"/;

2351

2352 PUT RES1 "</head><body alink=#800000 link=#800000>"/;

2353

2354 PUT RES1 " <br />"//;

2355 PUT RES1 " <h3><b>STEAM Interface</b></h3></hr><hr></hr>"//;

2356

2357 PUT RES1 "<h4><font color=#353535> Optimal Synthesis and Operation of Utility Plants</h

4></font><br>"///;

2358

2359 PUT RES1 "<table align=center border =4 bordercolor=#6E6E6E width=80%><th colspan =10

bgcolor=#922414> <font color=#FFFFFF> DATA </font></th>"///;

2360 PUT RES1 "<tr></tr> "/;

2361

2362 *PUT RES1 "<br />"/;

2363 *PUT RES1 "<br />"/;

2364 PUT RES1 "<tr><tr><br><th <b> Demands: </b> "/;

2365 PUT RES1 "<center><p> HP Heating: " HtReq(’HP’):2:0 " MW </p></center>"/;

2366 PUT RES1 "<center><p> MP Heating: " HtReq(’MP’):2:0 " MW </p></center>"/;

2367 PUT RES1 "<center><p> LP Heating: " HtReq(’LP’):2:0 " MW </p></center>"/;

2368 PUT RES1 "<center><p> Electricity: " ElecDmd:3:0 " MW - Options: Gas Turbine, any type

of steam turbine, combination of both or purcharsed externally</p></center>"/;

2369 loop (MechDmd,

2370 PUT RES1 " Mechanical Power No" ord (MechDmd):2:0;

2371 PUT RES1 ": " MDReq(MechDmd):2:0 " MW - Options: Any type of steam turbine or electric

motors"/;

2372 PUT RES1 "<br />"/;

2373 );

2374 PUT RES1 "<p> ___________________________</p> "/;

2375

2376

2377 PUT RES1 "<table align=center border =1 bordercolor=#800000 width=70%><th colspan =8 bg

color=#C0C0C0> Pressure of Steam Headers (MPa) </th>"///;

2378 PUT RES1 "<tr> "/;

2379 *PUT RES1 "<tr><br><th "/;

2380

2381 PUT RES1 "<td bgcolor=#E0E0F8><center> High Pressure (HP) Header<td bgcolor=#E0E0F8><ce

nter> Medium Pressure (MP) Header <td bgcolor=#E0E0F8><center>Low Pressure (LP) Header "/;

2382 PUT RES1 "<td bgcolor=#E0E0F8><center> Condensate Header <td bgcolor=#E0E0F8><center> Va

ccum Header </td><tr>"/;

2383 PUT RES1 "<td><center>" (FxPL(’hp’)*0.1):4:2 "<td><center>" (FxPL(’mp’)*0.1):6:2 "<td><

model.lst Wed May 30 15:17:17 2018 65

center>"(FxPL(’lp’)*0.1):6:2"<td><center>" (FxPL(’cdp’)*0.1):6:2 "<td><center>" (FxPL(’vp’)*0.

1):6:2"</td><tr>"/;

2384

2385

2386 PUT RES1 "</tr>"/;

2387 PUT RES1 "</table><p>"/;

model.lst Wed May 30 15:17:17 2018 66


05/30/18 15:17:15 Page 46




2389

2390 PUT RES1 "<table align=center border =4 bordercolor=#6E6E6E bgcolor=#FFFFFF width=80%><

th colspan =15 bgcolor=#922414> <font color=#FFFFFF > RESULTS </font></th>"///;

2391 PUT RES1 "<tr><td> "/;

2392


color=#C0C0C0> Steam Headers </th>"///;

2394 PUT RES1 "<tr> "/;

2395

2396 PUT RES1 "<td bgcolor=#E0E0F8><center> Pressure (MPa)<td bgcolor=#E0E0F8><center> Tempe

rature (K) <td bgcolor=#E0E0F8><center> Tsat (k) </td><tr>"/;

2397 PUT RES1 "<td><center> HP : " (POpr.l(’HP’)*0.1):4:1"<td><center>" TOpr.l(’HP’):6:1 "<t

d><center>"TSatOpr.l(’HP’):6:1"</td><tr>"/;

2398 PUT RES1 "<td><center> HP : " (POpr.l(’MP’)*0.1):4:1"<td><center>" TOpr.l(’MP’):6:1 "<t

d><center>"TSatOpr.l(’MP’):6:1"</td><tr>"/;

2399 PUT RES1 "<td><center> HP : " (POpr.l(’LP’)*0.1):4:1"<td><center>" TOpr.l(’LP’):6:1 "<t

d><center>"TSatOpr.l(’LP’):6:1"</td><tr>"/;

2400

2401 PUT RES1 "</tr>"/;


2403

INCLUDE /var/www/html/interfaces/cgi-bin/steam/boiler.inc

INCLUDE /var/www/html/interfaces/cgi-bin/steam/boiler13.inc

2406


color=#C0C0C0> Boilers </th>"///;

2408 PUT RES1 "<tr> "/;

2409

2410 PUT RES1 "<td><td bgcolor=#E0E0F8><center> HP Boiler<td bgcolor=#E0E0F8><center> MP Boi

ler <td bgcolor=#E0E0F8><center> HRSG Boiler</td><tr>"/;

2411 PUT RES1 "<td bgcolor=#FEFDCD> Boiler Feed Water (BFW) (ton/h) "/;

2412

2413 loop(Blr,

2414 loop(Str$( InWtrBlr(Blr,Str)),

2415 PUT$(f.l(str) ne 0) RES1 " <td><center> " (f.l(str)*18/1000):7:2;

2416 PUT$( f.l(str) eq 0) RES1 "<td><center> --- "/ ;

2417 );

2418 );

2419 put res1 "<tr>"/;

2420 PUT RES1 "<td bgcolor=#FEFDCD> Steam (ton/h) "/;

2421 loop(Blr,

2422 loop(Str$( OutStmBlr (Blr,Str)),

2423 PUT $(f.l(str) ne 0)RES1 " <td><center> " (f.l(str)*18/1000):7:2;

2424 PUT$( f.l(str) eq 0) RES1 " <td><center> --- " ;

2425 );

2426 );

2427 put res1 "<tr>"/;

2428

2429 PUT RES1 "<td bgcolor=#FEFDCD> Steam Pressure (MPa) "/;

2430 loop(Blr,


2432 PUT$(f.l(str) ne 0) RES1 " <td><center> " (p.l(str)*0.1):7:2;

2433 PUT$( f.l(str) eq 0) RES1 "<td><center> --- " ;

2434

2435 );

model.lst Wed May 30 15:17:17 2018 67

2436 );

2437 put res1 "<tr>"/;

2438

2439 PUT RES1 "<td bgcolor=#FEFDCD> Steam Temperature (K) "/;

2440 loop(Blr,

model.lst Wed May 30 15:17:17 2018 68


05/30/18 15:17:15 Page 47




2442 PUT$(f.l(str) ne 0) RES1 " <td><center> " t.l(str):7:2;

2443 PUT$( f.l(str) eq 0) RES1 "<td><center> --- " ;

2444 );

2445 );

2446 PUT RES1 "</tr>"/;


2448

2449

2450


color=#C0C0C0> Steam Turbines </th>"///;

2452 PUT RES1 "<tr><td> "/;


color=#E0E0F8> High Pressure Steam Turbines </th>"///;

2454 PUT RES1 "<tr> "/;

2455 loop (HPStmTurb,

2456

2457 PUT$(TotWorkHPStmTurb.l(HPStmTurb) ne 0) RES1 " <td bgcolor=#FEFDCD> "HPStmTurb.tl:5:0

"<td bgcolor=#FEFDCD> Power: "

2458 PUT$(TotWorkHPStmTurb.l(HPStmTurb) ne 0) RES1 "<td>" TotWorkHPStmTurb.l(HPStmTurb):4:0 "

MW <tr>"/;

2459

2460 loop (str$((InHPStmTurb(HPStmTurb,Str)) or (OutMPHPStmTurb(HPStmTurb,Str)) or (OutLPHPSt

mTurb(HPStmTurb,Str)) or (OutVPHPStmTurb(HPStmTurb,Str))),

2461

2462 PUT$((f.l(str) ne 0)and (InHPStmTurb(HPStmTurb,Str))) RES1 " <td><td bgcolor=#F5FFFA>

Inlet";

2463 PUT$((f.l(str) ne 0)and (InHPStmTurb(HPStmTurb,Str))) RES1 "<td>" ((f.l(str)*18)/1000)

:7:2 " Ton/h <tr>"/;

2464

2465

2466 PUT$((OutMPHPStmTurb(HPStmTurb,Str)) and (f.l(str) ne 0))RES1 " <td><td bgcolor=#F0FFF0>

Outlet";

2467 PUT$((OutLPHPStmTurb(HPStmTurb,Str)) and (f.l(str) ne 0))RES1 " <td><td bgcolor=#F0FFF0>

Outlet";

2468 PUT$((OutVPHPStmTurb(HPStmTurb,Str)) and (f.l(str) ne 0))RES1 " <td><td bgcolor=#F0FFF0>

Outlet";

2469

2470 PUT$((OutMPHPStmTurb(HPStmTurb,Str))and (f.l(str) ne 0)) RES1 "<td>" ((f.l(str)*18)/1000

):7:2 " Ton/h to MP Header @" t.l(str):6:2 " K <tr>" /;

2471 PUT$((OutLPHPStmTurb(HPStmTurb,Str))and (f.l(str) ne 0)) RES1 "<td>" ((f.l(str)*18)/1000

):7:2 " Ton/h to LP Header @" t.l(str):6:2 " K <tr>" /;

2472 PUT$((OutVPHPStmTurb(HPStmTurb,Str))and (f.l(str) ne 0)) RES1 "<td>" ((f.l(str)*18)/1000

):7:2 " Ton/h to VP Header @" t.l(str):6:2 " K <tr>" /;

2473

2474 );

2475 put res1 "<tr>"/;

2476 );

2477 PUT RES1 "</td></tr>"/;

2478 PUT RES1 "</table>"/;

2479

2480


color=#E0E0F8> Medium Pressure Steam Turbines </th>"///;

2482 PUT RES1 "<tr> "/;

model.lst Wed May 30 15:17:17 2018 69

2483 loop (MPStmTurb,

2484 PUT$(TotWorkMPStmTurb.l(MPStmTurb) ne 0) RES1 "<td bgcolor=#FEFDCD> "MPStmTurb.tl:5:0

"<td bgcolor=#FEFDCD> Power "

2485 PUT$(TotWorkMPStmTurb.l(MPStmTurb) ne 0) RES1 "<td>" TotWorkMPStmTurb.l(MPStmTurb):4:0 "

MW <tr>"/;

2486

2487 loop (str$((InMPStmTurb(MPStmTurb,Str)) or (OutLPMPStmTurb(MPStmTurb,Str)) or (OutVPMPSt

mTurb(MPStmTurb,Str))),

2488

2489

2490 PUT$((f.l(str) ne 0)and (InMPStmTurb(MPStmTurb,Str))) RES1 "<td><td bgcolor=#F5FFFA> Inl

et";

2491 PUT$((f.l(str) ne 0)and (InMPStmTurb(MPStmTurb,Str))) RES1 "<td> " ((f.l(str)*18)/1000

):7:2 " Ton/h <tr>" /;

2492 PUT$((OutLPMPStmTurb(MPStmTurb,Str)) and (f.l(str) ne 0))RES1 "<td><td bgcolor=#F0FFF0>

Outlet";

2493 PUT$((OutVPMPStmTurb(MPStmTurb,Str)) and (f.l(str) ne 0))RES1 "<td><td bgcolor=#F0FFF0>

Outlet";

model.lst Wed May 30 15:17:17 2018 70


05/30/18 15:17:15 Page 48



2494

2495 PUT$((OutLPMPStmTurb(MPStmTurb,Str))and (f.l(str) ne 0)) RES1 "<td>" ((f.l(str)*18)/1000

):7:2 " Ton/h to LP Header @" t.l(str):6:2 " K <tr>" /;

2496 PUT$((OutVPMPStmTurb(MPStmTurb,Str))and (f.l(str) ne 0)) RES1 "<td>" ((f.l(str)*18)/1000

):7:2 " Ton/h to Vaccum Header @" t.l(str):6:2 " K <tr>" /;

2497 );

2498 put res1 "<tr>"/;

2499 );

2500 PUT RES1 "</td></tr>"/;



2503

2504

2505 ********


color=#C0C0C0> GAS TURBINE </th>"///;

2507 PUT RES1 "<tr> "/;

2508

2509 PUT RES1 "<td bgcolor=#E0E0F8><center> Power <td><center> "WorkGT.l:6:0 " MW </td><tr

>"/;

2510 *PUT RES1 "<td bgcolor=#E0E0F8><center> From MP to LP = <td><center> " ((f.l(’51’)*18)/

1000):6:2 " Ton/h </td><tr>"/;

2511 PUT RES1 "</tr>"/;


2513 *****

2514

********

PUT RES1 "<table align=center border =1 bordercolor=#800000 width=50%><th colspan =8 bg

color=#C0C0C0> THROTTLE VALVES </th>"///;

PUT RES1 "<tr> "/;

PUT RES1 "<td bgcolor=#E0E0F8><center> From HP to MP = <td><center> "((f.l(’49’)*18)/10

00):6:2 " Ton/h </td><tr>"/;

PUT RES1 "<td bgcolor=#E0E0F8><center> From MP to LP = <td><center> " ((f.l(’51’)*18)/1

000):6:2 " Ton/h </td><tr>"/;

PUT RES1 "</tr>"/;

PUT RES1 "</table><p>"/;

*****


color=#C0C0C0> DEMINERALIZED WATER </th>"///;

2527 PUT RES1 "<tr> "/;

2528

2529 PUT RES1 "<td bgcolor=#E0E0F8><center> Flow rate <td><center> "((f.l(’17’)*18)/1000):6:

2 " Ton/h </td><tr>"/;

2530 PUT RES1 "<td bgcolor=#E0E0F8><center> Temperature <td><center> " t.l(’17’):6:2 " K </

td><tr>"/;

2531 PUT RES1 "</tr>"/;


2533


color=#C0C0C0> COOLING WATER </th>"///;

2535 PUT RES1 "<tr> "/;

2536

2537 PUT RES1 "<td bgcolor=#E0E0F8><center> Flow rate <td><center> "(((MassFCW.l)*3600)/1000

):7:2 " Ton/h </td><tr>"/;

2538 PUT RES1 "<td bgcolor=#E0E0F8><center> Increase Temp. <td><center> 20 K </td><tr>"/;

model.lst Wed May 30 15:17:17 2018 71

2539 PUT RES1 "</tr>"/;


2541


color=#C0C0C0> DEAERATOR </th>"///;

2543 PUT RES1 "<tr> "/;

2544

2545 PUT RES1 "<td bgcolor=#E0E0F8><center> Pressure <td><center> "(DeaerP):7:2 " MPa </td>

<tr>"/;

2546 *PUT RES1 "<td bgcolor=#E0E0F8><center> BFW Flow rate <td><center>"(((f.l(’13’) + f.l(

’14’) + f.l(’15’))*18)/1000):7:2 " Ton/h </td><tr>"/;

2547 PUT RES1 "<td bgcolor=#E0E0F8><center> Steam Flow rate <td><center> "(((SteamFDeaertr)*

18)/1000):7:2 " Ton/h </td><tr>"/;

2548 PUT RES1 "<td bgcolor=#E0E0F8><center> Vent Flow rate <td><center> "((f.l(’16’)*18)/100

0):7:2 " Ton/h </td><tr>"/;

model.lst Wed May 30 15:17:17 2018 72


05/30/18 15:17:15 Page 49



2549 PUT RES1 "</tr>"/;


2551

2552


color=#C0C0C0> UTILITY PLANT COST </th>"///;

2554 PUT RES1 "<tr> "/;

2555

2556 PUT RES1 "<td bgcolor=#E0E0F8><center> Demineralized water <td><center> "((8600*0.32*18

*F.l(’17’))/1000):10:2 " $/year </td><tr>"/;

2557 PUT RES1 "<td bgcolor=#E0E0F8><center> Cooling water <td><center>"(MassFCW.l*(8600*0.

0269*3600)/1000):10:2 " $/year </td><tr>"/;

2558 PUT RES1 "<td bgcolor=#E0E0F8><center> Fuel (Syngas) <td><center> "((SUM(SyngasStr, SUM

(Comp, Fc.l(SyngasStr,Comp)*HHV(Comp)))*12*8600)/1000000):10:2 " Million $/year</td><tr>"/;

2559 PUT RES1 "</tr>"/;


2561

2562 ****8600 hr = 1 operational year

2563 PUT RES1 "<center><b> Total Plant Cost: " (((z.l)*(8600))/1000000):7:2 " Million $/ye

ar </b>";

2564


2566

INCLUDE /var/www/html/interfaces/cgi-bin/steam/buttons.inc

2568 PUT RES1 ’<br><table align=center><td class="ref"><A HREF="./../cgi-bin/steam/graph.cgi"

target=new_window>SEE SUPERSTRUCTURE</A>’/;

2569 PUT RES1 ’<td class="ref"><a href="model.pdf" target=new_window>GAMS LIST FILE</a>’;

2570 PUT RES1 "</table></body></html>"/;

model.lst Wed May 30 15:17:17 2018 73


05/30/18 15:17:15 Page 50


Include File Summary

SEQ GLOBAL TYPE PARENT LOCAL FILENAME

1 1 INPUT 0 0 /var/www/html/interfaces/cgi-bin/steam/model.gms

2 1 INCLUDE 1 1 ./var/www/html/interfaces/cgi-bin/steam/ex3.dat

3 297 INCLUDE 1 2 ./var/www/html/interfaces/cgi-bin/steam/model.inc

4 2293 INCLUDE 1 3 ./var/www/html/interfaces/cgi-bin/steam/sumres.inc

5 2404 INCLUDE 4 111 ../var/www/html/interfaces/cgi-bin/steam/boiler.inc

6 2405 INCLUDE 5 1 .../var/www/html/interfaces/cgi-bin/steam/boiler13.i

nc

7 2567 INCLUDE 4 229 ../var/www/html/interfaces/cgi-bin/steam/buttons.inc

COMPILATION TIME = 0.010 SECONDS 3 MB 24.4.1 r50296 LEX-LEG

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Equation Listing SOLVE TEST4a Using MINLP From line 2276

---- EqTotMolStr =E= Total mass balance for stream (Total Mole flow = sum of component Mole

flow)

EqTotMolStr(1).. F(1) - Fc(1,H2) - Fc(1,O2) - Fc(1,N2) - Fc(1,CH4) - Fc(1,CO) - Fc(1,CO2) - F

c(1,H2O) =E= 0 ; (LHS = 0)


c(2,H2O) =E= 0 ; (LHS = 0)


c(3,H2O) =E= 0 ; (LHS = 0)


c(4,H2O) =E= 0 ; (LHS = 0)


c(5,H2O) =E= 0 ; (LHS = 0)


c(6,H2O) =E= 0 ; (LHS = 0)


c(7,H2O) =E= 0 ; (LHS = 0)


c(8,H2O) =E= 0 ; (LHS = 0)


c(9,H2O) =E= 0 ; (LHS = 0)

EqTotMolStr(10).. F(10) - Fc(10,H2) - Fc(10,O2) - Fc(10,N2) - Fc(10,CH4) - Fc(10,CO) - Fc(10,

CO2) - Fc(10,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(11,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(12,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(13,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(14,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(15,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(16,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(17,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(18,H2O) =E= 0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 75


CO2) - Fc(19,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(20,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(21,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(22,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(23,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(24,H2O) =E= 0 ; (LHS = 0)

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EqTotMolStr =E= Total mass balance for stream (Total Mole flow = sum of component Mole

flow)


CO2) - Fc(25,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(26,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(27,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(28,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(29,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(30,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(31,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(32,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(33,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(34,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(35,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(36,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(37,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(38,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(39,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(40,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(41,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(42,H2O) =E= 0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 77


CO2) - Fc(43,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(44,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(45,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(46,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(47,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(48,H2O) =E= 0 ; (LHS = 0)

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EqTotMolStr =E= Total mass balance for stream (Total Mole flow = sum of component Mole

flow)


CO2) - Fc(49,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(50,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(51,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(52,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(53,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(54,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(55,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(56,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(57,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(58,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(59,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(60,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(61,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(62,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(63,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(64,H2O) =E= 0 ; (LHS = 0)


CO2) - Fc(65,H2O) =E= 0 ; (LHS = 0)

---- EqEnthpyGasStr1 =E=

model.lst Wed May 30 15:17:17 2018 79

EqEnthpyGasStr1(21,H2).. - (8.14452778766379E-6)*T(21) + Hc(21,H2) =E= -0.00228509828994363 ;

(LHS = -0.00228509828994363)

EqEnthpyGasStr1(21,O2).. - (8.73316984448387E-6)*T(21) + Hc(21,O2) =E= -0.00241700206679658 ;

(LHS = -0.00241700206679658)

EqEnthpyGasStr1(21,N2).. - (8.29742739116574E-6)*T(21) + Hc(21,N2) =E= -0.00241309370464962 ;

(LHS = -0.00241309370464962)

EqEnthpyGasStr1(21,CH4).. - (1.34896990306911E-5)*T(21) + Hc(21,CH4) =E= -0.0235072469137719

; (LHS = -0.0235072469137719)

EqEnthpyGasStr1(21,CO).. - (8.36790657253685E-6)*T(21) + Hc(21,CO) =E= -0.0331187071262073 ;

(LHS = -0.0331187071262073)

EqEnthpyGasStr1(21,CO2).. - (1.26157551451301E-5)*T(21) + Hc(21,CO2) =E= -0.111880706258689 ;

(LHS = -0.111880706258689)

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EqEnthpyGasStr1 =E=

EqEnthpyGasStr1(21,H2O).. - (9.89371207808497E-6)*T(21) + Hc(21,H2O) =E= -0.069944520823574 ;

(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.0699445208235739)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.0699445208235739)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)

model.lst Wed May 30 15:17:17 2018 81


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.0699445208235739)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)

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EqEnthpyGasStr1 =E=


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)

model.lst Wed May 30 15:17:17 2018 83


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)

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EqEnthpyGasStr1 =E=


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)

model.lst Wed May 30 15:17:17 2018 85


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994362)

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EqEnthpyGasStr1 =E=


(LHS = -0.0024170020667966)


(LHS = -0.00241309370464963)


; (LHS = -0.023507246913772)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)

model.lst Wed May 30 15:17:17 2018 87


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)

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EqEnthpyGasStr1 =E=


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)


(LHS = -0.00228509828994363)


(LHS = -0.00241700206679658)


(LHS = -0.00241309370464962)


; (LHS = -0.0235072469137719)


(LHS = -0.0331187071262073)


(LHS = -0.111880706258689)


(LHS = -0.069944520823574)

---- EqEnthVapStr2 =E=

EqEnthVapStr2(1).. - (1.03922637096986E-5)*T(1) + HVap(1) =E= -0.069944520823574 ; (LHS = -0.

069944520823574)


069944520823574)


069944520823574)


069944520823574)


069944520823574)


069944520823574)


0699445208235739)

model.lst Wed May 30 15:17:17 2018 89

EqEnthVapStr2(12).. - (9.61540615714804E-6)*T(12) + HVap(12) =E= -0.069944520823574 ; (LHS =

-0.069944520823574)


-0.069944520823574)


-0.0699445208235739)


-0.0699445208235739)


-0.069944520823574)

EqEnthVapStr2(33).. - (9.6154061573211E-6)*T(33) + HVap(33) =E= -0.069944520823574 ; (LHS = -

0.069944520823574)

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EqEnthVapStr2 =E=


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)


-0.069944520823574)

model.lst Wed May 30 15:17:17 2018 91


-0.0699445208235739)

---- EqEnthSatLiq =E=

EqEnthSatLiq(1).. 0.000277777777777778*LatHtVapP2(1,H2O) - (9.86428795757015E-6)*TSat(1) + HS

atLiq(1) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


atLiq(2) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


atLiq(3) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


atLiq(4) =E= -0.069944520823574 ; (LHS = -0.069944520823574)

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EqEnthSatLiq =E=


atLiq(5) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


atLiq(6) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


atLiq(7) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


atLiq(8) =E= -0.069944520823574 ; (LHS = -0.069944520823574)

EqEnthSatLiq(10).. 0.000277777777777778*LatHtVapP2(10,H2O) - (9.73756236574658E-6)*TSat(10) +

HSatLiq(10) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(11) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(12) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(13) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(14) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(15) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(25) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(26) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(31) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(32) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(33) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(34) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(35) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(36) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)

model.lst Wed May 30 15:17:17 2018 93


HSatLiq(37) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(38) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(47) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(48) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(49) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(50) =E= -0.069944520823574 ; (LHS = -0.069944520823574)

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EqEnthSatLiq =E=


HSatLiq(51) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(52) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(53) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(54) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(55) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(56) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(57) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(58) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(59) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(60) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(61) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(62) =E= -0.069944520823574 ; (LHS = -0.0699445208235739)


HSatLiq(63) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(64) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


HSatLiq(65) =E= -0.069944520823574 ; (LHS = -0.069944520823574)

---- EqTSat =E=

EqTSat(1).. P(1) - (0.739754740916448)*TSat(1) =E= 0 ; (LHS = -1.56319401867222E-13)

EqTSat(2).. P(2) - (0.395838725890801)*TSat(2) =E= 0 ; (LHS = 1.17239551400417E-13)

EqTSat(3).. P(3) - (0.173532578840636)*TSat(3) =E= 0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 95


EqTSat(5).. P(5) - (0.395838725890801)*TSat(5) =E= 0 ; (LHS = 1.17239551400417E-13)




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EqTSat =E=




EqTSat(13).. P(13) - (0.0471726943081477)*TSat(13) =E= 0 ; (LHS = -6.57669940729022E-9, INFES

= 6.57669940729022E-9 ****)









= 1.23148184982824E-8 ****)











= 1.23148184982824E-8 ****)



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EqTSat =E=




= 1.23148184982824E-8 ****)





= 1.23148184982824E-8 ****)





= 1.23148184982824E-8 ****)


---- EqEnthP2Str =E= Enthalpy of 2 phase stream

EqEnthP2Str(1).. (0.0100285619317359)*Wetns(1) + H(1) - (1)*HVap(1) + (0)*HSatLiq(1) =E= 0 ;

(LHS = 0)


(LHS = 0)

EqEnthP2Str(3).. (0.0103635486804393)*Wetns(3) + H(3) - (0.85)*HVap(3) - (0.15)*HSatLiq(3) =E

= 0 ; (LHS = 0)


= 0 ; (LHS = 0)


(LHS = 0)


= 0 ; (LHS = 0)


= 0 ; (LHS = 0)

EqEnthP2Str(12).. (0.0103635486804393)*Wetns(12) + H(12) - (0.583629102463594)*HVap(12) - (0.

416370897536405)*HSatLiq(12) =E= 0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 98

EqEnthP2Str(25).. (0.0094553487502852)*Wetns(25) + H(25) - (1)*HVap(25) + (0)*HSatLiq(25) =E=

0 ; (LHS = 0)

EqEnthP2Str(26).. (0.00836169010981347)*Wetns(26) + H(26) - (1)*HVap(26) + (0)*HSatLiq(26) =E

= 0 ; (LHS = 0)


= 0 ; (LHS = 0)

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EqEnthP2Str =E= Enthalpy of 2 phase stream


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)

EqEnthP2Str(36).. (0.0103635486804393)*Wetns(36) + H(36) - (0.9999)*HVap(36) - (0.0001)*HSatL

iq(36) =E= 0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)

EqEnthP2Str(57).. (0.0118158135016933)*Wetns(57) + H(57) - (0.85)*HVap(57) - (0.15)*HSatLiq(5

7) =E= 0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


0 ; (LHS = 0)


1) =E= 0 ; (LHS = 0)


0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 100


= 0 ; (LHS = 0)


0 ; (LHS = 0)


5) =E= 0 ; (LHS = 0)

---- EqTP2 =G=

EqTP2(1).. T(1) - TSat(1) =G= 0 ; (LHS = 164.687388023361)

EqTP2(2).. T(2) - TSat(2) =G= 0 ; (LHS = 82.9611399253009)

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EqTP2 =G=

EqTP2(3).. T(3) - TSat(3) =G= 0 ; (LHS = 0)

EqTP2(4).. T(4) - TSat(4) =G= 0 ; (LHS = 0)

EqTP2(5).. T(5) - TSat(5) =G= 0 ; (LHS = 82.9611399253009)

EqTP2(6).. T(6) - TSat(6) =G= 0 ; (LHS = 0)

EqTP2(7).. T(7) - TSat(7) =G= 0 ; (LHS = 0)

EqTP2(12).. T(12) - TSat(12) =G= 0 ; (LHS = 1.13686837721616E-13)

EqTP2(25).. T(25) - TSat(25) =G= 0 ; (LHS = 0)

EqTP2(26).. T(26) - TSat(26) =G= 0 ; (LHS = 0)

EqTP2(31).. T(31) - TSat(31) =G= 0 ; (LHS = 0)

EqTP2(32).. T(32) - TSat(32) =G= 0 ; (LHS = 0)

EqTP2(33).. T(33) - TSat(33) =G= 0 ; (LHS = 0)

EqTP2(34).. T(34) - TSat(34) =G= 0 ; (LHS = 164.687388023361)

EqTP2(35).. T(35) - TSat(35) =G= 0 ; (LHS = 82.9611399252992)

EqTP2(36).. T(36) - TSat(36) =G= 0 ; (LHS = 1.13686837721616E-13)

EqTP2(47).. T(47) - TSat(47) =G= 0 ; (LHS = 164.687388023362)

EqTP2(48).. T(48) - TSat(48) =G= 0 ; (LHS = 164.687388023361)

EqTP2(49).. T(49) - TSat(49) =G= 0 ; (LHS = 0)

EqTP2(50).. T(50) - TSat(50) =G= 0 ; (LHS = 82.9611399252992)

EqTP2(51).. T(51) - TSat(51) =G= 0 ; (LHS = 0)

EqTP2(55).. T(55) - TSat(55) =G= 0 ; (LHS = 82.9611399252992)

EqTP2(56).. T(56) - TSat(56) =G= 0 ; (LHS = 21.8303521887313)

EqTP2(57).. T(57) - TSat(57) =G= 0 ; (LHS = 0)

EqTP2(58).. T(58) - TSat(58) =G= 0 ; (LHS = 164.687388023361)

EqTP2(59).. T(59) - TSat(59) =G= 0 ; (LHS = 82.9611399252992)

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EqTP2 =G=

EqTP2(60).. T(60) - TSat(60) =G= 0 ; (LHS = 0)

EqTP2(61).. T(61) - TSat(61) =G= 0 ; (LHS = 0)

EqTP2(62).. T(62) - TSat(62) =G= 0 ; (LHS = 164.687388023361)

EqTP2(63).. T(63) - TSat(63) =G= 0 ; (LHS = 44.4116628831039)

EqTP2(64).. T(64) - TSat(64) =G= 0 ; (LHS = 21.8303521887313)

EqTP2(65).. T(65) - TSat(65) =G= 0 ; (LHS = 0)

---- EqLogP21 =L=

EqLogP21(1).. Wetns(1) - YP2(1) =L= 0 ; (LHS = 0)


EqLogP21(3).. Wetns(3) - YP2(3) =L= 0 ; (LHS = -0.85)















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EqLogP21 =L=
















---- EqLogP22 =G=

EqLogP22(1).. Wetns(1) - 0.0001*YP2(1) =G= 0 ; (LHS = 0)


EqLogP22(3).. Wetns(3) - 0.0001*YP2(3) =G= 0 ; (LHS = 0.1499)






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EqLogP22 =G=

























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---- EqLogP23 =L=

EqLogP23(1).. T(1) - TSat(1) + 500*YP2(1) =L= 500 ; (LHS = 164.687388023361)


EqLogP23(3).. T(3) - TSat(3) + 500*YP2(3) =L= 500 ; (LHS = 500)







EqLogP23(26).. T(26) - TSat(26) + 500*YP2(26) =L= 500 ; (LHS = -1.13686837721616E-13)

EqLogP23(31).. T(31) - TSat(31) + 500*YP2(31) =L= 500 ; (LHS = -1.13686837721616E-13)














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EqLogP23 =L=









---- EqTrP2 =E=

EqTrP2(1).. TrP2(1) - 0.00154528456415249*TSat(1) =E= 0 ; (LHS = 0)















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EqTrP2 =E=

























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EqTrP2 =E=





---- EqLatHtVapP2 =E=

EqLatHtVapP2(1,H2O).. (64.2852084961303)*TrP2(1) + LatHtVapP2(1,H2O) =E= 0 ; (LHS = 0)



















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EqLatHtVapP2 =E=

























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---- EqEnthSatLiq1 =E=

EqEnthSatLiq1(8).. H(8) - HSatLiq(8) =E= 0 ; (LHS = 0)











---- EqnTfSatLiqVap =E=

EqnTfSatLiqVap(8).. T(8) - TSat(8) =E= 0 ; (LHS = 0)












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---- EqEnthLiqStr =E=

EqEnthLiqStr(9).. - (9.39707716715866E-6)*T(9) + 0.000277777777777778*LatHtVapLiq(9,H2O) + H(

9) =E= -0.069944520823574 ; (LHS = -0.069944520823574)

EqEnthLiqStr(17).. - (9.34353757021754E-6)*T(17) + 0.000277777777777778*LatHtVapLiq(17,H2O) +

H(17) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


H(18) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


H(19) =E= -0.069944520823574 ; (LHS = -0.069944520823574)


H(20) =E= -0.069944520823574 ; (LHS = -0.069944520823574)

---- EqTrLiq =E=

EqTrLiq(9).. - 0.00154528456415249*T(9) + TrLiq(9) =E= 0 ; (LHS = 0)





---- EqLatHtVapLiq =E=

EqLatHtVapLiq(9,H2O).. (26.122472028129)*TrLiq(9) + LatHtVapLiq(9,H2O) =E= 0 ; (LHS = 0)





---- EqEnthSatVap =E=

EqEnthSatVap(16).. - (9.48965944308724E-6)*TSat(16) + HSatVap(16) =E= -0.069944520823574 ; (L

HS = -0.069944520823574)

---- EqEnthSatVap1 =E=

EqEnthSatVap1(16).. H(16) - HSatVap(16) =E= 0 ; (LHS = 0)

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---- EqCompMolBalHPStmTurb =E= Component mol balance

EqCompMolBalHPStmTurb(1,H2).. Fc(1,H2) - Fc(2,H2) - Fc(3,H2) - Fc(4,H2) =E= 0 ; (LHS = 0)

EqCompMolBalHPStmTurb(1,O2).. Fc(1,O2) - Fc(2,O2) - Fc(3,O2) - Fc(4,O2) =E= 0 ; (LHS = 0)

EqCompMolBalHPStmTurb(1,N2).. Fc(1,N2) - Fc(2,N2) - Fc(3,N2) - Fc(4,N2) =E= 0 ; (LHS = 0)

EqCompMolBalHPStmTurb(1,CH4).. Fc(1,CH4) - Fc(2,CH4) - Fc(3,CH4) - Fc(4,CH4) =E= 0 ; (LHS = 0

)

EqCompMolBalHPStmTurb(1,CO).. Fc(1,CO) - Fc(2,CO) - Fc(3,CO) - Fc(4,CO) =E= 0 ; (LHS = 0)

EqCompMolBalHPStmTurb(1,CO2).. Fc(1,CO2) - Fc(2,CO2) - Fc(3,CO2) - Fc(4,CO2) =E= 0 ; (LHS = 0

)

EqCompMolBalHPStmTurb(1,H2O).. Fc(1,H2O) - Fc(2,H2O) - Fc(3,H2O) - Fc(4,H2O) =E= 0 ; (LHS = 0

)




EqCompMolBalHPStmTurb(2,CH4).. Fc(58,CH4) - Fc(59,CH4) - Fc(60,CH4) - Fc(61,CH4) =E= 0 ; (LHS

= 0)


EqCompMolBalHPStmTurb(2,CO2).. Fc(58,CO2) - Fc(59,CO2) - Fc(60,CO2) - Fc(61,CO2) =E= 0 ; (LHS

= 0)

EqCompMolBalHPStmTurb(2,H2O).. Fc(58,H2O) - Fc(59,H2O) - Fc(60,H2O) - Fc(61,H2O) =E= 0 ; (LHS

= 0)




EqCompMolBalHPStmTurb(3,CH4).. Fc(62,CH4) - Fc(63,CH4) - Fc(64,CH4) - Fc(65,CH4) =E= 0 ; (LHS

= 0)


EqCompMolBalHPStmTurb(3,CO2).. Fc(62,CO2) - Fc(63,CO2) - Fc(64,CO2) - Fc(65,CO2) =E= 0 ; (LHS

= 0)

EqCompMolBalHPStmTurb(3,H2O).. Fc(62,H2O) - Fc(63,H2O) - Fc(64,H2O) - Fc(65,H2O) =E= 0 ; (LHS

= 0)

---- EqInHPPHPStmTurb =E= Equating inlet HP Pressure to that of corresponding HP stream

model.lst Wed May 30 15:17:17 2018 113

EqInHPPHPStmTurb(1).. P(1) - InHPPHPStmTurb(1) =E= 0 ; (LHS = 0)


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EqInHPPHPStmTurb =E= Equating inlet HP Pressure to that of corresponding HP stream


---- EqInHPTHPStmTurb =E= Equating inlet HP temperature to that of corresponding HP stream

EqInHPTHPStmTurb(1).. T(1) - InHPTHPStmTurb(1) =E= 0 ; (LHS = 0)



---- EqOutMPPHPStmTurb =E= Equatiing outlet MP Pressure to that of corresponding MP stream

EqOutMPPHPStmTurb(1).. P(2) - OutMPPHPStmTurb(1) =E= 0 ; (LHS = 0)



---- EqOutLPPHPStmTurb =E= Equatiing outlet LP Pressure to that of corresponding LP stream

EqOutLPPHPStmTurb(1).. P(3) - OutLPPHPStmTurb(1) =E= 0 ; (LHS = 0)



---- EqPTRel1HPStmTurb =E= P T relationship for compression from high to medium pressure

EqPTRel1HPStmTurb(1).. (3.13485927191185)*InHPPHPStmTurb(1) - (0.817742119730613)*InHPTHPStmT

urb(1) - (7.05343336180167)*OutMPPHPStmTurb(1) + OutMPTHPStmTurb(1) =E= 0 ; (LHS = 0)





---- EqPTRel1aHPStmTurb =E=

EqPTRel1aHPStmTurb(1).. OutMPTHPStmTurb(1) - Dum11HPStmTurb(1) - Dum22HPStmTurb(1) =E= 0 ; (L

HS = 0)


HS = 0)


HS = 0)

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---- EqPTRel1bHPStmTurb =E=

EqPTRel1bHPStmTurb(1).. - Dum33HPStmTurb(1) - Dum44HPStmTurb(1) =E= -530 ; (LHS = -530)



---- EqPTRel1cHPStmTurb =E=

EqPTRel1cHPStmTurb(1).. T(2) - Dum55HPStmTurb(1) - Dum66HPStmTurb(1) =E= 0 ; (LHS = 0)



---- EqPTRel1dHPStmTurb =E=

EqPTRel1dHPStmTurb(1).. - Dum11HPStmTurb(1) + Dum55HPStmTurb(1) =E= 0 ; (LHS = 0)



---- EqPTRel1eHPStmTurb =E=

EqPTRel1eHPStmTurb(1).. - Dum44HPStmTurb(1) + Dum66HPStmTurb(1) =E= 0 ; (LHS = 0)



---- EqPTRel1fHPStmTurb =L=

EqPTRel1fHPStmTurb(1).. - 701*Y(1) + Dum55HPStmTurb(1) =L= 0 ; (LHS = -132.450522957805)

EqPTRel1fHPStmTurb(2).. - 701*Y(58) + Dum55HPStmTurb(2) =L= 0 ; (LHS = -132.450522957805)

EqPTRel1fHPStmTurb(3).. - 701*Y(62) + Dum55HPStmTurb(3) =L= 0 ; (LHS = 0)

---- EqPTRel1gHPStmTurb =L=

EqPTRel1gHPStmTurb(1).. 701*Y(1) + Dum66HPStmTurb(1) =L= 701 ; (LHS = 701)


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EqPTRel1gHPStmTurb =L=


---- EqPTRel1hHPStmTurb =L=

EqPTRel1hHPStmTurb(1).. - 701*Y(1) + Dum11HPStmTurb(1) =L= 0 ; (LHS = -132.450522957805)

EqPTRel1hHPStmTurb(2).. - 701*Y(58) + Dum11HPStmTurb(2) =L= 0 ; (LHS = -132.450522957805)

EqPTRel1hHPStmTurb(3).. - 701*Y(62) + Dum11HPStmTurb(3) =L= 0 ; (LHS = 0)

---- EqPTRel1iHPStmTurb =L=

EqPTRel1iHPStmTurb(1).. 701*Y(1) + Dum44HPStmTurb(1) =L= 701 ; (LHS = 701)



---- EqPTRel1jHPStmTurb =L=

EqPTRel1jHPStmTurb(1).. 701*Y(1) + Dum22HPStmTurb(1) =L= 701 ; (LHS = 701)

EqPTRel1jHPStmTurb(2).. 701*Y(58) + Dum22HPStmTurb(2) =L= 701 ; (LHS = 701)

EqPTRel1jHPStmTurb(3).. 701*Y(62) + Dum22HPStmTurb(3) =L= 701 ; (LHS = 568.549477042195)

---- EqPTRel1kHPStmTurb =L=

EqPTRel1kHPStmTurb(1).. - 701*Y(1) + Dum33HPStmTurb(1) =L= 0 ; (LHS = -171)

EqPTRel1kHPStmTurb(2).. - 701*Y(58) + Dum33HPStmTurb(2) =L= 0 ; (LHS = -171)

EqPTRel1kHPStmTurb(3).. - 701*Y(62) + Dum33HPStmTurb(3) =L= 0 ; (LHS = 0)

---- EqPTRel2HPStmTurb =E=

EqPTRel2HPStmTurb(1).. (5.43593923888347)*OutMPPHPStmTurb(1) - (15.5312549682385)*OutLPPHPStm

Turb(1) - (0.770679888793187)*OutMPTHPStmTurb(1) + OutLPTHPStmTurb(1) =E= 0 ; (LHS = 0)





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---- EqPTRel2aHPStmTurb =E=

EqPTRel2aHPStmTurb(1).. OutLPTHPStmTurb(1) - Dum1HPStmTurb(1) - Dum2HPStmTurb(1) =E= 0 ; (LHS

= 0)


= 0)


= 0)

---- EqPTRel2bHPStmTurb =E=




---- EqPTRel2cHPStmTurb =E=




---- EqPTRel2dHPStmTurb =E=




---- EqPTRel2eHPStmTurb =E=




---- EqPTRel2fHPStmTurb =L=

EqPTRel2fHPStmTurb(1).. Dum5HPStmTurb(1) - 581*YLP(1) =L= 0 ; (LHS = -142.830352259696)

EqPTRel2fHPStmTurb(2).. Dum5HPStmTurb(2) - 581*YLP(2) =L= 0 ; (LHS = -142.830352259696)

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EqPTRel2fHPStmTurb =L=

EqPTRel2fHPStmTurb(3).. Dum5HPStmTurb(3) - 581*YLP(3) =L= 0 ; (LHS = 0)

---- EqPTRel2gHPStmTurb =L=

EqPTRel2gHPStmTurb(1).. Dum6HPStmTurb(1) + 581*YLP(1) =L= 581 ; (LHS = 581)

EqPTRel2gHPStmTurb(2).. Dum6HPStmTurb(2) + 581*YLP(2) =L= 581 ; (LHS = 581.000000070965)

EqPTRel2gHPStmTurb(3).. Dum6HPStmTurb(3) + 581*YLP(3) =L= 581 ; (LHS = 460)

---- EqPTRel2hHPStmTurb =L=

EqPTRel2hHPStmTurb(1).. Dum1HPStmTurb(1) - 581*YLP(1) =L= 0 ; (LHS = -142.830352259696)

EqPTRel2hHPStmTurb(2).. Dum1HPStmTurb(2) - 581*YLP(2) =L= 0 ; (LHS = -142.830352259696)

EqPTRel2hHPStmTurb(3).. Dum1HPStmTurb(3) - 581*YLP(3) =L= 0 ; (LHS = 0)

---- EqPTRel2iHPStmTurb =L=

EqPTRel2iHPStmTurb(1).. Dum4HPStmTurb(1) + 581*YLP(1) =L= 581 ; (LHS = 581)

EqPTRel2iHPStmTurb(2).. Dum4HPStmTurb(2) + 581*YLP(2) =L= 581 ; (LHS = 581.000000070965)

EqPTRel2iHPStmTurb(3).. Dum4HPStmTurb(3) + 581*YLP(3) =L= 581 ; (LHS = 460)

---- EqPTRel2jHPStmTurb =L=

EqPTRel2jHPStmTurb(1).. Dum2HPStmTurb(1) + 581*YLP(1) =L= 581 ; (LHS = 581)

EqPTRel2jHPStmTurb(2).. Dum2HPStmTurb(2) + 581*YLP(2) =L= 581 ; (LHS = 581)

EqPTRel2jHPStmTurb(3).. Dum2HPStmTurb(3) + 581*YLP(3) =L= 581 ; (LHS = 438.169647740304)

---- EqPTRel2kHPStmTurb =L=

EqPTRel2kHPStmTurb(1).. Dum3HPStmTurb(1) - 581*YLP(1) =L= 0 ; (LHS = -121)

EqPTRel2kHPStmTurb(2).. Dum3HPStmTurb(2) - 581*YLP(2) =L= 0 ; (LHS = -121.000000070965)

EqPTRel2kHPStmTurb(3).. Dum3HPStmTurb(3) - 581*YLP(3) =L= 0 ; (LHS = 0)

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---- EqPTRel2lHPStmTurb =G=

EqPTRel2lHPStmTurb(1).. - YModeHPStmTurb(1,LPExt) + YLP(1) =G= 0 ; (LHS = 1)



---- EqPTRel2mHPStmTurb =G=

EqPTRel2mHPStmTurb(1).. - YModeHPStmTurb(1,LPBkPr) + YLP(1) =G= 0 ; (LHS = 0)



---- EqPTRel2nHPStmTurb =G=

EqPTRel2nHPStmTurb(1).. - YModeHPStmTurb(1,VPCond) + YLP(1) =G= 0 ; (LHS = 1)



---- EqPTRel3HPStmTurb =E=

EqPTRel3HPStmTurb(1).. Wetns(4) =E= 0.15 ; (LHS = 0.15)



---- EqMPWorkHPStmTurb =E=

EqMPWorkHPStmTurb(1).. - (0.00129018676456021)*Fc(1,H2O) - (3639.78325890297)*H(1) + (3639.78

325890297)*H(2) + MPWorkHPStmTurb(1) =E= 0 ; (LHS = 0)

EqMPWorkHPStmTurb(2).. - (0.00129018676456021)*Fc(58,H2O) - (16385.9503504084)*H(58) + (16385

.9503504084)*H(59) + MPWorkHPStmTurb(2) =E= 0 ; (LHS = 0)

EqMPWorkHPStmTurb(3).. - (0.00167259321335331)*Fc(62,H2O) + (0)*H(62) + (0)*H(63) + MPWorkHPS

tmTurb(3) =E= 0 ; (LHS = 0)

---- EqLPWorkHPStmTurb =E=

EqLPWorkHPStmTurb(1).. - (0.00283093774561763)*Fc(1,H2O) + (0.00283093774561763)*Fc(2,H2O) -

(3639.78325890297)*H(2) + (3639.78325890297)*H(3) + LPWorkHPStmTurb(1) =E= 0 ; (LHS = 0)

EqLPWorkHPStmTurb(2).. - (0.00127640544286937)*Fc(58,H2O) + (0.00127640544286937)*Fc(59,H2O)

- (12504.3347030767)*H(59) + (12504.3347030767)*H(60) + LPWorkHPStmTurb(2) =E= 0 ; (LHS = 0)

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EqLPWorkHPStmTurb =E=

EqLPWorkHPStmTurb(3).. - (0.000683499793628028)*Fc(62,H2O) + (0.000683499793628028)*Fc(63,H2O

) + (0)*H(63) + (0)*H(64) + LPWorkHPStmTurb(3) =E= 0 ; (LHS = 0)

---- EqVPWorkHPStmTurb =E=

EqVPWorkHPStmTurb(1).. - (0.00121526674242521)*Fc(1,H2O) + (0.00121526674242521)*Fc(2,H2O) +

(0.00121526674242521)*Fc(3,H2O) + (0)*H(3) + (0)*H(4) + VPWorkHPStmTurb(1) =E= 0 ; (LHS = 0)

EqVPWorkHPStmTurb(2).. - (0.00276979904517345)*Fc(58,H2O) + (0.00276979904517345)*Fc(59,H2O)

+ (0.00276979904517345)*Fc(60,H2O) - (11138.8529129714)*H(60) + (11138.8529129714)*H(61) + VPW

orkHPStmTurb(2) =E= 0 ; (LHS = 0)

EqVPWorkHPStmTurb(3).. - (0.00298029824554574)*Fc(62,H2O) + (0.00298029824554574)*Fc(63,H2O)

+ (0.00298029824554574)*Fc(64,H2O) + (0)*H(64) + (0)*H(65) + VPWorkHPStmTurb(3) =E= 0 ; (LHS =

0)

---- EqTotWorkHPStmTurb =E=

EqTotWorkHPStmTurb(1).. - MPWorkHPStmTurb(1) - LPWorkHPStmTurb(1) - VPWorkHPStmTurb(1) + TotW






---- EqWetCnst1HPStmTurb =L=

EqWetCnst1HPStmTurb(1).. Wetns(2) =L= 0.15 ; (LHS = 0)



---- EqWetCnst2HPStmTurb =L=

EqWetCnst2HPStmTurb(1).. Wetns(3) =L= 0.15 ; (LHS = 0.15)



---- EqLogMode1HPStmTurb =G=

EqLogMode1HPStmTurb(1).. - YModeHPStmTurb(1,MPExt) + YModeHPStmTurb(1,LPBkPr) + YModeHPStmTur

b(1,VPCond) =G= 0 ; (LHS = 0)


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b(2,VPCond) =G= 0 ; (LHS = 0)


b(3,VPCond) =G= 0 ; (LHS = 0)

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EqLogMode2HPStmTurb(1).. - YModeHPStmTurb(1,LPExt) + YModeHPStmTurb(1,VPCond) =G= 0 ; (LHS =

0)


0)


0)

---- EqLogMode3HPStmTurb =L=

EqLogMode3HPStmTurb(1).. YModeHPStmTurb(1,LPBkPr) + YModeHPStmTurb(1,LPExt) =L= 1 ; (LHS = 1)




EqLogMode4HPStmTurb(1).. YModeHPStmTurb(1,MPBkPr) + YModeHPStmTurb(1,MPExt) =L= 1 ; (LHS = 1)




EqLogMode5HPStmTurb(1).. YModeHPStmTurb(1,MPBkPr) + YModeHPStmTurb(1,LPBkPr) + YModeHPStmTurb

(1,VPCond) =L= 1 ; (LHS = 1)


(2,VPCond) =L= 1 ; (LHS = 1)


(3,VPCond) =L= 1 ; (LHS = 0)


EqLogMode6HPStmTurb(1).. Wetns(2) + YModeHPStmTurb(1,MPExt) =L= 1 ; (LHS = 1)




EqLogMode7HPStmTurb(1).. Wetns(3) + YModeHPStmTurb(1,LPExt) =L= 1 ; (LHS = 0.15)

EqLogMode7HPStmTurb(2).. Wetns(60) + YModeHPStmTurb(2,LPExt) =L= 1 ; (LHS = 1)

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EqLogMode7HPStmTurb =L=

EqLogMode7HPStmTurb(3).. Wetns(64) + YModeHPStmTurb(3,LPExt) =L= 1 ; (LHS = 0)


EqLogMode8HPStmTurb(1,MPBkPr).. Y(1) - YModeHPStmTurb(1,MPBkPr) =G= 0 ; (LHS = 1)

EqLogMode8HPStmTurb(1,MPExt).. Y(1) - YModeHPStmTurb(1,MPExt) =G= 0 ; (LHS = 0)

EqLogMode8HPStmTurb(1,LPBkPr).. Y(1) - YModeHPStmTurb(1,LPBkPr) =G= 0 ; (LHS = 0)

EqLogMode8HPStmTurb(1,LPExt).. Y(1) - YModeHPStmTurb(1,LPExt) =G= 0 ; (LHS = 1)

EqLogMode8HPStmTurb(1,VPCond).. Y(1) - YModeHPStmTurb(1,VPCond) =G= 0 ; (LHS = 1)











---- EqLogBnd1HPStmTurb =L=

EqLogBnd1HPStmTurb(1).. F(2) - 100000000*YModeHPStmTurb(1,MPBkPr) - 100000000*YModeHPStmTurb(

1,MPExt) =L= 0 ; (LHS = -100000000)

EqLogBnd1HPStmTurb(2).. F(59) - 100000000*YModeHPStmTurb(2,MPBkPr) - 100000000*YModeHPStmTurb

(2,MPExt) =L= 0 ; (LHS = -99996118.3843527)

EqLogBnd1HPStmTurb(3).. F(63) - 100000000*YModeHPStmTurb(3,MPBkPr) - 100000000*YModeHPStmTurb

(3,MPExt) =L= 0 ; (LHS = 0)


EqLogBnd2HPStmTurb(1).. F(3) - 100000000*YModeHPStmTurb(1,LPBkPr) - 100000000*YModeHPStmTurb(

1,LPExt) =L= 0 ; (LHS = -99996360.2167411)

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EqLogBnd2HPStmTurb =L=

EqLogBnd2HPStmTurb(2).. F(60) - 100000000*YModeHPStmTurb(2,LPBkPr) - 100000000*YModeHPStmTurb

(2,LPExt) =L= 0 ; (LHS = -99998634.5182099)

EqLogBnd2HPStmTurb(3).. F(64) - 100000000*YModeHPStmTurb(3,LPBkPr) - 100000000*YModeHPStmTurb

(3,LPExt) =L= 0 ; (LHS = 0)


EqLogBnd3HPStmTurb(1).. F(4) - 100000000*YModeHPStmTurb(1,VPCond) =L= 0 ; (LHS = 0)

EqLogBnd3HPStmTurb(2).. F(61) - 100000000*YModeHPStmTurb(2,VPCond) =L= 0 ; (LHS = -99988861.1

47087)

EqLogBnd3HPStmTurb(3).. F(65) - 100000000*YModeHPStmTurb(3,VPCond) =L= 0 ; (LHS = 0)


EqLogBnd4HPStmTurb(1,1).. F(1) - 100000000*Y(1) =L= 0 ; (LHS = -99996360.2167411)

EqLogBnd4HPStmTurb(2,58).. F(58) - 100000000*Y(58) =L= 0 ; (LHS = -99983614.0496496)

EqLogBnd4HPStmTurb(3,62).. F(62) - 100000000*Y(62) =L= 0 ; (LHS = 0)

---- EqCompMolBalMPStmTurb =E= Component mol balance

EqCompMolBalMPStmTurb(1,H2).. Fc(5,H2) - Fc(6,H2) - Fc(7,H2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(1,O2).. Fc(5,O2) - Fc(6,O2) - Fc(7,O2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(1,N2).. Fc(5,N2) - Fc(6,N2) - Fc(7,N2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(1,CH4).. Fc(5,CH4) - Fc(6,CH4) - Fc(7,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(1,CO).. Fc(5,CO) - Fc(6,CO) - Fc(7,CO) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(1,CO2).. Fc(5,CO2) - Fc(6,CO2) - Fc(7,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(1,H2O).. Fc(5,H2O) - Fc(6,H2O) - Fc(7,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(2,H2).. Fc(55,H2) - Fc(56,H2) - Fc(57,H2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(2,O2).. Fc(55,O2) - Fc(56,O2) - Fc(57,O2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(2,N2).. Fc(55,N2) - Fc(56,N2) - Fc(57,N2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(2,CH4).. Fc(55,CH4) - Fc(56,CH4) - Fc(57,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(2,CO).. Fc(55,CO) - Fc(56,CO) - Fc(57,CO) =E= 0 ; (LHS = 0)

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EqCompMolBalMPStmTurb =E= Component mol balance

EqCompMolBalMPStmTurb(2,CO2).. Fc(55,CO2) - Fc(56,CO2) - Fc(57,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalMPStmTurb(2,H2O).. Fc(55,H2O) - Fc(56,H2O) - Fc(57,H2O) =E= 0 ; (LHS = 0)

---- EqInMPPMPStmTurb =E= Equating inlet HP Pressure to that of corresponding HP stream

EqInMPPMPStmTurb(1).. P(5) - InMPPMPStmTurb(1) =E= 0 ; (LHS = 0)

EqInMPPMPStmTurb(2).. P(55) - InMPPMPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqInMPTMPStmTurb =E= Equating inlet HP temperature to that of corresponding HP stream

EqInMPTMPStmTurb(1).. T(5) - InMPTMPStmTurb(1) =E= 0 ; (LHS = 0)

EqInMPTMPStmTurb(2).. T(55) - InMPTMPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqOutLPPMPStmTurb =E= Equatiing outlet LP Pressure to that of corresponding LP stream

EqOutLPPMPStmTurb(1).. P(6) - OutLPPMPStmTurb(1) =E= 0 ; (LHS = 0)

EqOutLPPMPStmTurb(2).. P(56) - OutLPPMPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqPTRel1MPStmTurb =E=

EqPTRel1MPStmTurb(1).. (5.43593923888347)*InMPPMPStmTurb(1) - (0.770679888793187)*InMPTMPStmT

urb(1) - (15.5312549682385)*OutLPPMPStmTurb(1) + OutLPTMPStmTurb(1) =E= 0 ; (LHS = 0)

EqPTRel1MPStmTurb(2).. (5.43593923888347)*InMPPMPStmTurb(2) - (0.770679888793187)*InMPTMPStmT

urb(2) - (15.5312549682385)*OutLPPMPStmTurb(2) + OutLPTMPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqPTRel1aMPStmTurb =E=

EqPTRel1aMPStmTurb(1).. OutLPTMPStmTurb(1) - Dum11MPStmTurb(1) - Dum22MPStmTurb(1) =E= 0 ; (L

HS = 0)

EqPTRel1aMPStmTurb(2).. OutLPTMPStmTurb(2) - Dum11MPStmTurb(2) - Dum22MPStmTurb(2) =E= 0 ; (L

HS = 0)

---- EqPTRel1bMPStmTurb =E=

EqPTRel1bMPStmTurb(1).. - Dum33MPStmTurb(1) - Dum44MPStmTurb(1) =E= -460 ; (LHS = -460)

EqPTRel1bMPStmTurb(2).. - Dum33MPStmTurb(2) - Dum44MPStmTurb(2) =E= -460 ; (LHS = -460)

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---- EqPTRel1cMPStmTurb =E=

EqPTRel1cMPStmTurb(1).. T(6) - Dum55MPStmTurb(1) - Dum66MPStmTurb(1) =E= 0 ; (LHS = 0)

EqPTRel1cMPStmTurb(2).. T(56) - Dum55MPStmTurb(2) - Dum66MPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqPTRel1dMPStmTurb =E=

EqPTRel1dMPStmTurb(1).. - Dum11MPStmTurb(1) + Dum55MPStmTurb(1) =E= 0 ; (LHS = 0)

EqPTRel1dMPStmTurb(2).. - Dum11MPStmTurb(2) + Dum55MPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqPTRel1eMPStmTurb =E=

EqPTRel1eMPStmTurb(1).. - Dum44MPStmTurb(1) + Dum66MPStmTurb(1) =E= 0 ; (LHS = 0)

EqPTRel1eMPStmTurb(2).. - Dum44MPStmTurb(2) + Dum66MPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqPTRel1fMPStmTurb =L=

EqPTRel1fMPStmTurb(1).. - 581*Y(5) + Dum55MPStmTurb(1) =L= 0 ; (LHS = -142.830352259696)

EqPTRel1fMPStmTurb(2).. - 581*Y(55) + Dum55MPStmTurb(2) =L= 0 ; (LHS = 0)

---- EqPTRel1gMPStmTurb =L=

EqPTRel1gMPStmTurb(1).. 581*Y(5) + Dum66MPStmTurb(1) =L= 581 ; (LHS = 581)

EqPTRel1gMPStmTurb(2).. 581*Y(55) + Dum66MPStmTurb(2) =L= 581 ; (LHS = 460)

---- EqPTRel1hMPStmTurb =L=

EqPTRel1hMPStmTurb(1).. - 581*Y(5) + Dum11MPStmTurb(1) =L= 0 ; (LHS = -142.830352259696)

EqPTRel1hMPStmTurb(2).. - 581*Y(55) + Dum11MPStmTurb(2) =L= 0 ; (LHS = 0)

---- EqPTRel1iMPStmTurb =L=

EqPTRel1iMPStmTurb(1).. 581*Y(5) + Dum44MPStmTurb(1) =L= 581 ; (LHS = 581)

EqPTRel1iMPStmTurb(2).. 581*Y(55) + Dum44MPStmTurb(2) =L= 581 ; (LHS = 460)

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---- EqPTRel1jMPStmTurb =L=

EqPTRel1jMPStmTurb(1).. 581*Y(5) + Dum22MPStmTurb(1) =L= 581 ; (LHS = 581)

EqPTRel1jMPStmTurb(2).. 581*Y(55) + Dum22MPStmTurb(2) =L= 581 ; (LHS = 438.169647740304)

---- EqPTRel1kMPStmTurb =L=

EqPTRel1kMPStmTurb(1).. - 581*Y(5) + Dum33MPStmTurb(1) =L= 0 ; (LHS = -121)

EqPTRel1kMPStmTurb(2).. - 581*Y(55) + Dum33MPStmTurb(2) =L= 0 ; (LHS = 0)

---- EqPTRel2MPStmTurb =E=

EqPTRel2MPStmTurb(1).. Wetns(7) =E= 0.15 ; (LHS = 0.15)

EqPTRel2MPStmTurb(2).. Wetns(57) =E= 0.15 ; (LHS = 0.15)

---- EqLPWorkMPStmTurb =E=

EqLPWorkMPStmTurb(1).. - (0.00283093774561763)*Fc(5,H2O) - (1766.19920651386)*H(5) + (1766.19

920651386)*H(6) + LPWorkMPStmTurb(1) =E= 0 ; (LHS = 0)

EqLPWorkMPStmTurb(2).. - (0.00106590624242113)*Fc(55,H2O) + (0)*H(55) + (0)*H(56) + LPWorkMPS

tmTurb(2) =E= 0 ; (LHS = 0)

---- EqVPWorkMPStmTurb =E=

EqVPWorkMPStmTurb(1).. - (0.00121526674234924)*Fc(5,H2O) + (0.00121526674234924)*Fc(6,H2O) +

(0)*H(6) + (0)*H(7) + VPWorkMPStmTurb(1) =E= 0 ; (LHS = 0)

EqVPWorkMPStmTurb(2).. - (0.0029802982456217)*Fc(55,H2O) + (0.0029802982456217)*Fc(56,H2O) +

(0)*H(56) + (0)*H(57) + VPWorkMPStmTurb(2) =E= 0 ; (LHS = 0)

---- EqTotWorkMPStmTurb =E=

EqTotWorkMPStmTurb(1).. - LPWorkMPStmTurb(1) - VPWorkMPStmTurb(1) + TotWorkMPStmTurb(1) =E= 0

; (LHS = 0)

EqTotWorkMPStmTurb(2).. - LPWorkMPStmTurb(2) - VPWorkMPStmTurb(2) + TotWorkMPStmTurb(2) =E= 0

; (LHS = 0)

---- EqWetCnst1MPStmTurb =L=

EqWetCnst1MPStmTurb(1).. Wetns(6) =L= 0.15 ; (LHS = 0.15)

EqWetCnst1MPStmTurb(2).. Wetns(56) =L= 0.15 ; (LHS = 0)

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---- EqLogMode1MPStmTurb =G=

EqLogMode1MPStmTurb(1).. - YModeMPStmTurb(1,LPExt) + YModeMPStmTurb(1,VPCond) =G= 0 ; (LHS =

0)

EqLogMode1MPStmTurb(2).. - YModeMPStmTurb(2,LPExt) + YModeMPStmTurb(2,VPCond) =G= 0 ; (LHS =

0)

---- EqLogMode2MPStmTurb =L=

EqLogMode2MPStmTurb(1).. YModeMPStmTurb(1,LPBkPr) + YModeMPStmTurb(1,LPExt) =L= 1 ; (LHS = 1)

EqLogMode2MPStmTurb(2).. YModeMPStmTurb(2,LPBkPr) + YModeMPStmTurb(2,LPExt) =L= 1 ; (LHS = 0)


EqLogMode3MPStmTurb(1).. YModeMPStmTurb(1,LPBkPr) + YModeMPStmTurb(1,VPCond) =L= 1 ; (LHS = 1

)

EqLogMode3MPStmTurb(2).. YModeMPStmTurb(2,LPBkPr) + YModeMPStmTurb(2,VPCond) =L= 1 ; (LHS = 0

)


EqLogMode4MPStmTurb(1).. Wetns(6) + YModeMPStmTurb(1,LPExt) =L= 1 ; (LHS = 0.15)

EqLogMode4MPStmTurb(2).. Wetns(56) + YModeMPStmTurb(2,LPExt) =L= 1 ; (LHS = 0)

---- EqLogMode5MPStmTurb =G=

EqLogMode5MPStmTurb(1,LPBkPr).. Y(5) - YModeMPStmTurb(1,LPBkPr) =G= 0 ; (LHS = 0)

EqLogMode5MPStmTurb(1,LPExt).. Y(5) - YModeMPStmTurb(1,LPExt) =G= 0 ; (LHS = 1)

EqLogMode5MPStmTurb(1,VPCond).. Y(5) - YModeMPStmTurb(1,VPCond) =G= 0 ; (LHS = 1)

EqLogMode5MPStmTurb(2,LPBkPr).. Y(55) - YModeMPStmTurb(2,LPBkPr) =G= 0 ; (LHS = 0)

EqLogMode5MPStmTurb(2,LPExt).. Y(55) - YModeMPStmTurb(2,LPExt) =G= 0 ; (LHS = 0)

EqLogMode5MPStmTurb(2,VPCond).. Y(55) - YModeMPStmTurb(2,VPCond) =G= 0 ; (LHS = 0)

---- EqLogBnd1MPStmTurb =L=

EqLogBnd1MPStmTurb(1).. F(6) - 100000000*YModeMPStmTurb(1,LPBkPr) - 100000000*YModeMPStmTurb(

1,LPExt) =L= 0 ; (LHS = -99998233.8007935)

EqLogBnd1MPStmTurb(2).. F(56) - 100000000*YModeMPStmTurb(2,LPBkPr) - 100000000*YModeMPStmTurb

(2,LPExt) =L= 0 ; (LHS = 0)

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EqLogBnd2MPStmTurb(1).. F(7) - 100000000*YModeMPStmTurb(1,VPCond) =L= 0 ; (LHS = 0)

EqLogBnd2MPStmTurb(2).. F(57) - 100000000*YModeMPStmTurb(2,VPCond) =L= 0 ; (LHS = 0)


EqLogBnd3MPStmTurb(1,5).. F(5) - 100000000*Y(5) =L= 0 ; (LHS = -99998233.8007935)

EqLogBnd3MPStmTurb(2,55).. F(55) - 100000000*Y(55) =L= 0 ; (LHS = 0)

---- EqCompMolBalVacCondTurb =E= Component mass bal

EqCompMolBalVacCondTurb(1,H2).. Fc(4,H2) + Fc(7,H2) - Fc(8,H2) + Fc(57,H2) + Fc(61,H2) + Fc(6

5,H2) =E= 0 ; (LHS = 0)

EqCompMolBalVacCondTurb(1,O2).. Fc(4,O2) + Fc(7,O2) - Fc(8,O2) + Fc(57,O2) + Fc(61,O2) + Fc(6

5,O2) =E= 0 ; (LHS = 0)

EqCompMolBalVacCondTurb(1,N2).. Fc(4,N2) + Fc(7,N2) - Fc(8,N2) + Fc(57,N2) + Fc(61,N2) + Fc(6

5,N2) =E= 0 ; (LHS = 0)

EqCompMolBalVacCondTurb(1,CH4).. Fc(4,CH4) + Fc(7,CH4) - Fc(8,CH4) + Fc(57,CH4) + Fc(61,CH4)

+ Fc(65,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalVacCondTurb(1,CO).. Fc(4,CO) + Fc(7,CO) - Fc(8,CO) + Fc(57,CO) + Fc(61,CO) + Fc(6

5,CO) =E= 0 ; (LHS = 0)

EqCompMolBalVacCondTurb(1,CO2).. Fc(4,CO2) + Fc(7,CO2) - Fc(8,CO2) + Fc(57,CO2) + Fc(61,CO2)

+ Fc(65,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalVacCondTurb(1,H2O).. Fc(4,H2O) + Fc(7,H2O) - Fc(8,H2O) + Fc(57,H2O) + Fc(61,H2O)

+ Fc(65,H2O) =E= 0 ; (LHS = 0)

---- EqEnthBalVacCondTurb =E= Energy balance

EqEnthBalVacCondTurb(1).. (0.0686147825047606)*F(4) + (0.0686147825046847)*F(7) - (0.07865822

39812)*F(8) + (0.0686147825047606)*F(57) + (0.0686147825047606)*F(61) + (0.0686147825046847)*F

(65) + (0)*H(4) + (0)*H(7) + (11138.8529129714)*H(8) + (0)*H(57)

- (11138.8529129714)*H(61) + (0)*H(65) + HtLdVacCondTurb(1) =E= 0 ; (LHS = 0)

---- EqMassFCW =E= calculate mass flowrate of cooling water (kg per s)

EqMassFCW(1).. HtLdVacCondTurb(1) - 0.08368*MassFCW =E= 0 ; (LHS = 0)

---- EqPr1VacCondTurb =E= equates Vacuum pressure to pressure of inlet stream

EqPr1VacCondTurb(1,4).. P(4) =E= 0.2 ; (LHS = 0.2)

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EqPr1VacCondTurb =E= equates Vacuum pressure to pressure of inlet stream



---- EqPr2VacCondTurb =E= equates Vacuum pressure to pressure of outlet stream


---- EqWorkPumpVCT =E= Work for vacuum pump in MW (mass is kg per s)

EqWorkPumpVCT(1).. - 0.00069*MassFCW + WorkPumpVCT =E= 0 ; (LHS = 0)

---- EqCompMolBalPump =E= Component mass bal

EqCompMolBalPump(VP,H2).. Fc(8,H2) - Fc(9,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(VP,O2).. Fc(8,O2) - Fc(9,O2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(VP,N2).. Fc(8,N2) - Fc(9,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(VP,CH4).. Fc(8,CH4) - Fc(9,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPump(VP,CO).. Fc(8,CO) - Fc(9,CO) =E= 0 ; (LHS = 0)

EqCompMolBalPump(VP,CO2).. Fc(8,CO2) - Fc(9,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(VP,H2O).. Fc(8,H2O) - Fc(9,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,H2).. Fc(13,H2) - Fc(18,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,O2).. Fc(13,O2) - Fc(18,O2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,N2).. Fc(13,N2) - Fc(18,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,CH4).. Fc(13,CH4) - Fc(18,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,CO).. Fc(13,CO) - Fc(18,CO) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,CO2).. Fc(13,CO2) - Fc(18,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(MP,H2O).. Fc(13,H2O) - Fc(18,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HP,H2).. Fc(14,H2) - Fc(19,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HP,O2).. Fc(14,O2) - Fc(19,O2) =E= 0 ; (LHS = 0)

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EqCompMolBalPump =E= Component mass bal

EqCompMolBalPump(HP,N2).. Fc(14,N2) - Fc(19,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HP,CH4).. Fc(14,CH4) - Fc(19,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HP,CO).. Fc(14,CO) - Fc(19,CO) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HP,CO2).. Fc(14,CO2) - Fc(19,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HP,H2O).. Fc(14,H2O) - Fc(19,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,H2).. Fc(15,H2) - Fc(20,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,O2).. Fc(15,O2) - Fc(20,O2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,N2).. Fc(15,N2) - Fc(20,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,CH4).. Fc(15,CH4) - Fc(20,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,CO).. Fc(15,CO) - Fc(20,CO) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,CO2).. Fc(15,CO2) - Fc(20,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalPump(HRSG,H2O).. Fc(15,H2O) - Fc(20,H2O) =E= 0 ; (LHS = 0)

---- EqTEqPump =E= Tin = Tout

EqTEqPump(VP).. T(8) - T(9) =E= 0 ; (LHS = 0)

EqTEqPump(MP).. T(13) - T(18) =E= 0 ; (LHS = 0)

EqTEqPump(HP).. T(14) - T(19) =E= 0 ; (LHS = 0)

EqTEqPump(HRSG).. T(15) - T(20) =E= 0 ; (LHS = 0)

---- EqPgePump =G= Pout >= Pin

EqPgePump(VP).. - P(8) + P(9) =G= 0 ; (LHS = 1.2)

EqPgePump(MP).. - P(13) + P(18) =G= 0 ; (LHS = 18.6)

EqPgePump(HP).. - P(14) + P(19) =G= 0 ; (LHS = 43.6)

EqPgePump(HRSG).. - P(15) + P(20) =G= 0 ; (LHS = 43.6)

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---- EqWorkPump =E= Work done by pump

EqWorkPump(VP).. - (6E-7)*F(8) + (0.00556942645648572)*P(8) - (0.00556942645648572)*P(9) + Wo

rkPump(VP) =E= 0 ; (LHS = 0)

EqWorkPump(MP).. - (9.3E-6)*F(13) + (0)*P(13) + (0)*P(18) + WorkPump(MP) =E= 0 ; (LHS = 0)

EqWorkPump(HP).. - (2.18E-5)*F(14) + (0)*P(14) + (0)*P(19) + WorkPump(HP) =E= 0 ; (LHS = 0)

EqWorkPump(HRSG).. - (2.18E-5)*F(15) + (0.0106308034267167)*P(15) - (0.0106308034267167)*P(20

) + WorkPump(HRSG) =E= 0 ; (LHS = 0)

---- EqCompMolBalCondHdr =E= Component mass bal

EqCompMolBalCondHdr(1,H2).. Fc(10,H2) - Fc(11,H2) + Fc(37,H2) + Fc(38,H2) =E= 0 ; (LHS = 0)

EqCompMolBalCondHdr(1,O2).. Fc(10,O2) - Fc(11,O2) + Fc(37,O2) + Fc(38,O2) =E= 0 ; (LHS = 0)

EqCompMolBalCondHdr(1,N2).. Fc(10,N2) - Fc(11,N2) + Fc(37,N2) + Fc(38,N2) =E= 0 ; (LHS = 0)

EqCompMolBalCondHdr(1,CH4).. Fc(10,CH4) - Fc(11,CH4) + Fc(37,CH4) + Fc(38,CH4) =E= 0 ; (LHS =

0)

EqCompMolBalCondHdr(1,CO).. Fc(10,CO) - Fc(11,CO) + Fc(37,CO) + Fc(38,CO) =E= 0 ; (LHS = 0)

EqCompMolBalCondHdr(1,CO2).. Fc(10,CO2) - Fc(11,CO2) + Fc(37,CO2) + Fc(38,CO2) =E= 0 ; (LHS =

0)

EqCompMolBalCondHdr(1,H2O).. Fc(10,H2O) - Fc(11,H2O) + Fc(37,H2O) + Fc(38,H2O) =E= 0 ; (LHS =

0)

---- EqPRel1CondHdr =E= Pressure of outlet stream equals the pressure of header

EqPRel1CondHdr(1).. P(11) =E= 1.4 ; (LHS = 1.4)

---- EqCompMolBalDeAertr =E=

EqCompMolBalDeAertr(1,H2).. Fc(9,H2) + Fc(11,H2) + Fc(12,H2) - Fc(13,H2) - Fc(14,H2) - Fc(15,

H2) - Fc(16,H2) + Fc(17,H2) =E= 0 ; (LHS = 0)

EqCompMolBalDeAertr(1,O2).. Fc(9,O2) + Fc(11,O2) + Fc(12,O2) - Fc(13,O2) - Fc(14,O2) - Fc(15,

O2) - Fc(16,O2) + Fc(17,O2) =E= 0 ; (LHS = 0)

EqCompMolBalDeAertr(1,N2).. Fc(9,N2) + Fc(11,N2) + Fc(12,N2) - Fc(13,N2) - Fc(14,N2) - Fc(15,

N2) - Fc(16,N2) + Fc(17,N2) =E= 0 ; (LHS = 0)

EqCompMolBalDeAertr(1,CH4).. Fc(9,CH4) + Fc(11,CH4) + Fc(12,CH4) - Fc(13,CH4) - Fc(14,CH4) -

Fc(15,CH4) - Fc(16,CH4) + Fc(17,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalDeAertr(1,CO).. Fc(9,CO) + Fc(11,CO) + Fc(12,CO) - Fc(13,CO) - Fc(14,CO) - Fc(15,

CO) - Fc(16,CO) + Fc(17,CO) =E= 0 ; (LHS = 0)

EqCompMolBalDeAertr(1,CO2).. Fc(9,CO2) + Fc(11,CO2) + Fc(12,CO2) - Fc(13,CO2) - Fc(14,CO2) -

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Fc(15,CO2) - Fc(16,CO2) + Fc(17,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalDeAertr(1,H2O).. Fc(9,H2O) + Fc(11,H2O) + Fc(12,H2O) - Fc(13,H2O) - Fc(14,H2O) -

Fc(15,H2O) - Fc(16,H2O) + Fc(17,H2O) =E= 0 ; (LHS = 0)

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---- EqEnthBalDeAertr =E=

EqEnthBalDeAertr(1).. - (0.0786582239811999)*F(9) - (0.0775864176832051)*F(11) - (0.070160063

5260063)*F(12) + (0.0775864176800003)*F(13) + (0.0775864176832051)*F(14) + (0.0775864176832051

)*F(15) + (0.0663768970822343)*F(16) - (0.0793565091785469)*F(17)

+ (11138.8529129714)*H(9) + (7538.52621063471)*H(11) + (1946.37952422423)*H(12) + (0)*H(

13) + (0)*H(14) - (21261.6068534334)*H(15) - (106.84224549464)*H(16) + (744.690451097644)*H(17

) =E= 0 ;

(LHS = -9.61942737376376E-6, INFES = 9.61942737376376E-6 ****)

---- EqVentVapDeAertr =E=

EqVentVapDeAertr(1).. - 0.005*Fc(9,H2O) - 0.005*Fc(11,H2O) - 0.005*Fc(12,H2O) + Fc(16,H2O) -

0.005*Fc(17,H2O) =E= 0 ; (LHS = 0)

---- EqPRel1DeAertr =E=

EqPRel1DeAertr(1,16).. P(16) =E= 1.4 ; (LHS = 1.4)

---- EqPRel2DeAertr =E=




---- EqCompMolBalBlrCmbtr =E= Component mol balance

EqCompMolBalBlrCmbtr(MP,H2).. - Fc(23,H2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(MP,O2).. - Fc(23,O2) - 0.5*Dum1BlrCmbtr(MP,H2) + Dum1BlrCmbtr(MP,O2) - 2

*Dum1BlrCmbtr(MP,CH4) - 0.5*Dum1BlrCmbtr(MP,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(MP,N2).. - Fc(23,N2) + Dum1BlrCmbtr(MP,N2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(MP,CH4).. - Fc(23,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(MP,CO).. - Fc(23,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(MP,CO2).. - Fc(23,CO2) + Dum1BlrCmbtr(MP,CH4) + Dum1BlrCmbtr(MP,CO) + Du

m1BlrCmbtr(MP,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(MP,H2O).. - Fc(23,H2O) + Dum1BlrCmbtr(MP,H2) + 2*Dum1BlrCmbtr(MP,CH4) +

Dum1BlrCmbtr(MP,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(HP,H2).. - Fc(21,H2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(HP,O2).. - Fc(21,O2) - 0.5*Dum1BlrCmbtr(HP,H2) + Dum1BlrCmbtr(HP,O2) - 2

*Dum1BlrCmbtr(HP,CH4) - 0.5*Dum1BlrCmbtr(HP,CO) =E= 0 ; (LHS = 0)

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EqCompMolBalBlrCmbtr(HP,N2).. - Fc(21,N2) + Dum1BlrCmbtr(HP,N2) =E= 0 ; (LHS = 0)

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EqCompMolBalBlrCmbtr =E= Component mol balance

EqCompMolBalBlrCmbtr(HP,CH4).. - Fc(21,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(HP,CO).. - Fc(21,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(HP,CO2).. - Fc(21,CO2) + Dum1BlrCmbtr(HP,CH4) + Dum1BlrCmbtr(HP,CO) + Du

m1BlrCmbtr(HP,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(HP,H2O).. - Fc(21,H2O) + Dum1BlrCmbtr(HP,H2) + 2*Dum1BlrCmbtr(HP,CH4) +

Dum1BlrCmbtr(HP,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,H2).. - Fc(42,H2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,O2).. - Fc(42,O2) - 0.5*Dum1BlrCmbtr(GT,H2) + Dum1BlrCmbtr(GT,O2) - 2

*Dum1BlrCmbtr(GT,CH4) - 0.5*Dum1BlrCmbtr(GT,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,N2).. - Fc(42,N2) + Dum1BlrCmbtr(GT,N2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,CH4).. - Fc(42,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,CO).. - Fc(42,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,CO2).. - Fc(42,CO2) + Dum1BlrCmbtr(GT,CH4) + Dum1BlrCmbtr(GT,CO) + Du

m1BlrCmbtr(GT,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GT,H2O).. - Fc(42,H2O) + Dum1BlrCmbtr(GT,H2) + 2*Dum1BlrCmbtr(GT,CH4) +

Dum1BlrCmbtr(GT,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,H2).. - Fc(45,H2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,O2).. - Fc(45,O2) - 0.5*Dum1BlrCmbtr(GTSF,H2) + Dum1BlrCmbtr(GTSF,O

2) - 2*Dum1BlrCmbtr(GTSF,CH4) - 0.5*Dum1BlrCmbtr(GTSF,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,N2).. - Fc(45,N2) + Dum1BlrCmbtr(GTSF,N2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,CH4).. - Fc(45,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,CO).. - Fc(45,CO) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,CO2).. - Fc(45,CO2) + Dum1BlrCmbtr(GTSF,CH4) + Dum1BlrCmbtr(GTSF,CO

) + Dum1BlrCmbtr(GTSF,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalBlrCmbtr(GTSF,H2O).. - Fc(45,H2O) + Dum1BlrCmbtr(GTSF,H2) + 2*Dum1BlrCmbtr(GTSF,C

H4) + Dum1BlrCmbtr(GTSF,H2O) =E= 0 ; (LHS = 0)

---- EqDum1BlrCmbtr =E= Dummy (calculates inlet flow for particular component)

EqDum1BlrCmbtr(MP,H2).. - Fc(29,H2) - Fc(30,H2) + Dum1BlrCmbtr(MP,H2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(MP,O2).. - Fc(29,O2) - Fc(30,O2) + Dum1BlrCmbtr(MP,O2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(MP,N2).. - Fc(29,N2) - Fc(30,N2) + Dum1BlrCmbtr(MP,N2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(MP,CH4).. - Fc(29,CH4) - Fc(30,CH4) + Dum1BlrCmbtr(MP,CH4) =E= 0 ; (LHS = 0)

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EqDum1BlrCmbtr(MP,CO).. - Fc(29,CO) - Fc(30,CO) + Dum1BlrCmbtr(MP,CO) =E= 0 ; (LHS = 0)

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EqDum1BlrCmbtr =E= Dummy (calculates inlet flow for particular component)

EqDum1BlrCmbtr(MP,CO2).. - Fc(29,CO2) - Fc(30,CO2) + Dum1BlrCmbtr(MP,CO2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(MP,H2O).. - Fc(29,H2O) - Fc(30,H2O) + Dum1BlrCmbtr(MP,H2O) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,H2).. - Fc(27,H2) - Fc(28,H2) + Dum1BlrCmbtr(HP,H2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,O2).. - Fc(27,O2) - Fc(28,O2) + Dum1BlrCmbtr(HP,O2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,N2).. - Fc(27,N2) - Fc(28,N2) + Dum1BlrCmbtr(HP,N2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,CH4).. - Fc(27,CH4) - Fc(28,CH4) + Dum1BlrCmbtr(HP,CH4) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,CO).. - Fc(27,CO) - Fc(28,CO) + Dum1BlrCmbtr(HP,CO) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,CO2).. - Fc(27,CO2) - Fc(28,CO2) + Dum1BlrCmbtr(HP,CO2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(HP,H2O).. - Fc(27,H2O) - Fc(28,H2O) + Dum1BlrCmbtr(HP,H2O) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,H2).. - Fc(40,H2) - Fc(41,H2) + Dum1BlrCmbtr(GT,H2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,O2).. - Fc(40,O2) - Fc(41,O2) + Dum1BlrCmbtr(GT,O2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,N2).. - Fc(40,N2) - Fc(41,N2) + Dum1BlrCmbtr(GT,N2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,CH4).. - Fc(40,CH4) - Fc(41,CH4) + Dum1BlrCmbtr(GT,CH4) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,CO).. - Fc(40,CO) - Fc(41,CO) + Dum1BlrCmbtr(GT,CO) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,CO2).. - Fc(40,CO2) - Fc(41,CO2) + Dum1BlrCmbtr(GT,CO2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GT,H2O).. - Fc(40,H2O) - Fc(41,H2O) + Dum1BlrCmbtr(GT,H2O) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GTSF,H2).. - Fc(43,H2) - Fc(44,H2) + Dum1BlrCmbtr(GTSF,H2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GTSF,O2).. - Fc(43,O2) - Fc(44,O2) + Dum1BlrCmbtr(GTSF,O2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GTSF,N2).. - Fc(43,N2) - Fc(44,N2) + Dum1BlrCmbtr(GTSF,N2) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GTSF,CH4).. - Fc(43,CH4) - Fc(44,CH4) + Dum1BlrCmbtr(GTSF,CH4) =E= 0 ; (LHS =

0)

EqDum1BlrCmbtr(GTSF,CO).. - Fc(43,CO) - Fc(44,CO) + Dum1BlrCmbtr(GTSF,CO) =E= 0 ; (LHS = 0)

EqDum1BlrCmbtr(GTSF,CO2).. - Fc(43,CO2) - Fc(44,CO2) + Dum1BlrCmbtr(GTSF,CO2) =E= 0 ; (LHS =

0)

EqDum1BlrCmbtr(GTSF,H2O).. - Fc(43,H2O) - Fc(44,H2O) + Dum1BlrCmbtr(GTSF,H2O) =E= 0 ; (LHS =

0)

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---- EqEgyBalBlrCmbtr =E= Energy balance for combustor

EqEgyBalBlrCmbtr(MP).. - (0.00159574278372965)*Fc(23,H2) - (0.00165505241110473)*Fc(23,O2) -

(0.00160730410628413)*Fc(23,N2) + (0.018462681064419)*Fc(23,CH4) + (0.0290897239253213)*Fc(23,

CO) + (0.107072466036317)*Fc(23,CO2)

+ (0.0652886755962375)*Fc(23,H2O) + (0)*Fc(29,H2) + (0)*Fc(29,O2) + (0)*Fc(29,N2) - (0.0

207)*Fc(29,CH4) - (0.0307027777777778)*Fc(29,CO) - (0.109308333333333)*Fc(29,CO2) - (0.0671705

555555556)*Fc(29,H2O) + (0)*Fc(30,H2) + (0)*Fc(30,O2)

+ (0)*Fc(30,N2) - (0.0207)*Fc(30,CH4) - (0.0307027777777778)*Fc(30,CO) - (0.109308333333

333)*Fc(30,CO2) - (0.0671705555555556)*Fc(30,H2O) + (0)*Hc(23,H2) + (0)*Hc(23,O2) + (0)*Hc(23,

N2) + (0)*Hc(23,CH4) + (0)*Hc(23,CO) + (0)*Hc(23,CO2)

+ (0)*Hc(23,H2O) + (0)*Hc(29,H2) + (0)*Hc(29,O2) + (0)*Hc(29,N2) + (0)*Hc(29,CH4) + (0)*

Hc(29,CO) + (0)*Hc(29,CO2) + (0)*Hc(29,H2O) + (0)*Hc(30,H2) + (0)*Hc(30,O2) + (0)*Hc(30,N2) +

(0)*Hc(30,CH4) + (0)*Hc(30,CO) + (0)*Hc(30,CO2) + (0)*Hc(30,H2O)

=E= 0 ; (LHS = 0)

EqEgyBalBlrCmbtr(HP).. - (0.00196192420252093)*Fc(21,H2) - (0.00204533880433055)*Fc(21,O2) -

(0.0019792817775278)*Fc(21,N2) + (0.0178721026759565)*Fc(21,CH4) + (0.0287148794735374)*Fc(21,

CO) + (0.106513160723588)*Fc(21,CO2)

+ (0.0648464734303417)*Fc(21,H2O) + (0)*Fc(27,H2) + (0)*Fc(27,O2) + (0)*Fc(27,N2) - (0.0

207)*Fc(27,CH4) - (0.0307027777777778)*Fc(27,CO) - (0.109308333333333)*Fc(27,CO2) - (0.0671705

555555556)*Fc(27,H2O) + (0)*Fc(28,H2) + (0)*Fc(28,O2)

+ (0)*Fc(28,N2) - (0.0207)*Fc(28,CH4) - (0.0307027777777778)*Fc(28,CO) - (0.109308333333

333)*Fc(28,CO2) - (0.0671705555555556)*Fc(28,H2O) + (0)*Hc(21,H2) + (0)*Hc(21,O2) + (0)*Hc(21,

N2) + (0)*Hc(21,CH4) + (0)*Hc(21,CO) + (0)*Hc(21,CO2)

+ (0)*Hc(21,H2O) + (0)*Hc(27,H2) + (0)*Hc(27,O2) + (0)*Hc(27,N2) + (0)*Hc(27,CH4) + (0)*

Hc(27,CO) + (0)*Hc(27,CO2) + (0)*Hc(27,H2O) + (0)*Hc(28,H2) + (0)*Hc(28,O2) + (0)*Hc(28,N2) +

(0)*Hc(28,CH4) + (0)*Hc(28,CO) + (0)*Hc(28,CO2) + (0)*Hc(28,H2O)

=E= 0 ; (LHS = 0)

EqEgyBalBlrCmbtr(GT).. (0.00264965602091713)*Fc(40,H2) + (0.00279122781038525)*Fc(40,O2) + (0

.0026842386842132)*Fc(40,N2) - (0.016675949084017)*Fc(40,CH4) - (0.0280029454734525)*Fc(40,CO)

- (0.105421752109749)*Fc(40,CO2) - (0.0640010568196236)*Fc(40,H2O)

+ (0)*Fc(41,H2) + (0)*Fc(41,O2) + (0)*Fc(41,N2) - (0.0207)*Fc(41,CH4) - (0.0307027777777

778)*Fc(41,CO) - (0.109308333333333)*Fc(41,CO2) - (0.0671705555555556)*Fc(41,H2O) - (0.0100794

789383741)*Fc(42,H2) - (0.0112775227252278)*Fc(42,O2)

- (0.0106703509663167)*Fc(42,N2) - (0.00132189024000543)*Fc(42,CH4) + (0.019909424612068

6)*Fc(42,CO) + (0.0921940581391073)*Fc(42,CO2) + (0.0537956073668386)*Fc(42,H2O) + (0)*Hc(40,H

2) + (18171.4005610171)*Hc(40,O2) + (68359.0783009692)*Hc(40,N2)

+ (0)*Hc(40,CH4) + (0)*Hc(40,CO) + (0)*Hc(40,CO2) + (0)*Hc(40,H2O) + (5338.12355237439)*

Hc(41,H2) + (0)*Hc(41,O2) + (0)*Hc(41,N2) + (970.567918613525)*Hc(41,CH4) + (2911.70375584058)

*Hc(41,CO) + (485.283959306763)*Hc(41,CO2) + (0)*Hc(41,H2O)

+ (0)*Hc(42,H2) - (12105.3510696826)*Hc(42,O2) - (68359.0783009692)*Hc(42,N2) + (0)*Hc(4

2,CH4) + (0)*Hc(42,CO) - (4367.55563376086)*Hc(42,CO2) - (7279.25938960144)*Hc(42,H2O) =E= 0 ;

(LHS = 0)

model.lst Wed May 30 15:17:17 2018 143

EqEgyBalBlrCmbtr(GTSF).. (0.00376527481036826)*Fc(43,H2) + (0.00403508431008718)*Fc(43,O2) +

(0.00384782458318875)*Fc(43,N2) - (0.0144963214618929)*Fc(43,CH4) - (0.0268242574641663)*Fc(43

,CO) - (0.103554934344382)*Fc(43,CO2)

- (0.0625847155763706)*Fc(43,H2O) + (0)*Fc(44,H2) + (0)*Fc(44,O2) + (0)*Fc(44,N2) - (0.0

207)*Fc(44,CH4) - (0.0307027777777778)*Fc(44,CO) - (0.109308333333333)*Fc(44,CO2) - (0.0671705

555555556)*Fc(44,H2O) - (0.00376527481036826)*Fc(45,H2)

- (0.00403508431008718)*Fc(45,O2) - (0.00384782458318875)*Fc(45,N2) + (0.014496321461892

9)*Fc(45,CH4) + (0.0268242574641663)*Fc(45,CO) + (0.103554934344382)*Fc(45,CO2) + (0.062584715

5763706)*Fc(45,H2O) + (0)*Hc(43,H2) + (12105.3510696826)*Hc(43,O2)

+ (68359.0783009692)*Hc(43,N2) + (0)*Hc(43,CH4) + (0)*Hc(43,CO) + (4367.55563376086)*Hc(

43,CO2) + (7279.25938960144)*Hc(43,H2O) + (0)*Hc(44,H2) + (0)*Hc(44,O2) + (0)*Hc(44,N2) + (0)*

Hc(44,CH4) + (0)*Hc(44,CO) + (0)*Hc(44,CO2) + (0)*Hc(44,H2O)

+ (0)*Hc(45,H2) - (12105.3510696826)*Hc(45,O2) - (68359.0783009692)*Hc(45,N2) + (0)*Hc(4

5,CH4) + (0)*Hc(45,CO) - (4367.55563376086)*Hc(45,CO2) - (7279.25938960144)*Hc(45,H2O) =E= 0 ;

(LHS = 0)

---- EqOutPBlrCmbtr1 =E= Equality of pressure

EqOutPBlrCmbtr1(MP,29).. P(23) - P(29) =E= 0 ; (LHS = 0)

EqOutPBlrCmbtr1(MP,30).. P(23) - P(30) =E= 0 ; (LHS = 0)

EqOutPBlrCmbtr1(HP,27).. P(21) - P(27) =E= 0 ; (LHS = 0)

EqOutPBlrCmbtr1(HP,28).. P(21) - P(28) =E= 0 ; (LHS = 0)

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EqOutPBlrCmbtr1 =E= Equality of pressure

EqOutPBlrCmbtr1(GT,40).. - P(40) + P(42) =E= 0 ; (LHS = 0)

EqOutPBlrCmbtr1(GT,41).. - P(41) + P(42) =E= 0 ; (LHS = 0)

EqOutPBlrCmbtr1(GTSF,43).. - P(43) + P(45) =E= 0 ; (LHS = 0)

EqOutPBlrCmbtr1(GTSF,44).. - P(44) + P(45) =E= 0 ; (LHS = 0)

---- EqExcessO2BlrCmbtr =G= constraint for excess O2

EqExcessO2BlrCmbtr(MP).. 0.575*Dum1BlrCmbtr(MP,H2) + Dum1BlrCmbtr(MP,O2) + 2.3*Dum1BlrCmbtr(M

P,CH4) + 0.575*Dum1BlrCmbtr(MP,CO) =G= 0 ; (LHS = 0)

EqExcessO2BlrCmbtr(HP).. 0.575*Dum1BlrCmbtr(HP,H2) + Dum1BlrCmbtr(HP,O2) + 2.3*Dum1BlrCmbtr(H

P,CH4) + 0.575*Dum1BlrCmbtr(HP,CO) =G= 0 ; (LHS = 0)

EqExcessO2BlrCmbtr(GT).. 0.575*Dum1BlrCmbtr(GT,H2) + Dum1BlrCmbtr(GT,O2) + 2.3*Dum1BlrCmbtr(G

T,CH4) + 0.575*Dum1BlrCmbtr(GT,CO) =G= 0 ; (LHS = 25147.3574760518)

EqExcessO2BlrCmbtr(GTSF).. 0.575*Dum1BlrCmbtr(GTSF,H2) + Dum1BlrCmbtr(GTSF,O2) + 2.3*Dum1BlrC

mbtr(GTSF,CH4) + 0.575*Dum1BlrCmbtr(GTSF,CO) =G= 0 ; (LHS = 12105.3510696826)

---- EqTCnstrtBlrCmbtr =L= Constraint for maximum allowable temperature

EqTCnstrtBlrCmbtr(MP).. T(23) =L= 1500 ; (LHS = 495.588337116896)

EqTCnstrtBlrCmbtr(HP).. T(21) =L= 1500 ; (LHS = 540.580060386281)

EqTCnstrtBlrCmbtr(GT).. T(42) =L= 1500 ; (LHS = 1500)

EqTCnstrtBlrCmbtr(GTSF).. T(45) =L= 1500 ; (LHS = 761.291470669467)

---- Eq1AirStr =E=

Eq1AirStr(27).. - 3.76190476190476*Fc(27,O2) + Fc(27,N2) =E= 0 ; (LHS = 0)

Eq1AirStr(29).. - 3.76190476190476*Fc(29,O2) + Fc(29,N2) =E= 0 ; (LHS = 0)

Eq1AirStr(39).. - 3.76190476190476*Fc(39,O2) + Fc(39,N2) =E= 0 ; (LHS = 1.45519152283669E-11)

---- Eq2AirStr =E=

Eq2AirStr(27).. P(27) =E= 1.01325 ; (LHS = 1.01325)

Eq2AirStr(29).. P(29) =E= 1.01325 ; (LHS = 1.01325)

Eq2AirStr(39).. P(39) =E= 1.01325 ; (LHS = 1.01325)

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---- Eq3AirStr =E=

Eq3AirStr(27).. T(27) =E= 298.15 ; (LHS = 298.15)

Eq3AirStr(29).. T(29) =E= 298.15 ; (LHS = 298.15)

Eq3AirStr(39).. T(39) =E= 298.15 ; (LHS = 298.15)

---- Eq1SyngasStr =E=

Eq1SyngasStr(28).. Fc(28,H2) - 11*Fc(28,CO2) =E= 0 ; (LHS = 0)




---- Eq1aSyngasStr =E=

Eq1aSyngasStr(28).. Fc(28,CO) - 6*Fc(28,CO2) =E= 0 ; (LHS = 0)


Eq1aSyngasStr(41).. Fc(41,CO) - 6*Fc(41,CO2) =E= 0 ; (LHS = -4.54747350886464E-13)


---- Eq1bSyngasStr =E=

Eq1bSyngasStr(28).. Fc(28,CH4) - 2*Fc(28,CO2) =E= 0 ; (LHS = 0)




---- Eq2SyngasStr =E=

Eq2SyngasStr(28).. T(28) =E= 298.15 ; (LHS = 298.15)



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Eq2SyngasStr =E=


---- EqWorkFan =E=

EqWorkFan.. - 8.15064643057898E-5*F(27) - 8.15064643057898E-5*F(29) + WorkFan =E= 0 ; (LHS =

0)

---- EqTSat2 =E=

EqTSat2(MP).. POpr(MP) - (0.395838725890814)*TSatOpr(MP) =E= 0 ; (LHS = -7.24753590475302E-13

)

EqTSat2(HP).. POpr(HP) - (0.739754740916448)*TSatOpr(HP) =E= 0 ; (LHS = -1.56319401867222E-13

)

EqTSat2(LP).. POpr(LP) - (0.173532578840636)*TSatOpr(LP) =E= 0 ; (LHS = 0)

---- EqUBTOpr =L=

EqUBTOpr(MP).. TOpr(MP) - TSatOpr(MP) =L= 175 ; (LHS = 82.9611399252991)

EqUBTOpr(HP).. TOpr(HP) - TSatOpr(HP) =L= 225 ; (LHS = 164.687388023361)

EqUBTOpr(LP).. TOpr(LP) - TSatOpr(LP) =L= 125 ; (LHS = 1.70530256582424E-13)

---- EqLBTOpr =G=

EqLBTOpr(MP).. TOpr(MP) - TSatOpr(MP) =G= 0 ; (LHS = 82.9611399252992)

EqLBTOpr(HP).. TOpr(HP) - TSatOpr(HP) =G= 0 ; (LHS = 164.687388023361)

EqLBTOpr(LP).. TOpr(LP) - TSatOpr(LP) =G= 0 ; (LHS = 1.13686837721616E-13)

---- EqCompMolBalPLev =E=

EqCompMolBalPLev(MP,H2).. Fc(2,H2) - Fc(5,H2) + Fc(25,H2) + Fc(32,H2) - Fc(35,H2) + Fc(49,H2)

- Fc(50,H2) - Fc(55,H2) + Fc(59,H2) + Fc(63,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(MP,O2).. Fc(2,O2) - Fc(5,O2) + Fc(25,O2) + Fc(32,O2) - Fc(35,O2) + Fc(49,O2)

- Fc(50,O2) - Fc(55,O2) + Fc(59,O2) + Fc(63,O2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(MP,N2).. Fc(2,N2) - Fc(5,N2) + Fc(25,N2) + Fc(32,N2) - Fc(35,N2) + Fc(49,N2)

- Fc(50,N2) - Fc(55,N2) + Fc(59,N2) + Fc(63,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(MP,CH4).. Fc(2,CH4) - Fc(5,CH4) + Fc(25,CH4) + Fc(32,CH4) - Fc(35,CH4) + Fc(

49,CH4) - Fc(50,CH4) - Fc(55,CH4) + Fc(59,CH4) + Fc(63,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(MP,CO).. Fc(2,CO) - Fc(5,CO) + Fc(25,CO) + Fc(32,CO) - Fc(35,CO) + Fc(49,CO)

- Fc(50,CO) - Fc(55,CO) + Fc(59,CO) + Fc(63,CO) =E= 0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 147

EqCompMolBalPLev(MP,CO2).. Fc(2,CO2) - Fc(5,CO2) + Fc(25,CO2) + Fc(32,CO2) - Fc(35,CO2) + Fc(

49,CO2) - Fc(50,CO2) - Fc(55,CO2) + Fc(59,CO2) + Fc(63,CO2) =E= 0 ; (LHS = 0)

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EqCompMolBalPLev =E=

EqCompMolBalPLev(MP,H2O).. Fc(2,H2O) - Fc(5,H2O) + Fc(25,H2O) + Fc(32,H2O) - Fc(35,H2O) + Fc(

49,H2O) - Fc(50,H2O) - Fc(55,H2O) + Fc(59,H2O) + Fc(63,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,H2).. - Fc(1,H2) + Fc(26,H2) + Fc(31,H2) - Fc(34,H2) + Fc(47,H2) - Fc(48,

H2) - Fc(58,H2) - Fc(62,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,O2).. - Fc(1,O2) + Fc(26,O2) + Fc(31,O2) - Fc(34,O2) + Fc(47,O2) - Fc(48,

O2) - Fc(58,O2) - Fc(62,O2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,N2).. - Fc(1,N2) + Fc(26,N2) + Fc(31,N2) - Fc(34,N2) + Fc(47,N2) - Fc(48,

N2) - Fc(58,N2) - Fc(62,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,CH4).. - Fc(1,CH4) + Fc(26,CH4) + Fc(31,CH4) - Fc(34,CH4) + Fc(47,CH4) -

Fc(48,CH4) - Fc(58,CH4) - Fc(62,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,CO).. - Fc(1,CO) + Fc(26,CO) + Fc(31,CO) - Fc(34,CO) + Fc(47,CO) - Fc(48,

CO) - Fc(58,CO) - Fc(62,CO) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,CO2).. - Fc(1,CO2) + Fc(26,CO2) + Fc(31,CO2) - Fc(34,CO2) + Fc(47,CO2) -

Fc(48,CO2) - Fc(58,CO2) - Fc(62,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(HP,H2O).. - Fc(1,H2O) + Fc(26,H2O) + Fc(31,H2O) - Fc(34,H2O) + Fc(47,H2O) -

Fc(48,H2O) - Fc(58,H2O) - Fc(62,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,H2).. Fc(3,H2) + Fc(6,H2) - Fc(12,H2) + Fc(33,H2) - Fc(36,H2) + Fc(51,H2)

+ Fc(56,H2) + Fc(60,H2) + Fc(64,H2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,O2).. Fc(3,O2) + Fc(6,O2) - Fc(12,O2) + Fc(33,O2) - Fc(36,O2) + Fc(51,O2)

+ Fc(56,O2) + Fc(60,O2) + Fc(64,O2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,N2).. Fc(3,N2) + Fc(6,N2) - Fc(12,N2) + Fc(33,N2) - Fc(36,N2) + Fc(51,N2)

+ Fc(56,N2) + Fc(60,N2) + Fc(64,N2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,CH4).. Fc(3,CH4) + Fc(6,CH4) - Fc(12,CH4) + Fc(33,CH4) - Fc(36,CH4) + Fc(

51,CH4) + Fc(56,CH4) + Fc(60,CH4) + Fc(64,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,CO).. Fc(3,CO) + Fc(6,CO) - Fc(12,CO) + Fc(33,CO) - Fc(36,CO) + Fc(51,CO)

+ Fc(56,CO) + Fc(60,CO) + Fc(64,CO) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,CO2).. Fc(3,CO2) + Fc(6,CO2) - Fc(12,CO2) + Fc(33,CO2) - Fc(36,CO2) + Fc(

51,CO2) + Fc(56,CO2) + Fc(60,CO2) + Fc(64,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalPLev(LP,H2O).. Fc(3,H2O) + Fc(6,H2O) - Fc(12,H2O) + Fc(33,H2O) - Fc(36,H2O) + Fc(

51,H2O) + Fc(56,H2O) + Fc(60,H2O) + Fc(64,H2O) =E= 0 ; (LHS = 0)

---- EqEgyBalPLev =E=

EqEgyBalPLev(MP).. - (0.0645685780167178)*F(2) + (0.0645685780167178)*F(5) - (0.0653861873889

167)*F(25) - (0.0653861873889167)*F(32) + (0.0645685780167178)*F(35) - (0.0653861873889167)*F(

49) + (0.0645685780167178)*F(50) + (0.0645685780167178)*F(55)

- (0.0645685780167178)*F(59) - (0.0649509844655109)*F(63) + (0)*H(2) - (1766.19920651386

)*H(5) + (0)*H(25) + (0)*H(32) - (2115.41644081786)*H(35) + (0)*H(49) + (0)*H(50) + (0)*H(55)

model.lst Wed May 30 15:17:17 2018 149

+ (3881.61564733172)*H(59) + (0)*H(63) =E= 0 ; (LHS = 0)

EqEgyBalPLev(HP).. (0.0632783912521576)*F(1) - (0.0649452630740801)*F(26) - (0.06494526307408

01)*F(31) + (0.0632783912521576)*F(34) - (0.0632783912521576)*F(47) + (0.0632783912521576)*F(4

8) + (0.0632783912521576)*F(58) + (0.0632783912521576)*F(62)

- (3639.78325890297)*H(1) + (0)*H(26) + (0)*H(31) - (598.025038518983)*H(34) + (20623.75

86478304)*H(47) + (0)*H(48) - (16385.9503504084)*H(58) + (0)*H(62) =E= 0 ; (LHS = 4.5474735088

6464E-13)

EqEgyBalPLev(LP).. - (0.0673995157623354)*F(3) - (0.0673995157623354)*F(6) + (0.0701600635260

063)*F(12) - (0.0658449834595872)*F(33) + (0.0658460198151376)*F(36) - (0.0658449834595872)*F(

51) - (0.0656344842591389)*F(56) - (0.0658449834595872)*F(60)

- (0.0656344842591389)*F(64) + (3639.78325890297)*H(3) + (1766.19920651386)*H(6) - (1946

.37952422423)*H(12) + (0)*H(33) - (4825.08473129786)*H(36) + (0)*H(51) + (0)*H(56) + (1365.481

79010526)*H(60) + (0)*H(64) =E= 0 ;

(LHS = 9.61942760113743E-6, INFES = 9.61942760113743E-6 ****)

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---- EqPRel1PLev =E=

EqPRel1PLev(MP,2).. P(2) - POpr(MP) =E= 0 ; (LHS = 0)






EqPRel1PLev(HP,26).. P(26) - POpr(HP) =E= 0 ; (LHS = 0)



EqPRel1PLev(LP,3).. P(3) - POpr(LP) =E= 0 ; (LHS = 0)







---- EqPRel2PLev =E=








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EqPRel2PLev =E=





---- EqTRel1PLev =E=

EqTRel1PLev(MP,5).. T(5) - TOpr(MP) =E= 0 ; (LHS = 0)




EqTRel1PLev(HP,1).. T(1) - TOpr(HP) =E= 0 ; (LHS = 0)





EqTRel1PLev(LP,12).. T(12) - TOpr(LP) =E= 0 ; (LHS = 0)

EqTRel1PLev(LP,36).. T(36) - TOpr(LP) =E= 0 ; (LHS = 0)

---- EqGasMolBalBlr =E=

EqGasMolBalBlr(MP,H2).. Fc(23,H2) - Fc(24,H2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(MP,O2).. Fc(23,O2) - Fc(24,O2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(MP,N2).. Fc(23,N2) - Fc(24,N2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(MP,CH4).. Fc(23,CH4) - Fc(24,CH4) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(MP,CO).. Fc(23,CO) - Fc(24,CO) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(MP,CO2).. Fc(23,CO2) - Fc(24,CO2) =E= 0 ; (LHS = 0)

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EqGasMolBalBlr =E=

EqGasMolBalBlr(MP,H2O).. Fc(23,H2O) - Fc(24,H2O) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,H2).. Fc(21,H2) - Fc(22,H2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,O2).. Fc(21,O2) - Fc(22,O2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,N2).. Fc(21,N2) - Fc(22,N2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,CH4).. Fc(21,CH4) - Fc(22,CH4) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,CO).. Fc(21,CO) - Fc(22,CO) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,CO2).. Fc(21,CO2) - Fc(22,CO2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HP,H2O).. Fc(21,H2O) - Fc(22,H2O) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,H2).. Fc(45,H2) - Fc(46,H2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,O2).. Fc(45,O2) - Fc(46,O2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,N2).. Fc(45,N2) - Fc(46,N2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,CH4).. Fc(45,CH4) - Fc(46,CH4) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,CO).. Fc(45,CO) - Fc(46,CO) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,CO2).. Fc(45,CO2) - Fc(46,CO2) =E= 0 ; (LHS = 0)

EqGasMolBalBlr(HRSG,H2O).. Fc(45,H2O) - Fc(46,H2O) =E= 0 ; (LHS = 0)

---- EqWtrMolBalBlr =E=

EqWtrMolBalBlr(MP,H2).. Fc(18,H2) - Fc(25,H2) - Fc(52,H2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(MP,O2).. Fc(18,O2) - Fc(25,O2) - Fc(52,O2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(MP,N2).. Fc(18,N2) - Fc(25,N2) - Fc(52,N2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(MP,CH4).. Fc(18,CH4) - Fc(25,CH4) - Fc(52,CH4) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(MP,CO).. Fc(18,CO) - Fc(25,CO) - Fc(52,CO) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(MP,CO2).. Fc(18,CO2) - Fc(25,CO2) - Fc(52,CO2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(MP,H2O).. Fc(18,H2O) - Fc(25,H2O) - Fc(52,H2O) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HP,H2).. Fc(19,H2) - Fc(26,H2) - Fc(53,H2) =E= 0 ; (LHS = 0)

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EqWtrMolBalBlr =E=

EqWtrMolBalBlr(HP,O2).. Fc(19,O2) - Fc(26,O2) - Fc(53,O2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HP,N2).. Fc(19,N2) - Fc(26,N2) - Fc(53,N2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HP,CH4).. Fc(19,CH4) - Fc(26,CH4) - Fc(53,CH4) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HP,CO).. Fc(19,CO) - Fc(26,CO) - Fc(53,CO) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HP,CO2).. Fc(19,CO2) - Fc(26,CO2) - Fc(53,CO2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HP,H2O).. Fc(19,H2O) - Fc(26,H2O) - Fc(53,H2O) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,H2).. Fc(20,H2) - Fc(47,H2) - Fc(54,H2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,O2).. Fc(20,O2) - Fc(47,O2) - Fc(54,O2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,N2).. Fc(20,N2) - Fc(47,N2) - Fc(54,N2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,CH4).. Fc(20,CH4) - Fc(47,CH4) - Fc(54,CH4) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,CO).. Fc(20,CO) - Fc(47,CO) - Fc(54,CO) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,CO2).. Fc(20,CO2) - Fc(47,CO2) - Fc(54,CO2) =E= 0 ; (LHS = 0)

EqWtrMolBalBlr(HRSG,H2O).. Fc(20,H2O) - Fc(47,H2O) - Fc(54,H2O) =E= 0 ; (LHS = 3.637978807091

71E-12)

---- EqGasEgyBalBlr =E=

EqGasEgyBalBlr(MP).. (0.00159574278372965)*Fc(23,H2) + (0.00165505241110473)*Fc(23,O2) + (0.0

0160730410628413)*Fc(23,N2) - (0.018462681064419)*Fc(23,CH4) - (0.0290897239253213)*Fc(23,CO)

- (0.107072466036317)*Fc(23,CO2) - (0.0652886755962375)*Fc(23,H2O)

- (0.000759228542169931)*Fc(24,H2) - (0.000779833439508448)*Fc(24,O2) - (0.0007637043003

20578)*Fc(24,N2) + (0.0196978342919161)*Fc(24,CH4) + (0.0299376169786605)*Fc(24,CO) + (0.10828

7243349511)*Fc(24,CO2) + (0.0662818959725452)*Fc(24,H2O)

+ (0)*Hc(23,H2) + (0)*Hc(23,O2) + (0)*Hc(23,N2) + (0)*Hc(23,CH4) + (0)*Hc(23,CO) + (0)*H

c(23,CO2) + (0)*Hc(23,H2O) + (0)*Hc(24,H2) + (0)*Hc(24,O2) + (0)*Hc(24,N2) + (0)*Hc(24,CH4) +

(0)*Hc(24,CO) + (0)*Hc(24,CO2) + (0)*Hc(24,H2O) - QBlr(MP) =E= 0 ;

(LHS = 0)

EqGasEgyBalBlr(HP).. (0.00196192420252093)*Fc(21,H2) + (0.00204533880433055)*Fc(21,O2) + (0.0

019792817775278)*Fc(21,N2) - (0.0178721026759565)*Fc(21,CH4) - (0.0287148794735374)*Fc(21,CO)

- (0.106513160723588)*Fc(21,CO2) - (0.0648464734303417)*Fc(21,H2O)

- (0.000763461498861121)*Fc(22,H2) - (0.000784212267803189)*Fc(22,O2) - (0.0007679600090

45014)*Fc(22,N2) + (0.0196919561496707)*Fc(22,CH4) + (0.0299333471445078)*Fc(22,CO) + (0.10828

1327671871)*Fc(22,CO2) + (0.0662769175797148)*Fc(22,H2O)

+ (0)*Hc(21,H2) + (0)*Hc(21,O2) + (0)*Hc(21,N2) + (0)*Hc(21,CH4) + (0)*Hc(21,CO) + (0)*H

c(21,CO2) + (0)*Hc(21,H2O) + (0)*Hc(22,H2) + (0)*Hc(22,O2) + (0)*Hc(22,N2) + (0)*Hc(22,CH4) +

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(0)*Hc(22,CO) + (0)*Hc(22,CO2) + (0)*Hc(22,H2O) - QBlr(HP) =E= 0 ;

(LHS = 0)

EqGasEgyBalBlr(HRSG).. (0.00376527481036826)*Fc(45,H2) + (0.00403508431008718)*Fc(45,O2) + (0

.00384782458318875)*Fc(45,N2) - (0.0144963214618929)*Fc(45,CH4) - (0.0268242574641663)*Fc(45,C

O) - (0.103554934344382)*Fc(45,CO2)

- (0.0625847155763706)*Fc(45,H2O) - (0.000759228541042472)*Fc(46,H2) - (0.00077983343834

2193)*Fc(46,O2) - (0.000763704299187067)*Fc(46,N2) + (0.0196978342934813)*Fc(46,CH4) + (0.0299

376169797978)*Fc(46,CO) + (0.108287243351087)*Fc(46,CO2)

+ (0.0662818959738712)*Fc(46,H2O) + (0)*Hc(45,H2) + (12105.3510696826)*Hc(45,O2) + (6835

9.0783009692)*Hc(45,N2) + (0)*Hc(45,CH4) + (0)*Hc(45,CO) + (4367.55563376086)*Hc(45,CO2) + (72

79.25938960144)*Hc(45,H2O) + (0)*Hc(46,H2)

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EqGasEgyBalBlr =E=

- (12105.3510696826)*Hc(46,O2) - (68359.0783009692)*Hc(46,N2) + (0)*Hc(46,CH4) + (0)*Hc(

46,CO) - (4367.55563376086)*Hc(46,CO2) - (7279.25938960144)*Hc(46,H2O) - QBlr(HRSG) =E= 0 ; (L

HS = 0)

---- EqWtrEgyBalBlr =E=

EqWtrEgyBalBlr(MP).. - (0.0775864176800003)*F(18) + (0.0653861873889167)*F(25) + (0.074841536

1392019)*F(52) + (0)*H(18) + (0)*H(25) + (0)*H(52) + QBlr(MP) =E= 0 ; (LHS = 0)

EqWtrEgyBalBlr(HP).. - (0.0775864176832051)*F(19) + (0.0649452630740801)*F(26) + (0.073306953

1838935)*F(53) + (0)*H(19) + (0)*H(26) + (0)*H(53) + QBlr(HP) =E= 0 ; (LHS = 0)

EqWtrEgyBalBlr(HRSG).. - (0.0775864176832051)*F(20) + (0.0632783912521576)*F(47) + (0.0733069

531838936)*F(54) + (21261.6068534334)*H(20) - (20623.7586478304)*H(47) - (637.848205603002)*H(

54) + QBlr(HRSG) =E= 0 ; (LHS = -4.54747350886464E-13)

---- EqBlowdown =E=

EqBlowdown(MP).. - 0.03*F(18) + F(52) =E= 0 ; (LHS = 0)

EqBlowdown(HP).. - 0.03*F(19) + F(53) =E= 0 ; (LHS = 0)

EqBlowdown(HRSG).. - 0.03*F(20) + F(54) =E= 0 ; (LHS = 0)

---- EqRel2Blr =G=

EqRel2Blr(MP).. T(23) - T(25) =G= 10 ; (LHS = 10)

EqRel2Blr(HP).. T(21) - T(26) =G= 10 ; (LHS = 10)

EqRel2Blr(HRSG).. T(45) - T(47) =G= 10 ; (LHS = 66.0240222598241)

---- EqRel3Blr =G=

EqRel3Blr(MP).. - T(18) + T(24) =G= 10 ; (LHS = 10)

EqRel3Blr(HP).. - T(19) + T(22) =G= 10 ; (LHS = 10.5234221121883)

EqRel3Blr(HRSG).. - T(20) + T(46) =G= 10 ; (LHS = 10)

---- EqRel4Blr =E=

EqRel4Blr(MP).. P(23) - P(24) =E= 0 ; (LHS = 0)

EqRel4Blr(HP).. P(21) - P(22) =E= 0 ; (LHS = 0)

EqRel4Blr(HRSG).. P(45) - P(46) =E= 0 ; (LHS = 0)

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---- EqRel5Blr =E=

EqRel5Blr(MP).. P(18) - P(25) =E= 0 ; (LHS = 0)

EqRel5Blr(HP).. P(19) - P(26) =E= 0 ; (LHS = 0)

EqRel5Blr(HRSG).. P(20) - P(47) =E= 0 ; (LHS = 0)

---- EqRel6Blr =E=

EqRel6Blr(MP).. - P(25) + P(52) =E= 0 ; (LHS = 0)

EqRel6Blr(HP).. - P(26) + P(53) =E= 0 ; (LHS = 0)

EqRel6Blr(HRSG).. - P(47) + P(54) =E= 0 ; (LHS = 0)

---- EqT1 =L=

EqT1.. T(25) - TOpr(MP) =L= 175 ; (LHS = -82.9611399252992)

---- EqT2 =L=

EqT2.. T(26) - TOpr(HP) =L= 225 ; (LHS = -164.687388023361)

---- EqT3 =L=

EqT3.. T(47) - TOpr(HP) =L= 225 ; (LHS = 4.54747350886464E-13)

---- EqCompMolBalStmDmd =E=

EqCompMolBalStmDmd(MP,H2).. - Fc(10,H2) + Fc(35,H2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(MP,O2).. - Fc(10,O2) + Fc(35,O2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(MP,N2).. - Fc(10,N2) + Fc(35,N2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(MP,CH4).. - Fc(10,CH4) + Fc(35,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(MP,CO).. - Fc(10,CO) + Fc(35,CO) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(MP,CO2).. - Fc(10,CO2) + Fc(35,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(MP,H2O).. - Fc(10,H2O) + Fc(35,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(HP,H2).. Fc(34,H2) - Fc(37,H2) =E= 0 ; (LHS = 0)

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EqCompMolBalStmDmd =E=

EqCompMolBalStmDmd(HP,O2).. Fc(34,O2) - Fc(37,O2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(HP,N2).. Fc(34,N2) - Fc(37,N2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(HP,CH4).. Fc(34,CH4) - Fc(37,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(HP,CO).. Fc(34,CO) - Fc(37,CO) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(HP,CO2).. Fc(34,CO2) - Fc(37,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(HP,H2O).. Fc(34,H2O) - Fc(37,H2O) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,H2).. Fc(36,H2) - Fc(38,H2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,O2).. Fc(36,O2) - Fc(38,O2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,N2).. Fc(36,N2) - Fc(38,N2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,CH4).. Fc(36,CH4) - Fc(38,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,CO).. Fc(36,CO) - Fc(38,CO) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,CO2).. Fc(36,CO2) - Fc(38,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalStmDmd(LP,H2O).. Fc(36,H2O) - Fc(38,H2O) =E= 0 ; (LHS = 0)

---- EqEgyBalStmDmd =E=

EqEgyBalStmDmd(MP).. (0.0653871329237918)*F(10) - (0.0645685780167178)*F(35) - (0.58755691643

7161)*LatHtVapP2(10,H2O) - (2115.41644081786)*H(10) + (2115.41644081786)*H(35) - WasteH(MP) =E

= 0 ; (LHS = 0)

EqEgyBalStmDmd(HP).. - (0.0632783912521576)*F(34) + (0.0649460992430911)*F(37) - (0.166101454

448648)*LatHtVapP2(37,H2O) + (598.025038518983)*H(34) - (598.025038518983)*H(37) - WasteH(HP)

=E= 0 ; (LHS = 0)

EqEgyBalStmDmd(LP).. - (0.0658460198151376)*F(36) + (0.0658460198151376)*F(38) - (1.340167284

11798)*LatHtVapP2(38,H2O) + (4825.08473129786)*H(36) - (4825.08473129786)*H(38) - WasteH(LP) =

E= 0 ; (LHS = 0)

---- EqPRel1StmDmd =E=

EqPRel1StmDmd(MP).. - P(10) + P(35) =E= 0 ; (LHS = 0)

EqPRel1StmDmd(HP).. P(34) - P(37) =E= 0 ; (LHS = 0)

EqPRel1StmDmd(LP).. P(36) - P(38) =E= 0 ; (LHS = 0)

---- EqHtReqStmDmd =G=

EqHtReqStmDmd(MP).. (0.0094544032154102)*F(10) + (0.587556916437161)*LatHtVapP2(10,H2O) =G= 2

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0 ; (LHS = 20)

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EqHtReqStmDmd =G=

EqHtReqStmDmd(HP).. (0.00836085394080249)*F(37) + (0.166101454448648)*LatHtVapP2(37,H2O) =G=

5 ; (LHS = 5)

EqHtReqStmDmd(LP).. (0.0103625123255713)*F(38) + (1.34016728411798)*LatHtVapP2(38,H2O) =G= 8

; (LHS = 50)

---- EqPen1StmDmd =E=

EqPen1StmDmd(MP).. WasteH(MP) - 0.08368*MassFCW1(MP) =E= 0 ; (LHS = 0)

EqPen1StmDmd(HP).. WasteH(HP) - 0.08368*MassFCW1(HP) =E= 0 ; (LHS = 0)

EqPen1StmDmd(LP).. WasteH(LP) - 0.08368*MassFCW1(LP) =E= 0 ; (LHS = 0)

---- EqCompMolBalGTCmpr =E= Component mol balance

EqCompMolBalGTCmpr(1,H2).. Fc(39,H2) - Fc(40,H2) =E= 0 ; (LHS = 0)

EqCompMolBalGTCmpr(1,O2).. Fc(39,O2) - Fc(40,O2) =E= 0 ; (LHS = 0)

EqCompMolBalGTCmpr(1,N2).. Fc(39,N2) - Fc(40,N2) =E= 0 ; (LHS = 0)

EqCompMolBalGTCmpr(1,CH4).. Fc(39,CH4) - Fc(40,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalGTCmpr(1,CO).. Fc(39,CO) - Fc(40,CO) =E= 0 ; (LHS = 0)

EqCompMolBalGTCmpr(1,CO2).. Fc(39,CO2) - Fc(40,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalGTCmpr(1,H2O).. Fc(39,H2O) - Fc(40,H2O) =E= 0 ; (LHS = 0)

---- EqOutPGTCmpr =E= Equate outlet P of compressor to that of outlet stream

EqOutPGTCmpr(1).. P(40) - OutPGTCmpr(1) =E= 0 ; (LHS = 0)

---- EqOutTGTCmpr =E= Equate outlet T of compressor to that of outlet stream

EqOutTGTCmpr(1).. T(40) - OutTGTCmpr(1) =E= 0 ; (LHS = 0)

---- EqInPGTCmpr =E= Equate inlet P of compressor to that of inlet stream

EqInPGTCmpr(1).. P(39) - InPGTCmpr(1) =E= 0 ; (LHS = 0)

---- EqInTGTCmpr =E= Equate inlet T of compressor to that of inlet stream

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EqInTGTCmpr =E= Equate inlet T of compressor to that of inlet stream

EqInTGTCmpr(1).. T(39) - InTGTCmpr(1) =E= 0 ; (LHS = 0)

---- EqPTRelGTCmpr =E= P-T relationship (adiabatic)

EqPTRelGTCmpr(1).. (153.02910786758)*InPGTCmpr(1) - (7.75283717734126)*OutPGTCmpr(1) - (2.096

01094544923)*InTGTCmpr(1) + OutTGTCmpr(1) =E= 0 ; (LHS = 0)

---- EqWorkGTCmpr =E= Calculation of work of compression (ideal) (MW)

EqWorkGTCmpr(1).. (0)*Fc(39,H2) + (0)*Fc(39,O2) + (0)*Fc(39,N2) - (0.0207)*Fc(39,CH4) - (0.03

07027777777778)*Fc(39,CO) - (0.109308333333333)*Fc(39,CO2) - (0.0671705555555556)*Fc(39,H2O) -

(0.00264965602091713)*Fc(40,H2) - (0.00279122781038525)*Fc(40,O2)

- (0.0026842386842132)*Fc(40,N2) + (0.016675949084017)*Fc(40,CH4) + (0.0280029454734525)

*Fc(40,CO) + (0.105421752109749)*Fc(40,CO2) + (0.0640010568196236)*Fc(40,H2O) + (0)*Hc(39,H2)

+ (18171.4005610171)*Hc(39,O2) + (68359.0783009692)*Hc(39,N2)

+ (0)*Hc(39,CH4) + (0)*Hc(39,CO) + (0)*Hc(39,CO2) + (0)*Hc(39,H2O) + (0)*Hc(40,H2) - (18

171.4005610171)*Hc(40,O2) - (68359.0783009692)*Hc(40,N2) + (0)*Hc(40,CH4) + (0)*Hc(40,CO) + (0

)*Hc(40,CO2) + (0)*Hc(40,H2O) + WorkGTCmpr(1) =E= 0 ; (LHS = 0)

---- EqPRelGtCmpr =G= Pout >= Pin

EqPRelGtCmpr(1).. - InPGTCmpr(1) + OutPGTCmpr(1) =G= 0 ; (LHS = 18.98675)

---- EqCompMolBalGTExpdr =E= Component mol balance

EqCompMolBalGTExpdr(1,H2).. Fc(42,H2) - Fc(43,H2) =E= 0 ; (LHS = 0)

EqCompMolBalGTExpdr(1,O2).. Fc(42,O2) - Fc(43,O2) =E= 0 ; (LHS = 0)

EqCompMolBalGTExpdr(1,N2).. Fc(42,N2) - Fc(43,N2) =E= 0 ; (LHS = 0)

EqCompMolBalGTExpdr(1,CH4).. Fc(42,CH4) - Fc(43,CH4) =E= 0 ; (LHS = 0)

EqCompMolBalGTExpdr(1,CO).. Fc(42,CO) - Fc(43,CO) =E= 0 ; (LHS = 0)

EqCompMolBalGTExpdr(1,CO2).. Fc(42,CO2) - Fc(43,CO2) =E= 0 ; (LHS = 0)

EqCompMolBalGTExpdr(1,H2O).. Fc(42,H2O) - Fc(43,H2O) =E= 0 ; (LHS = 0)

---- EqOutPGTExpdr =E= Equate outlet P of compressor to that of outlet stream

EqOutPGTExpdr(1).. P(43) - OutPGTExpdr(1) =E= 0 ; (LHS = 0)

---- EqOutTGTExpdr =E= Equate outlet T of compressor to that of outlet stream

EqOutTGTExpdr(1).. T(43) - OutTGTExpdr(1) =E= 0 ; (LHS = 0)

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---- EqInPGTExpdr =E= Equate inlet P of compressor to that of inlet stream

EqInPGTExpdr(1).. P(42) - InPGTExpdr(1) =E= 0 ; (LHS = 0)

---- EqInTGTExpdr =E= Equate inlet T of compressor to that of inlet stream

EqInTGTExpdr(1).. T(42) - InTGTExpdr(1) =E= 0 ; (LHS = 0)

---- EqPTRelGTExpdr =E= P-T relationship (adiabatic)

EqPTRelGTExpdr(1).. (9.44459343311745)*InPGTExpdr(1) - (145.301437432576)*OutPGTExpdr(1) - (0

.507527647112978)*InTGTExpdr(1) + OutTGTExpdr(1) =E= 0 ; (LHS = 0)

---- EqWorkGTExpdr =E= Calculation of work of compression (ideal) (MW)

EqWorkGTExpdr(1).. - (0.0100794789383741)*Fc(42,H2) - (0.0112775227252278)*Fc(42,O2) - (0.010

6703509663167)*Fc(42,N2) - (0.00132189024000543)*Fc(42,CH4) + (0.0199094246120686)*Fc(42,CO) +

(0.0921940581391073)*Fc(42,CO2) + (0.0537956073668386)*Fc(42,H2O)

+ (0.00376527481036826)*Fc(43,H2) + (0.00403508431008718)*Fc(43,O2) + (0.003847824583188

75)*Fc(43,N2) - (0.0144963214618929)*Fc(43,CH4) - (0.0268242574641663)*Fc(43,CO) - (0.10355493

4344382)*Fc(43,CO2) - (0.0625847155763706)*Fc(43,H2O)

+ (0)*Hc(42,H2) - (12105.3510696826)*Hc(42,O2) - (68359.0783009692)*Hc(42,N2) + (0)*Hc(4

2,CH4) + (0)*Hc(42,CO) - (4367.55563376086)*Hc(42,CO2) - (7279.25938960144)*Hc(42,H2O) + (0)*H

c(43,H2) + (12105.3510696826)*Hc(43,O2)

+ (68359.0783009692)*Hc(43,N2) + (0)*Hc(43,CH4) + (0)*Hc(43,CO) + (4367.55563376086)*Hc(

43,CO2) + (7279.25938960144)*Hc(43,H2O) + WorkGTExpdr(1) =E= 0 ; (LHS = 0)

---- EqPRelGTExpdr =L= Pout <= Pin

EqPRelGTExpdr(1).. - InPGTExpdr(1) + OutPGTExpdr(1) =L= 0 ; (LHS = -18.7)

---- EqWorkGT =E=

EqWorkGT.. WorkGTCmpr(1) - WorkGTExpdr(1) + WorkGT =E= 0 ; (LHS = 0)

---- EqMolBalVlv =E=

EqMolBalVlv(HPMP,H2).. Fc(48,H2) - Fc(49,H2) =E= 0 ; (LHS = 0)

EqMolBalVlv(HPMP,O2).. Fc(48,O2) - Fc(49,O2) =E= 0 ; (LHS = 0)

EqMolBalVlv(HPMP,N2).. Fc(48,N2) - Fc(49,N2) =E= 0 ; (LHS = 0)

EqMolBalVlv(HPMP,CH4).. Fc(48,CH4) - Fc(49,CH4) =E= 0 ; (LHS = 0)

EqMolBalVlv(HPMP,CO).. Fc(48,CO) - Fc(49,CO) =E= 0 ; (LHS = 0)

model.lst Wed May 30 15:17:17 2018 163

EqMolBalVlv(HPMP,CO2).. Fc(48,CO2) - Fc(49,CO2) =E= 0 ; (LHS = 0)

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EqMolBalVlv =E=

EqMolBalVlv(HPMP,H2O).. Fc(48,H2O) - Fc(49,H2O) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,H2).. Fc(50,H2) - Fc(51,H2) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,O2).. Fc(50,O2) - Fc(51,O2) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,N2).. Fc(50,N2) - Fc(51,N2) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,CH4).. Fc(50,CH4) - Fc(51,CH4) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,CO).. Fc(50,CO) - Fc(51,CO) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,CO2).. Fc(50,CO2) - Fc(51,CO2) =E= 0 ; (LHS = 0)

EqMolBalVlv(MPLP,H2O).. Fc(50,H2O) - Fc(51,H2O) =E= 0 ; (LHS = 0)

---- EqEgyBalVlv =E=

EqEgyBalVlv(HPMP).. - (0.0632783912521576)*F(48) + (0.0653861873889167)*F(49) + (0)*H(48) + (

0)*H(49) =E= 0 ; (LHS = 0)

EqEgyBalVlv(MPLP).. - (0.0645685780167178)*F(50) + (0.0658449834595872)*F(51) + (0)*H(50) + (

0)*H(51) =E= 0 ; (LHS = 0)

---- Eqstpd2 =L=

Eqstpd2.. F(39) - 13*F(41) =L= 0 ; (LHS = -39643.3505577719)

---- Eqstpd3 =L=

Eqstpd3.. F(27) - 13*F(28) =L= 0 ; (LHS = 0)

---- Eqstpd3a =L=

Eqstpd3a.. F(29) - 13*F(30) =L= 0 ; (LHS = 0)

---- Eqstpd4 =L=

Eqstpd4.. WorkPumpVCT + WorkPump(VP) + WorkPump(MP) + WorkPump(HP) + WorkPump(HRSG) + WorkFan

- WorkGT + MDE(1) + MDE(2) - WHPTE(1) - WHPTE(2) - WHPTE(3) =L= -30 ; (LHS = -500)

---- Eqstpd5 =E=

Eqstpd5(1).. - MDE(1) - MDC(1) =E= -10 ; (LHS = -5, INFES = 5 ****)

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Eqstpd5 =E=

Eqstpd5(2).. - MDE(2) - MDC(2) =E= -20 ; (LHS = -15, INFES = 5 ****)

---- Eqstpd6 =E=

Eqstpd6(1).. MDC(1) - WHPTM(1,1) - WHPTM(2,1) - WHPTM(3,1) - WMPTM(1,1) - WMPTM(2,1) =E= 0 ;

(LHS = 0)

Eqstpd6(2).. MDC(2) - WHPTM(1,2) - WHPTM(2,2) - WHPTM(3,2) - WMPTM(1,2) - WMPTM(2,2) =E= 0 ;

(LHS = 0)

---- Eqstpd7 =E=

Eqstpd7(1).. TotWorkHPStmTurb(1) - WHPTE(1) - WHPTM(1,1) - WHPTM(1,2) =E= 0 ; (LHS = 0)



---- Eqstpd8 =E=

Eqstpd8(1).. TotWorkMPStmTurb(1) - WMPTM(1,1) - WMPTM(1,2) =E= 0 ; (LHS = 0)

Eqstpd8(2).. TotWorkMPStmTurb(2) - WMPTM(2,1) - WMPTM(2,2) =E= 0 ; (LHS = 0)

---- Eqstpd9 =L=

Eqstpd9(1).. MDC(1) - 100*YMD(1) =L= 0 ; (LHS = -95)

Eqstpd9(2).. MDC(2) - 100*YMD(2) =L= 0 ; (LHS = -85)

---- Eqstpd10 =L=

Eqstpd10(1).. MDE(1) + 100*YMD(1) =L= 100 ; (LHS = 100)

Eqstpd10(2).. MDE(2) + 100*YMD(2) =L= 100 ; (LHS = 100)

---- Eqstpd11 =L=

Eqstpd11(1).. WHPTE(1) - 800*YWHPTE(1) =L= 0 ; (LHS = 0)

Eqstpd11(2).. WHPTE(2) - 800*YWHPTE(2) =L= 0 ; (LHS = -732.046078696019)

Eqstpd11(3).. WHPTE(3) - 800*YWHPTE(3) =L= 0 ; (LHS = 0)

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---- Eqstpd12 =L=

Eqstpd12(1,1).. WHPTM(1,1) - 100*YWHPTM(1,1) =L= 0 ; (LHS = 0)

Eqstpd12(1,2).. WHPTM(1,2) - 100*YWHPTM(1,2) =L= 0 ; (LHS = -85)





---- Eqstpd13 =L=

Eqstpd13(1,1).. WMPTM(1,1) - 100*YWMPTM(1,1) =L= 0 ; (LHS = -95)

Eqstpd13(1,2).. WMPTM(1,2) - 100*YWMPTM(1,2) =L= 0 ; (LHS = 0)



---- Eqstpd14 =L=

Eqstpd14.. YWHPTE(1) + YWHPTE(2) + YWHPTE(3) =L= 1 ; (LHS = 1)

---- Eqstpd15 =L=

Eqstpd15(1).. YWHPTM(1,1) + YWHPTM(2,1) + YWHPTM(3,1) + YWMPTM(1,1) + YWMPTM(2,1) =L= 1 ; (LH

S = 1)

Eqstpd15(2).. YWHPTM(1,2) + YWHPTM(2,2) + YWHPTM(3,2) + YWMPTM(1,2) + YWMPTM(2,2) =L= 1 ; (LH

S = 1)

---- Eqstpd16 =L=

Eqstpd16(1).. YWHPTE(1) + YWHPTM(1,1) + YWHPTM(1,2) =L= 1 ; (LHS = 1)



---- Eqstpd17 =L=

Eqstpd17(1).. YWMPTM(1,1) + YWMPTM(1,2) =L= 1 ; (LHS = 1)

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Eqstpd17 =L=

Eqstpd17(2).. YWMPTM(2,1) + YWMPTM(2,2) =L= 1 ; (LHS = 0)

---- obj =E= objective function cost in dollar per hr

obj.. - 0.00576*F(17) - 3.231096*Fc(28,H2) - 10.076052*Fc(28,CH4) - 3.234696*Fc(28,CO) - 3.23

1096*Fc(30,H2) - 10.076052*Fc(30,CH4) - 3.234696*Fc(30,CO) - 3.231096*Fc(41,H2) - 10.076052*Fc

(41,CH4) - 3.234696*Fc(41,CO) - 3.231096*Fc(44,H2)

- 10.076052*Fc(44,CH4) - 3.234696*Fc(44,CO) - 0.001*Y(1) - 0.001*Y(5) - 0.001*Y(55) - 0.

001*Y(58) - 0.001*Y(62) - 0.001*YP2(1) - 0.001*YP2(2) - 0.001*YP2(3) - 0.001*YP2(4) - 0.001*YP

2(5) - 0.001*YP2(6) - 0.001*YP2(7) - 0.001*YP2(12) - 0.001*YP2(25)

- 0.001*YP2(26) - 0.001*YP2(31) - 0.001*YP2(32) - 0.001*YP2(33) - 0.001*YP2(34) - 0.001*

YP2(35) - 0.001*YP2(36) - 0.001*YP2(47) - 0.001*YP2(48) - 0.001*YP2(49) - 0.001*YP2(50) - 0.00

1*YP2(51) - 0.001*YP2(55) - 0.001*YP2(56) - 0.001*YP2(57)

- 0.001*YP2(58) - 0.001*YP2(59) - 0.001*YP2(60) - 0.001*YP2(61) - 0.001*YP2(62) - 0.001*

YP2(63) - 0.001*YP2(64) - 0.001*YP2(65) - 0.001*YModeHPStmTurb(1,MPBkPr) - 0.001*YModeHPStmTur

b(1,MPExt) - 0.001*YModeHPStmTurb(1,LPBkPr)

- 0.001*YModeHPStmTurb(1,LPExt) - 0.001*YModeHPStmTurb(1,VPCond) - 0.001*YModeMPStmTurb(

1,LPBkPr) - 0.001*YModeMPStmTurb(1,LPExt) - 0.001*YModeMPStmTurb(1,VPCond) - 0.09684*MassFCW +

Z =E= 0 ; (LHS = 0.213905195647385

, INFES = 0.213905195647385 ****)

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Column Listing SOLVE TEST4a Using MINLP From line 2276

---- F Flowrate of Stream (kmol per hr)

F(1)

(.LO, .L, .UP, .M = 0, 3639.78325890297, 1000000, 0)

1 EqTotMolStr(1)

1 EqLogBnd4HPStmTurb(1,1)

(0.0633) EqEgyBalPLev(HP)

F(2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0267481060951711)

1 EqTotMolStr(2)

1 EqLogBnd1HPStmTurb(1)

(-0.0646) EqEgyBalPLev(MP)

F(3)

(.LO, .L, .UP, .M = 0, 3639.78325890297, 1000000, 0)

1 EqTotMolStr(3)


(-0.0674) EqEgyBalPLev(LP)

F(4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.110633873568393)

1 EqTotMolStr(4)


(0.0686) EqEnthBalVacCondTurb(1)

F(5)

(.LO, .L, .UP, .M = 0, 1766.19920651386, 1000000, 0)

1 EqTotMolStr(5)

1 EqLogBnd3MPStmTurb(1,5)

(0.0646) EqEgyBalPLev(MP)

F(6)

(.LO, .L, .UP, .M = 0, 1766.19920651386, 1000000, 0)

1 EqTotMolStr(6)

1 EqLogBnd1MPStmTurb(1)


F(7)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(7)



F(8)

(.LO, .L, .UP, .M = 0, 11138.8529129714, 1000000, 0)

1 EqTotMolStr(8)

(-0.0787) EqEnthBalVacCondTurb(1)

(-6.000000E-7) EqWorkPump(VP)

F(9)

(.LO, .L, .UP, .M = 0, 11138.8529129714, 1000000, 0)

1 EqTotMolStr(9)

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F Flowrate of Stream (kmol per hr)

(-0.0787) EqEnthBalDeAertr(1)

F(10)

(.LO, .L, .UP, .M = 0, 2115.41644081786, 1000000, 0)

1 EqTotMolStr(10)

(0.0654) EqEgyBalStmDmd(MP)

(0.0095) EqHtReqStmDmd(MP)

F(11)

(.LO, .L, .UP, .M = 0, 7538.52621063471, 1000000, 0)

1 EqTotMolStr(11)


F(12)

(.LO, .L, .UP, .M = 0, 1946.37952422423, 1000000, 0)

1 EqTotMolStr(12)


(0.0702) EqEgyBalPLev(LP)

F(13)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(13)

(-9.300000E-6) EqWorkPump(MP)

(0.0776) EqEnthBalDeAertr(1)

F(14)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(14)

(-2.180000E-5) EqWorkPump(HP)


F(15)

(.LO, .L, .UP, .M = 0, 21261.6068534334, 1000000, 0)

1 EqTotMolStr(15)

(-2.180000E-5) EqWorkPump(HRSG)


F(16)

(.LO, .L, .UP, .M = 0, 106.84224549464, 1000000, 0)

1 EqTotMolStr(16)


F(17)

(.LO, .L, .UP, .M = 0, 744.690451097644, 1000000, 0)

1 EqTotMolStr(17)


-0.0058 obj

F(18)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(18)

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(-0.0776) EqWtrEgyBalBlr(MP)

-0.03 EqBlowdown(MP)

F(19)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(19)

(-0.0776) EqWtrEgyBalBlr(HP)

-0.03 EqBlowdown(HP)

F(20)

(.LO, .L, .UP, .M = 0, 21261.6068534334, 1000000, 0)

1 EqTotMolStr(20)

(-0.0776) EqWtrEgyBalBlr(HRSG)

-0.03 EqBlowdown(HRSG)

F(21)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(21)

F(22)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(22)

F(23)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0621224325901353)

1 EqTotMolStr(23)

F(24)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(24)

F(25)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(25)


(0.0654) EqWtrEgyBalBlr(MP)

F(26)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(26)

(-0.0649) EqEgyBalPLev(HP)

(0.0649) EqWtrEgyBalBlr(HP)

F(27)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(27)

-8.150646E-5 EqWorkFan

1 Eqstpd3

F(28)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

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1 EqTotMolStr(28)

-13 Eqstpd3

F(29)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(29)

-8.150646E-5 EqWorkFan

1 Eqstpd3a

F(30)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(30)

-13 Eqstpd3a

F(31)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(31)


F(32)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(32)


F(33)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(33)


F(34)

(.LO, .L, .UP, .M = 0, 598.025038518983, 1000000, 0)

1 EqTotMolStr(34)


(-0.0633) EqEgyBalStmDmd(HP)

F(35)

(.LO, .L, .UP, .M = 0, 2115.41644081786, 1000000, 0)

1 EqTotMolStr(35)


(-0.0646) EqEgyBalStmDmd(MP)

F(36)

(.LO, .L, .UP, .M = 0, 4825.08473129786, 1000000, 0)

1 EqTotMolStr(36)


(-0.0658) EqEgyBalStmDmd(LP)

F(37)

(.LO, .L, .UP, .M = 0, 598.025038518983, 1000000, 0)

1 EqTotMolStr(37)

(0.0649) EqEgyBalStmDmd(HP)

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(0.0084) EqHtReqStmDmd(HP)

F(38)

(.LO, .L, .UP, .M = 0, 4825.08473129786, 1000000, 0)

1 EqTotMolStr(38)

(0.0658) EqEgyBalStmDmd(LP)

(0.0104) EqHtReqStmDmd(LP)

F(39)

(.LO, .L, .UP, .M = 0, 86530.4788619863, 1000000, 0)

1 EqTotMolStr(39)

1 Eqstpd2

F(40)

(.LO, .L, .UP, .M = 0, 86530.4788619863, 1000000, 0)

1 EqTotMolStr(40)

F(41)

(.LO, .L, .UP, .M = 0, 9705.67918613525, 1000000, 0)

1 EqTotMolStr(41)

-13 Eqstpd2

F(42)

(.LO, .L, .UP, .M = 0, 92111.2443940141, 1000000, 0)

1 EqTotMolStr(42)

F(43)

(.LO, .L, .UP, .M = 0, 92111.2443940141, 1000000, 0)

1 EqTotMolStr(43)

F(44)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(44)

F(45)

(.LO, .L, .UP, .M = 0, 92111.2443940141, 1000000, 0)

1 EqTotMolStr(45)

F(46)

(.LO, .L, .UP, .M = 0, 92111.2443940141, 1000000, 0)

1 EqTotMolStr(46)

F(47)

(.LO, .L, .UP, .M = 0, 20623.7586478304, 1000000, 0)

1 EqTotMolStr(47)


(0.0633) EqWtrEgyBalBlr(HRSG)

F(48)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0847614991523211)

1 EqTotMolStr(48)

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(-0.0633) EqEgyBalVlv(HPMP)

F(49)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(49)


(0.0654) EqEgyBalVlv(HPMP)

F(50)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(50)


(-0.0646) EqEgyBalVlv(MPLP)

F(51)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(51)


(0.0658) EqEgyBalVlv(MPLP)

F(52)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(52)

(0.0748) EqWtrEgyBalBlr(MP)

1 EqBlowdown(MP)

F(53)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(53)

(0.0733) EqWtrEgyBalBlr(HP)

1 EqBlowdown(HP)

F(54)

(.LO, .L, .UP, .M = 0, 637.848205603002, 1000000, 0)

1 EqTotMolStr(54)


1 EqBlowdown(HRSG)

F(55)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0437388368323991)

1 EqTotMolStr(55)

1 EqLogBnd3MPStmTurb(2,55)


F(56)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(56)



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F(57)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0783774806048653)

1 EqTotMolStr(57)



F(58)

(.LO, .L, .UP, .M = 0, 16385.9503504084, 1000000, 0)

1 EqTotMolStr(58)



F(59)

(.LO, .L, .UP, .M = 0, 3881.61564733172, 1000000, 0)

1 EqTotMolStr(59)



F(60)

(.LO, .L, .UP, .M = 0, 1365.48179010526, 1000000, 0)

1 EqTotMolStr(60)



F(61)

(.LO, .L, .UP, .M = 0, 11138.8529129714, 1000000, 0)

1 EqTotMolStr(61)



F(62)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(62)



F(63)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(63)



F(64)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(64)



F(65)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

1 EqTotMolStr(65)

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---- Fc Component flowrate of stream

Fc(1,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,H2)

-1 EqCompMolBalPLev(HP,H2)

Fc(1,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,O2)

-1 EqCompMolBalPLev(HP,O2)

Fc(1,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,N2)

-1 EqCompMolBalPLev(HP,N2)

Fc(1,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,CH4)

-1 EqCompMolBalPLev(HP,CH4)

Fc(1,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,CO)

-1 EqCompMolBalPLev(HP,CO)

Fc(1,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,CO2)

-1 EqCompMolBalPLev(HP,CO2)

Fc(1,H2O)

(.LO, .L, .UP, .M = 0, 3639.78325890297, 1000000, 0)

-1 EqTotMolStr(1)

1 EqCompMolBalHPStmTurb(1,H2O)

(-0.0013) EqMPWorkHPStmTurb(1)

(-0.0028) EqLPWorkHPStmTurb(1)

(-0.0012) EqVPWorkHPStmTurb(1)

-1 EqCompMolBalPLev(HP,H2O)

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Fc Component flowrate of stream

Fc(2,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.301264499467441)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,H2)

1 EqCompMolBalPLev(MP,H2)

Fc(2,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.301264499467441)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,O2)

1 EqCompMolBalPLev(MP,O2)

Fc(2,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.301264499467441)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,N2)

1 EqCompMolBalPLev(MP,N2)

Fc(2,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.301264499467441)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,CH4)

1 EqCompMolBalPLev(MP,CH4)

Fc(2,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.301264499467441)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,CO)

1 EqCompMolBalPLev(MP,CO)

Fc(2,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.301264499467441)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,CO2)

1 EqCompMolBalPLev(MP,CO2)

Fc(2,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(2)

-1 EqCompMolBalHPStmTurb(1,H2O)

(0.0028) EqLPWorkHPStmTurb(1)

(0.0012) EqVPWorkHPStmTurb(1)

1 EqCompMolBalPLev(MP,H2O)

Fc(3,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(3)


1 EqCompMolBalPLev(LP,H2)

Fc(3,O2)

model.lst Wed May 30 15:17:17 2018 177


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(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(3)


1 EqCompMolBalPLev(LP,O2)

Fc(3,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(3)


1 EqCompMolBalPLev(LP,N2)

Fc(3,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(3)


1 EqCompMolBalPLev(LP,CH4)

Fc(3,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(3)


1 EqCompMolBalPLev(LP,CO)

Fc(3,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(3)


1 EqCompMolBalPLev(LP,CO2)

Fc(3,H2O)

(.LO, .L, .UP, .M = 0, 3639.78325890297, 1000000, 0)

-1 EqTotMolStr(3)



1 EqCompMolBalPLev(LP,H2O)

Fc(4,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.228864840095033)

-1 EqTotMolStr(4)


1 EqCompMolBalVacCondTurb(1,H2)

Fc(4,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.228864840095033)

-1 EqTotMolStr(4)


1 EqCompMolBalVacCondTurb(1,O2)

Fc(4,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.228864840095033)

-1 EqTotMolStr(4)

model.lst Wed May 30 15:17:17 2018 178


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1 EqCompMolBalVacCondTurb(1,N2)

Fc(4,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.228864840095033)

-1 EqTotMolStr(4)


1 EqCompMolBalVacCondTurb(1,CH4)

Fc(4,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.228864840095033)

-1 EqTotMolStr(4)


1 EqCompMolBalVacCondTurb(1,CO)

Fc(4,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.228864840095033)

-1 EqTotMolStr(4)


1 EqCompMolBalVacCondTurb(1,CO2)

Fc(4,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(4)


1 EqCompMolBalVacCondTurb(1,H2O)

Fc(5,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,H2)

-1 EqCompMolBalPLev(MP,H2)

Fc(5,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,O2)

-1 EqCompMolBalPLev(MP,O2)

Fc(5,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,N2)

-1 EqCompMolBalPLev(MP,N2)

Fc(5,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,CH4)

-1 EqCompMolBalPLev(MP,CH4)

model.lst Wed May 30 15:17:17 2018 179


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Fc(5,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,CO)

-1 EqCompMolBalPLev(MP,CO)

Fc(5,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,CO2)

-1 EqCompMolBalPLev(MP,CO2)

Fc(5,H2O)

(.LO, .L, .UP, .M = 0, 1766.19920651386, 1000000, 0)

-1 EqTotMolStr(5)

1 EqCompMolBalMPStmTurb(1,H2O)

(-0.0028) EqLPWorkMPStmTurb(1)

(-0.0012) EqVPWorkMPStmTurb(1)

-1 EqCompMolBalPLev(MP,H2O)

Fc(6,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,H2)


Fc(6,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,O2)


Fc(6,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,N2)


Fc(6,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,CH4)


Fc(6,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,CO)


Fc(6,CO2)

model.lst Wed May 30 15:17:17 2018 180


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(.LO, .L, .UP, .M = 0, 0, 0, 0.905183086905409)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,CO2)


Fc(6,H2O)

(.LO, .L, .UP, .M = 0, 1766.19920651386, 1000000, 0)

-1 EqTotMolStr(6)

-1 EqCompMolBalMPStmTurb(1,H2O)

(0.0012) EqVPWorkMPStmTurb(1)


Fc(7,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(7)



Fc(7,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(7)



Fc(7,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(7)



Fc(7,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(7)



Fc(7,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(7)



Fc(7,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(7)



Fc(7,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.122116317440297)

-1 EqTotMolStr(7)

model.lst Wed May 30 15:17:17 2018 181


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Fc(8,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.135577977532185)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,H2)

1 EqCompMolBalPump(VP,H2)

Fc(8,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.135577977532185)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,O2)

1 EqCompMolBalPump(VP,O2)

Fc(8,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.135577977532185)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,N2)

1 EqCompMolBalPump(VP,N2)

Fc(8,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.135577977532185)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,CH4)

1 EqCompMolBalPump(VP,CH4)

Fc(8,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.135577977532185)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,CO)

1 EqCompMolBalPump(VP,CO)

Fc(8,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.135577977532185)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,CO2)

1 EqCompMolBalPump(VP,CO2)

Fc(8,H2O)

(.LO, .L, .UP, .M = 0, 11138.8529129714, 1000000, 0)

-1 EqTotMolStr(8)

-1 EqCompMolBalVacCondTurb(1,H2O)

1 EqCompMolBalPump(VP,H2O)

Fc(9,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.05638880618766)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,H2)

1 EqCompMolBalDeAertr(1,H2)

model.lst Wed May 30 15:17:17 2018 182


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Fc(9,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.05638880618766)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,O2)

1 EqCompMolBalDeAertr(1,O2)

Fc(9,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.05638880618766)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,N2)

1 EqCompMolBalDeAertr(1,N2)

Fc(9,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.05638880618766)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,CH4)

1 EqCompMolBalDeAertr(1,CH4)

Fc(9,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.05638880618766)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,CO)

1 EqCompMolBalDeAertr(1,CO)

Fc(9,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.05638880618766)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,CO2)

1 EqCompMolBalDeAertr(1,CO2)

Fc(9,H2O)

(.LO, .L, .UP, .M = 0, 11138.8529129714, 1000000, 0)

-1 EqTotMolStr(9)

-1 EqCompMolBalPump(VP,H2O)

1 EqCompMolBalDeAertr(1,H2O)

-0.005 EqVentVapDeAertr(1)

Fc(10,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.244983865250431)

-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,H2)

-1 EqCompMolBalStmDmd(MP,H2)

Fc(10,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.244983865250431)

-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,O2)

-1 EqCompMolBalStmDmd(MP,O2)

Fc(10,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.244983865250431)

model.lst Wed May 30 15:17:17 2018 183


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-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,N2)

-1 EqCompMolBalStmDmd(MP,N2)

Fc(10,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.244983865250431)

-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,CH4)

-1 EqCompMolBalStmDmd(MP,CH4)

Fc(10,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.244983865250431)

-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,CO)

-1 EqCompMolBalStmDmd(MP,CO)

Fc(10,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.244983865250431)

-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,CO2)

-1 EqCompMolBalStmDmd(MP,CO2)

Fc(10,H2O)

(.LO, .L, .UP, .M = 0, 2115.41644081786, 1000000, 0)

-1 EqTotMolStr(10)

1 EqCompMolBalCondHdr(1,H2O)

-1 EqCompMolBalStmDmd(MP,H2O)

Fc(11,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.04199432690379)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,H2)


Fc(11,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.04199432690379)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,O2)


Fc(11,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.04199432690379)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,N2)


Fc(11,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.04199432690379)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,CH4)


model.lst Wed May 30 15:17:17 2018 184


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Fc(11,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.04199432690379)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,CO)


Fc(11,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.04199432690379)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,CO2)


Fc(11,H2O)

(.LO, .L, .UP, .M = 0, 7538.52621063471, 1000000, 0)

-1 EqTotMolStr(11)

-1 EqCompMolBalCondHdr(1,H2O)



Fc(12,H2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(12)


-1 EqCompMolBalPLev(LP,H2)

Fc(12,O2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(12)


-1 EqCompMolBalPLev(LP,O2)

Fc(12,N2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(12)


-1 EqCompMolBalPLev(LP,N2)

Fc(12,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(12)


-1 EqCompMolBalPLev(LP,CH4)

Fc(12,CO)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(12)


-1 EqCompMolBalPLev(LP,CO)

Fc(12,CO2)

model.lst Wed May 30 15:17:17 2018 185


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(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(12)


-1 EqCompMolBalPLev(LP,CO2)

Fc(12,H2O)

(.LO, .L, .UP, .M = 0, 1946.37952422423, 1000000, 0)

-1 EqTotMolStr(12)



-1 EqCompMolBalPLev(LP,H2O)

Fc(13,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04135828737878)

-1 EqTotMolStr(13)

1 EqCompMolBalPump(MP,H2)

-1 EqCompMolBalDeAertr(1,H2)

Fc(13,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04135828737878)

-1 EqTotMolStr(13)

1 EqCompMolBalPump(MP,O2)

-1 EqCompMolBalDeAertr(1,O2)

Fc(13,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04135828737878)

-1 EqTotMolStr(13)

1 EqCompMolBalPump(MP,N2)

-1 EqCompMolBalDeAertr(1,N2)

Fc(13,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04135828737878)

-1 EqTotMolStr(13)

1 EqCompMolBalPump(MP,CH4)

-1 EqCompMolBalDeAertr(1,CH4)

Fc(13,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04135828737878)

-1 EqTotMolStr(13)

1 EqCompMolBalPump(MP,CO)

-1 EqCompMolBalDeAertr(1,CO)

Fc(13,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04135828737878)

-1 EqTotMolStr(13)

1 EqCompMolBalPump(MP,CO2)

-1 EqCompMolBalDeAertr(1,CO2)

Fc(13,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(13)

model.lst Wed May 30 15:17:17 2018 186


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1 EqCompMolBalPump(MP,H2O)

-1 EqCompMolBalDeAertr(1,H2O)

Fc(14,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,H2)


Fc(14,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,O2)


Fc(14,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,N2)


Fc(14,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,CH4)


Fc(14,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,CO)


Fc(14,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,CO2)


Fc(14,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(14)

1 EqCompMolBalPump(HP,H2O)


Fc(15,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,H2)


model.lst Wed May 30 15:17:17 2018 187


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Fc(15,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,O2)


Fc(15,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,N2)


Fc(15,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,CH4)


Fc(15,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,CO)


Fc(15,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04050339564498)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,CO2)


Fc(15,H2O)

(.LO, .L, .UP, .M = 0, 21261.6068534334, 1000000, 0)

-1 EqTotMolStr(15)

1 EqCompMolBalPump(HRSG,H2O)


Fc(16,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.891449202869133)

-1 EqTotMolStr(16)


Fc(16,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.891449202869133)

-1 EqTotMolStr(16)


Fc(16,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.891449202869133)

-1 EqTotMolStr(16)


model.lst Wed May 30 15:17:17 2018 188


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Fc(16,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.891449202869133)

-1 EqTotMolStr(16)


Fc(16,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.891449202869133)

-1 EqTotMolStr(16)


Fc(16,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.891449202869133)

-1 EqTotMolStr(16)


Fc(16,H2O)

(.LO, .L, .UP, .M = 0, 106.84224549464, 1000000, 0)

-1 EqTotMolStr(16)


1 EqVentVapDeAertr(1)

Fc(17,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.07152685502563)

-1 EqTotMolStr(17)


Fc(17,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.07152685502563)

-1 EqTotMolStr(17)


Fc(17,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.07152685502563)

-1 EqTotMolStr(17)


Fc(17,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.07152685502563)

-1 EqTotMolStr(17)


Fc(17,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.07152685502563)

-1 EqTotMolStr(17)


Fc(17,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.07152685502563)

-1 EqTotMolStr(17)


model.lst Wed May 30 15:17:17 2018 189


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Fc(17,H2O)

(.LO, .L, .UP, .M = 0, 744.690451097644, 1000000, 0)

-1 EqTotMolStr(17)



Fc(18,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.55600269997968)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,H2)

1 EqWtrMolBalBlr(MP,H2)

Fc(18,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.55600269997968)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,O2)

1 EqWtrMolBalBlr(MP,O2)

Fc(18,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.55600269997968)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,N2)

1 EqWtrMolBalBlr(MP,N2)

Fc(18,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.55600269997968)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,CH4)

1 EqWtrMolBalBlr(MP,CH4)

Fc(18,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.55600269997968)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,CO)

1 EqWtrMolBalBlr(MP,CO)

Fc(18,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.55600269997968)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,CO2)

1 EqWtrMolBalBlr(MP,CO2)

Fc(18,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(18)

-1 EqCompMolBalPump(MP,H2O)

1 EqWtrMolBalBlr(MP,H2O)

Fc(19,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(19)

model.lst Wed May 30 15:17:17 2018 190


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-1 EqCompMolBalPump(HP,H2)

1 EqWtrMolBalBlr(HP,H2)

Fc(19,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(19)

-1 EqCompMolBalPump(HP,O2)

1 EqWtrMolBalBlr(HP,O2)

Fc(19,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(19)

-1 EqCompMolBalPump(HP,N2)

1 EqWtrMolBalBlr(HP,N2)

Fc(19,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(19)

-1 EqCompMolBalPump(HP,CH4)

1 EqWtrMolBalBlr(HP,CH4)

Fc(19,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(19)

-1 EqCompMolBalPump(HP,CO)

1 EqWtrMolBalBlr(HP,CO)

Fc(19,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(19)

-1 EqCompMolBalPump(HP,CO2)

1 EqWtrMolBalBlr(HP,CO2)

Fc(19,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(19)

-1 EqCompMolBalPump(HP,H2O)

1 EqWtrMolBalBlr(HP,H2O)

Fc(20,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,H2)

1 EqWtrMolBalBlr(HRSG,H2)

Fc(20,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,O2)

1 EqWtrMolBalBlr(HRSG,O2)

model.lst Wed May 30 15:17:17 2018 191


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Fc(20,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,N2)

1 EqWtrMolBalBlr(HRSG,N2)

Fc(20,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,CH4)

1 EqWtrMolBalBlr(HRSG,CH4)

Fc(20,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,CO)

1 EqWtrMolBalBlr(HRSG,CO)

Fc(20,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.77619105695637)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,CO2)

1 EqWtrMolBalBlr(HRSG,CO2)

Fc(20,H2O)

(.LO, .L, .UP, .M = 0, 21261.6068534334, 1000000, 0)

-1 EqTotMolStr(20)

-1 EqCompMolBalPump(HRSG,H2O)

1 EqWtrMolBalBlr(HRSG,H2O)

Fc(21,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,H2)

(-0.002) EqEgyBalBlrCmbtr(HP)

1 EqGasMolBalBlr(HP,H2)

(0.002) EqGasEgyBalBlr(HP)

Fc(21,O2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,O2)


1 EqGasMolBalBlr(HP,O2)


Fc(21,N2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,N2)


model.lst Wed May 30 15:17:17 2018 192


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1 EqGasMolBalBlr(HP,N2)


Fc(21,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,CH4)

(0.0179) EqEgyBalBlrCmbtr(HP)

1 EqGasMolBalBlr(HP,CH4)

(-0.0179) EqGasEgyBalBlr(HP)

Fc(21,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,CO)


1 EqGasMolBalBlr(HP,CO)


Fc(21,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,CO2)


1 EqGasMolBalBlr(HP,CO2)


Fc(21,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(21)

-1 EqCompMolBalBlrCmbtr(HP,H2O)


1 EqGasMolBalBlr(HP,H2O)


Fc(22,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,H2)


Fc(22,O2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,O2)


Fc(22,N2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,N2)

model.lst Wed May 30 15:17:17 2018 193


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Fc(22,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,CH4)


Fc(22,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,CO)


Fc(22,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,CO2)


Fc(22,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(22)

-1 EqGasMolBalBlr(HP,H2O)


Fc(23,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,H2)

(-0.0016) EqEgyBalBlrCmbtr(MP)

1 EqGasMolBalBlr(MP,H2)

(0.0016) EqGasEgyBalBlr(MP)

Fc(23,O2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,O2)


1 EqGasMolBalBlr(MP,O2)


Fc(23,N2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,N2)


1 EqGasMolBalBlr(MP,N2)


Fc(23,CH4)

model.lst Wed May 30 15:17:17 2018 194


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(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,CH4)

(0.0185) EqEgyBalBlrCmbtr(MP)

1 EqGasMolBalBlr(MP,CH4)

(-0.0185) EqGasEgyBalBlr(MP)

Fc(23,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,CO)


1 EqGasMolBalBlr(MP,CO)


Fc(23,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,CO2)


1 EqGasMolBalBlr(MP,CO2)


Fc(23,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(23)

-1 EqCompMolBalBlrCmbtr(MP,H2O)


1 EqGasMolBalBlr(MP,H2O)


Fc(24,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,H2)


Fc(24,O2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,O2)


Fc(24,N2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,N2)


Fc(24,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

model.lst Wed May 30 15:17:17 2018 195


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-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,CH4)


Fc(24,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,CO)


Fc(24,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,CO2)


Fc(24,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(24)

-1 EqGasMolBalBlr(MP,H2O)


Fc(25,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,H2)

Fc(25,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,O2)

Fc(25,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,N2)

Fc(25,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,CH4)

Fc(25,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,CO)

model.lst Wed May 30 15:17:17 2018 196


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Fc(25,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,CO2)

Fc(25,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(25)


-1 EqWtrMolBalBlr(MP,H2O)

Fc(26,H2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,H2)

-1 EqWtrMolBalBlr(HP,H2)

Fc(26,O2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,O2)

-1 EqWtrMolBalBlr(HP,O2)

Fc(26,N2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,N2)

-1 EqWtrMolBalBlr(HP,N2)

Fc(26,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,CH4)

-1 EqWtrMolBalBlr(HP,CH4)

Fc(26,CO)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,CO)

-1 EqWtrMolBalBlr(HP,CO)

Fc(26,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,CO2)

-1 EqWtrMolBalBlr(HP,CO2)

Fc(26,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

model.lst Wed May 30 15:17:17 2018 197


05/30/18 15:17:15 Page 146




-1 EqTotMolStr(26)

1 EqCompMolBalPLev(HP,H2O)

-1 EqWtrMolBalBlr(HP,H2O)

Fc(27,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.750744182844828)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,H2)

(0) EqEgyBalBlrCmbtr(HP)

Fc(27,O2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,O2)


-3.7619 Eq1AirStr(27)

Fc(27,N2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,N2)


1 Eq1AirStr(27)

Fc(27,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -2.50307787502691)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,CH4)


Fc(27,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.881306244461624)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,CO)


Fc(27,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00349378003199496)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,CO2)


Fc(27,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00105818438488581)

-1 EqTotMolStr(27)

-1 EqDum1BlrCmbtr(HP,H2O)


Fc(28,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 5.13047056928183)

-1 EqTotMolStr(28)

model.lst Wed May 30 15:17:17 2018 198


05/30/18 15:17:15 Page 147




-1 EqDum1BlrCmbtr(HP,H2)


1 Eq1SyngasStr(28)

-3.2311 obj

Fc(28,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00588832674496806)

-1 EqTotMolStr(28)

-1 EqDum1BlrCmbtr(HP,O2)


Fc(28,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00549087072292911)

-1 EqTotMolStr(28)

-1 EqDum1BlrCmbtr(HP,N2)


Fc(28,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(28)

-1 EqDum1BlrCmbtr(HP,CH4)


1 Eq1bSyngasStr(28)

-10.0761 obj

Fc(28,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(28)

-1 EqDum1BlrCmbtr(HP,CO)


1 Eq1aSyngasStr(28)

-3.2347 obj

Fc(28,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(28)

-1 EqDum1BlrCmbtr(HP,CO2)


-11 Eq1SyngasStr(28)

-6 Eq1aSyngasStr(28)

-2 Eq1bSyngasStr(28)

Fc(28,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00663252087244315)

-1 EqTotMolStr(28)

-1 EqDum1BlrCmbtr(HP,H2O)


Fc(29,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -3.04416218415785)

-1 EqTotMolStr(29)

model.lst Wed May 30 15:17:17 2018 199


05/30/18 15:17:15 Page 148




-1 EqDum1BlrCmbtr(MP,H2)

(0) EqEgyBalBlrCmbtr(MP)

Fc(29,O2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(29)

-1 EqDum1BlrCmbtr(MP,O2)


-3.7619 Eq1AirStr(29)

Fc(29,N2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(29)

-1 EqDum1BlrCmbtr(MP,N2)


1 Eq1AirStr(29)

Fc(29,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -10.1049695726082)

-1 EqTotMolStr(29)

-1 EqDum1BlrCmbtr(MP,CH4)


Fc(29,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -3.55266071261906)

-1 EqTotMolStr(29)

-1 EqDum1BlrCmbtr(MP,CO)


Fc(29,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.0208381764182253)

-1 EqTotMolStr(29)

-1 EqDum1BlrCmbtr(MP,CO2)


Fc(29,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, 0.00917143803094023)

-1 EqTotMolStr(29)

-1 EqDum1BlrCmbtr(MP,H2O)


Fc(30,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,H2)


1 Eq1SyngasStr(30)

-3.2311 obj

Fc(30,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00435854572605727)

model.lst Wed May 30 15:17:17 2018 200


05/30/18 15:17:15 Page 149




-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,O2)


Fc(30,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.00589752137352565)

-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,N2)


Fc(30,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,CH4)


1 Eq1bSyngasStr(30)

-10.0761 obj

Fc(30,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,CO)


1 Eq1aSyngasStr(30)

-3.2347 obj

Fc(30,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,CO2)





Fc(30,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, 0.00359710154338311)

-1 EqTotMolStr(30)

-1 EqDum1BlrCmbtr(MP,H2O)


Fc(31,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.48343907484214)

-1 EqTotMolStr(31)


Fc(31,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.48343907484214)

-1 EqTotMolStr(31)


model.lst Wed May 30 15:17:17 2018 201


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Fc(31,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.48343907484214)

-1 EqTotMolStr(31)


Fc(31,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 1.48343907484214)

-1 EqTotMolStr(31)


Fc(31,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 1.48343907484214)

-1 EqTotMolStr(31)


Fc(31,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 1.48343907484214)

-1 EqTotMolStr(31)


Fc(31,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.324680354319786)

-1 EqTotMolStr(31)


Fc(32,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(32,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(32,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(32,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(32,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(32,CO2)

model.lst Wed May 30 15:17:17 2018 202


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(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(32,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(32)


Fc(33,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(33)


Fc(33,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(33)


Fc(33,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(33)


Fc(33,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(33)


Fc(33,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(33)


Fc(33,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(33)


Fc(33,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.187221312010263)

-1 EqTotMolStr(33)


Fc(34,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,H2)

Fc(34,O2)

model.lst Wed May 30 15:17:17 2018 203


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(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,O2)

Fc(34,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,N2)

Fc(34,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,CH4)

Fc(34,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,CO)

Fc(34,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,CO2)

Fc(34,H2O)

(.LO, .L, .UP, .M = 0, 598.025038518983, 1000000, 0)

-1 EqTotMolStr(34)


1 EqCompMolBalStmDmd(HP,H2O)

Fc(35,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(35)


1 EqCompMolBalStmDmd(MP,H2)

Fc(35,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(35)


1 EqCompMolBalStmDmd(MP,O2)

Fc(35,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(35)


model.lst Wed May 30 15:17:17 2018 204


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1 EqCompMolBalStmDmd(MP,N2)

Fc(35,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(35)


1 EqCompMolBalStmDmd(MP,CH4)

Fc(35,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(35)


1 EqCompMolBalStmDmd(MP,CO)

Fc(35,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(35)


1 EqCompMolBalStmDmd(MP,CO2)

Fc(35,H2O)

(.LO, .L, .UP, .M = 0, 2115.41644081786, 1000000, 0)

-1 EqTotMolStr(35)


1 EqCompMolBalStmDmd(MP,H2O)

Fc(36,H2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,H2)

1 EqCompMolBalStmDmd(LP,H2)

Fc(36,O2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,O2)

1 EqCompMolBalStmDmd(LP,O2)

Fc(36,N2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,N2)

1 EqCompMolBalStmDmd(LP,N2)

Fc(36,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,CH4)

1 EqCompMolBalStmDmd(LP,CH4)

Fc(36,CO)

model.lst Wed May 30 15:17:17 2018 205


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(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,CO)

1 EqCompMolBalStmDmd(LP,CO)

Fc(36,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,CO2)

1 EqCompMolBalStmDmd(LP,CO2)

Fc(36,H2O)

(.LO, .L, .UP, .M = 0, 4825.08473129786, 1000000, 0)

-1 EqTotMolStr(36)

-1 EqCompMolBalPLev(LP,H2O)

1 EqCompMolBalStmDmd(LP,H2O)

Fc(37,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.333221469699439)

-1 EqTotMolStr(37)


-1 EqCompMolBalStmDmd(HP,H2)

Fc(37,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.333221469699439)

-1 EqTotMolStr(37)


-1 EqCompMolBalStmDmd(HP,O2)

Fc(37,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.333221469699439)

-1 EqTotMolStr(37)


-1 EqCompMolBalStmDmd(HP,N2)

Fc(37,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.333221469699439)

-1 EqTotMolStr(37)


-1 EqCompMolBalStmDmd(HP,CH4)

Fc(37,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.333221469699439)

-1 EqTotMolStr(37)


-1 EqCompMolBalStmDmd(HP,CO)

Fc(37,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.333221469699439)

-1 EqTotMolStr(37)


model.lst Wed May 30 15:17:17 2018 206


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-1 EqCompMolBalStmDmd(HP,CO2)

Fc(37,H2O)

(.LO, .L, .UP, .M = 0, 598.025038518983, 1000000, 0)

-1 EqTotMolStr(37)


-1 EqCompMolBalStmDmd(HP,H2O)

Fc(38,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04199432690379)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,H2)

Fc(38,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04199432690379)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,O2)

Fc(38,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04199432690379)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,N2)

Fc(38,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04199432690379)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,CH4)

Fc(38,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04199432690379)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,CO)

Fc(38,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.04199432690379)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,CO2)

Fc(38,H2O)

(.LO, .L, .UP, .M = 0, 4825.08473129786, 1000000, 0)

-1 EqTotMolStr(38)


-1 EqCompMolBalStmDmd(LP,H2O)

Fc(39,H2)

model.lst Wed May 30 15:17:17 2018 207


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(.LO, .L, .UP, .M = 0, 0, 0, -2.97247199166815)

-1 EqTotMolStr(39)

1 EqCompMolBalGTCmpr(1,H2)

(0) EqWorkGTCmpr(1)

Fc(39,O2)

(.LO, .L, .UP, .M = 0, 18171.4005610171, 1000000, 0)

-1 EqTotMolStr(39)

-3.7619 Eq1AirStr(39)

1 EqCompMolBalGTCmpr(1,O2)

(0) EqWorkGTCmpr(1)

Fc(39,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, 1000000, 0)

-1 EqTotMolStr(39)

1 Eq1AirStr(39)

1 EqCompMolBalGTCmpr(1,N2)

(0) EqWorkGTCmpr(1)

Fc(39,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -9.96133367289618)

-1 EqTotMolStr(39)

1 EqCompMolBalGTCmpr(1,CH4)

(-0.0207) EqWorkGTCmpr(1)

Fc(39,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -3.51204290051019)

-1 EqTotMolStr(39)

1 EqCompMolBalGTCmpr(1,CO)


Fc(39,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.0327174386162863)

-1 EqTotMolStr(39)

1 EqCompMolBalGTCmpr(1,CO2)


Fc(39,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.0162438214395344)

-1 EqTotMolStr(39)

1 EqCompMolBalGTCmpr(1,H2O)


Fc(40,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,H2)

(0.0026) EqEgyBalBlrCmbtr(GT)

-1 EqCompMolBalGTCmpr(1,H2)


model.lst Wed May 30 15:17:17 2018 208


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Fc(40,O2)

(.LO, .L, .UP, .M = 0, 18171.4005610171, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,O2)


-1 EqCompMolBalGTCmpr(1,O2)


Fc(40,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,N2)


-1 EqCompMolBalGTCmpr(1,N2)


Fc(40,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,CH4)

(-0.0167) EqEgyBalBlrCmbtr(GT)

-1 EqCompMolBalGTCmpr(1,CH4)

(0.0167) EqWorkGTCmpr(1)

Fc(40,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,CO)


-1 EqCompMolBalGTCmpr(1,CO)


Fc(40,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,CO2)


-1 EqCompMolBalGTCmpr(1,CO2)


Fc(40,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(40)

-1 EqDum1BlrCmbtr(GT,H2O)


-1 EqCompMolBalGTCmpr(1,H2O)


Fc(41,H2)

(.LO, .L, .UP, .M = 0, 5338.12355237439, 1000000, 0)

-1 EqTotMolStr(41)

model.lst Wed May 30 15:17:17 2018 209


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-1 EqDum1BlrCmbtr(GT,H2)

(0) EqEgyBalBlrCmbtr(GT)

1 Eq1SyngasStr(41)

-3.2311 obj

Fc(41,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.0695983368288706)

-1 EqTotMolStr(41)

-1 EqDum1BlrCmbtr(GT,O2)


Fc(41,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.0638947852128767)

-1 EqTotMolStr(41)

-1 EqDum1BlrCmbtr(GT,N2)


Fc(41,CH4)

(.LO, .L, .UP, .M = 0, 970.567918613525, 1000000, 0)

-1 EqTotMolStr(41)

-1 EqDum1BlrCmbtr(GT,CH4)


1 Eq1bSyngasStr(41)

-10.0761 obj

Fc(41,CO)

(.LO, .L, .UP, .M = 0, 2911.70375584058, 1000000, 0)

-1 EqTotMolStr(41)

-1 EqDum1BlrCmbtr(GT,CO)


1 Eq1aSyngasStr(41)

-3.2347 obj

Fc(41,CO2)

(.LO, .L, .UP, .M = 0, 485.283959306763, 1000000, 0)

-1 EqTotMolStr(41)

-1 EqDum1BlrCmbtr(GT,CO2)





Fc(41,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, -0.0924658656311785)

-1 EqTotMolStr(41)

-1 EqDum1BlrCmbtr(GT,H2O)


Fc(42,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(42)

model.lst Wed May 30 15:17:17 2018 210


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-1 EqCompMolBalBlrCmbtr(GT,H2)


1 EqCompMolBalGTExpdr(1,H2)

(-0.0101) EqWorkGTExpdr(1)

Fc(42,O2)

(.LO, .L, .UP, .M = 0, 12105.3510696826, 1000000, 0)

-1 EqTotMolStr(42)

-1 EqCompMolBalBlrCmbtr(GT,O2)


1 EqCompMolBalGTExpdr(1,O2)


Fc(42,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, 1000000, 0)

-1 EqTotMolStr(42)

-1 EqCompMolBalBlrCmbtr(GT,N2)


1 EqCompMolBalGTExpdr(1,N2)


Fc(42,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(42)

-1 EqCompMolBalBlrCmbtr(GT,CH4)


1 EqCompMolBalGTExpdr(1,CH4)


Fc(42,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(42)

-1 EqCompMolBalBlrCmbtr(GT,CO)


1 EqCompMolBalGTExpdr(1,CO)

(0.0199) EqWorkGTExpdr(1)

Fc(42,CO2)

(.LO, .L, .UP, .M = 0, 4367.55563376086, 1000000, 0)

-1 EqTotMolStr(42)

-1 EqCompMolBalBlrCmbtr(GT,CO2)


1 EqCompMolBalGTExpdr(1,CO2)


Fc(42,H2O)

(.LO, .L, .UP, .M = 0, 7279.25938960144, 1000000, 0)

-1 EqTotMolStr(42)

-1 EqCompMolBalBlrCmbtr(GT,H2O)


1 EqCompMolBalGTExpdr(1,H2O)

model.lst Wed May 30 15:17:17 2018 211


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Fc(43,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,H2)

(0.0038) EqEgyBalBlrCmbtr(GTSF)

-1 EqCompMolBalGTExpdr(1,H2)


Fc(43,O2)

(.LO, .L, .UP, .M = 0, 12105.3510696826, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,O2)


-1 EqCompMolBalGTExpdr(1,O2)


Fc(43,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,N2)


-1 EqCompMolBalGTExpdr(1,N2)


Fc(43,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,CH4)

(-0.0145) EqEgyBalBlrCmbtr(GTSF)

-1 EqCompMolBalGTExpdr(1,CH4)


Fc(43,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,CO)


-1 EqCompMolBalGTExpdr(1,CO)


Fc(43,CO2)

(.LO, .L, .UP, .M = 0, 4367.55563376086, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,CO2)


-1 EqCompMolBalGTExpdr(1,CO2)


Fc(43,H2O)

model.lst Wed May 30 15:17:17 2018 212


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(.LO, .L, .UP, .M = 0, 7279.25938960144, 1000000, 0)

-1 EqTotMolStr(43)

-1 EqDum1BlrCmbtr(GTSF,H2O)


-1 EqCompMolBalGTExpdr(1,H2O)


Fc(44,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 3.4144925542898)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,H2)

(0) EqEgyBalBlrCmbtr(GTSF)

1 Eq1SyngasStr(44)

-3.2311 obj

Fc(44,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.0178124676003816)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,O2)


Fc(44,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.0174440558928335)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,N2)


Fc(44,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,CH4)


1 Eq1bSyngasStr(44)

-10.0761 obj

Fc(44,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,CO)


1 Eq1aSyngasStr(44)

-3.2347 obj

Fc(44,CO2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,CO2)





model.lst Wed May 30 15:17:17 2018 213


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Fc(44,H2O)

(.LO, .L, .UP, .M = 0, 0, 0, 0.0202982062941186)

-1 EqTotMolStr(44)

-1 EqDum1BlrCmbtr(GTSF,H2O)


Fc(45,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,H2)


1 EqGasMolBalBlr(HRSG,H2)

(0.0038) EqGasEgyBalBlr(HRSG)

Fc(45,O2)

(.LO, .L, .UP, .M = 0, 12105.3510696826, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,O2)


1 EqGasMolBalBlr(HRSG,O2)


Fc(45,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,N2)


1 EqGasMolBalBlr(HRSG,N2)


Fc(45,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,CH4)


1 EqGasMolBalBlr(HRSG,CH4)

(-0.0145) EqGasEgyBalBlr(HRSG)

Fc(45,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,CO)


1 EqGasMolBalBlr(HRSG,CO)


Fc(45,CO2)

(.LO, .L, .UP, .M = 0, 4367.55563376086, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,CO2)

model.lst Wed May 30 15:17:17 2018 214


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1 EqGasMolBalBlr(HRSG,CO2)


Fc(45,H2O)

(.LO, .L, .UP, .M = 0, 7279.25938960144, 1000000, 0)

-1 EqTotMolStr(45)

-1 EqCompMolBalBlrCmbtr(GTSF,H2O)


1 EqGasMolBalBlr(HRSG,H2O)


Fc(46,H2)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(46)

-1 EqGasMolBalBlr(HRSG,H2)


Fc(46,O2)

(.LO, .L, .UP, .M = 0, 12105.3510696826, 1000000, 0)

-1 EqTotMolStr(46)

-1 EqGasMolBalBlr(HRSG,O2)


Fc(46,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, 1000000, 0)

-1 EqTotMolStr(46)

-1 EqGasMolBalBlr(HRSG,N2)


Fc(46,CH4)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(46)

-1 EqGasMolBalBlr(HRSG,CH4)


Fc(46,CO)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(46)

-1 EqGasMolBalBlr(HRSG,CO)


Fc(46,CO2)

(.LO, .L, .UP, .M = 0, 4367.55563376086, 1000000, 0)

-1 EqTotMolStr(46)

-1 EqGasMolBalBlr(HRSG,CO2)


Fc(46,H2O)

(.LO, .L, .UP, .M = 0, 7279.25938960144, 1000000, 0)

-1 EqTotMolStr(46)

model.lst Wed May 30 15:17:17 2018 215


05/30/18 15:17:15 Page 164




-1 EqGasMolBalBlr(HRSG,H2O)


Fc(47,H2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,H2)

Fc(47,O2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,O2)

Fc(47,N2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,N2)

Fc(47,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,CH4)

Fc(47,CO)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,CO)

Fc(47,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, EPS)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,CO2)

Fc(47,H2O)

(.LO, .L, .UP, .M = 0, 20623.7586478304, 1000000, 0)

-1 EqTotMolStr(47)


-1 EqWtrMolBalBlr(HRSG,H2O)

Fc(48,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.53012693049297)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,H2)

model.lst Wed May 30 15:17:17 2018 216


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Fc(48,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.53012693049297)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,O2)

Fc(48,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.53012693049297)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,N2)

Fc(48,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.53012693049297)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,CH4)

Fc(48,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.53012693049297)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,CO)

Fc(48,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.53012693049297)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,CO2)

Fc(48,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(48)


1 EqMolBalVlv(HPMP,H2O)

Fc(49,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(49)


-1 EqMolBalVlv(HPMP,H2)

Fc(49,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(49)


-1 EqMolBalVlv(HPMP,O2)

Fc(49,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(49)

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-1 EqMolBalVlv(HPMP,N2)

Fc(49,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(49)


-1 EqMolBalVlv(HPMP,CH4)

Fc(49,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(49)


-1 EqMolBalVlv(HPMP,CO)

Fc(49,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.277992498668956)

-1 EqTotMolStr(49)


-1 EqMolBalVlv(HPMP,CO2)

Fc(49,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(49)


-1 EqMolBalVlv(HPMP,H2O)

Fc(50,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,H2)

Fc(50,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,O2)

Fc(50,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,N2)

Fc(50,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,CH4)

model.lst Wed May 30 15:17:17 2018 218


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Fc(50,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,CO)

Fc(50,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.27451639337227)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,CO2)

Fc(50,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0872950813620075)

-1 EqTotMolStr(50)


1 EqMolBalVlv(MPLP,H2O)

Fc(51,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(51)


-1 EqMolBalVlv(MPLP,H2)

Fc(51,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(51)


-1 EqMolBalVlv(MPLP,O2)

Fc(51,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(51)


-1 EqMolBalVlv(MPLP,N2)

Fc(51,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(51)


-1 EqMolBalVlv(MPLP,CH4)

Fc(51,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(51)


-1 EqMolBalVlv(MPLP,CO)

Fc(51,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(51)

model.lst Wed May 30 15:17:17 2018 219


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-1 EqMolBalVlv(MPLP,CO2)

Fc(51,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(51)


-1 EqMolBalVlv(MPLP,H2O)

Fc(52,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,H2)

Fc(52,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,O2)

Fc(52,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,N2)

Fc(52,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,CH4)

Fc(52,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,CO)

Fc(52,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.58707618045143)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,CO2)

Fc(52,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(52)

-1 EqWtrMolBalBlr(MP,H2O)

Fc(53,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,H2)

Fc(53,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

model.lst Wed May 30 15:17:17 2018 220


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-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,O2)

Fc(53,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,N2)

Fc(53,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,CH4)

Fc(53,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,CO)

Fc(53,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,CO2)

Fc(53,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(53)

-1 EqWtrMolBalBlr(HP,H2O)

Fc(54,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(54)

-1 EqWtrMolBalBlr(HRSG,H2)

Fc(54,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(54)

-1 EqWtrMolBalBlr(HRSG,O2)

Fc(54,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(54)

-1 EqWtrMolBalBlr(HRSG,N2)

Fc(54,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(54)

-1 EqWtrMolBalBlr(HRSG,CH4)

Fc(54,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(54)

model.lst Wed May 30 15:17:17 2018 221


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-1 EqWtrMolBalBlr(HRSG,CO)

Fc(54,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.80811942916193)

-1 EqTotMolStr(54)

-1 EqWtrMolBalBlr(HRSG,CO2)

Fc(54,H2O)

(.LO, .L, .UP, .M = 0, 637.848205603002, 1000000, 0)

-1 EqTotMolStr(54)

-1 EqWtrMolBalBlr(HRSG,H2O)

Fc(55,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.230777556539871)

-1 EqTotMolStr(55)

1 EqCompMolBalMPStmTurb(2,H2)


Fc(55,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.230777556539871)

-1 EqTotMolStr(55)

1 EqCompMolBalMPStmTurb(2,O2)


Fc(55,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.230777556539871)

-1 EqTotMolStr(55)

1 EqCompMolBalMPStmTurb(2,N2)


Fc(55,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.230777556539871)

-1 EqTotMolStr(55)

1 EqCompMolBalMPStmTurb(2,CH4)


Fc(55,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.230777556539871)

-1 EqTotMolStr(55)

1 EqCompMolBalMPStmTurb(2,CO)


Fc(55,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.230777556539871)

-1 EqTotMolStr(55)

1 EqCompMolBalMPStmTurb(2,CO2)


Fc(55,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(55)

model.lst Wed May 30 15:17:17 2018 222


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1 EqCompMolBalMPStmTurb(2,H2O)


(-0.003) EqVPWorkMPStmTurb(2)


Fc(56,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(56)



Fc(56,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(56)



Fc(56,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(56)



Fc(56,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(56)



Fc(56,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(56)



Fc(56,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(56)



Fc(56,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(56)


(0.003) EqVPWorkMPStmTurb(2)


Fc(57,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.196608447131505)

-1 EqTotMolStr(57)

model.lst Wed May 30 15:17:17 2018 223


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Fc(57,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.196608447131505)

-1 EqTotMolStr(57)



Fc(57,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.196608447131505)

-1 EqTotMolStr(57)



Fc(57,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.196608447131505)

-1 EqTotMolStr(57)



Fc(57,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.196608447131505)

-1 EqTotMolStr(57)



Fc(57,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.196608447131505)

-1 EqTotMolStr(57)



Fc(57,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(57)



Fc(58,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(58)



Fc(58,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(58)



model.lst Wed May 30 15:17:17 2018 224


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Fc(58,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(58)



Fc(58,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(58)



Fc(58,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(58)



Fc(58,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(58)



Fc(58,H2O)

(.LO, .L, .UP, .M = 0, 16385.9503504084, 1000000, 0)

-1 EqTotMolStr(58)






Fc(59,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.27451639337227)

-1 EqTotMolStr(59)



Fc(59,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.27451639337227)

-1 EqTotMolStr(59)



Fc(59,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.27451639337227)

-1 EqTotMolStr(59)



model.lst Wed May 30 15:17:17 2018 225


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Fc(59,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.27451639337227)

-1 EqTotMolStr(59)



Fc(59,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.27451639337227)

-1 EqTotMolStr(59)



Fc(59,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.27451639337227)

-1 EqTotMolStr(59)



Fc(59,H2O)

(.LO, .L, .UP, .M = 0, 3881.61564733172, 1000000, 0)

-1 EqTotMolStr(59)





Fc(60,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(60)



Fc(60,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(60)



Fc(60,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(60)



Fc(60,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(60)



Fc(60,CO)

model.lst Wed May 30 15:17:17 2018 226


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(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(60)



Fc(60,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.884305543015365)

-1 EqTotMolStr(60)



Fc(60,H2O)

(.LO, .L, .UP, .M = 0, 1365.48179010526, 1000000, 0)

-1 EqTotMolStr(60)




Fc(61,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.11823096652664)

-1 EqTotMolStr(61)



Fc(61,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.11823096652664)

-1 EqTotMolStr(61)



Fc(61,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.11823096652664)

-1 EqTotMolStr(61)



Fc(61,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.11823096652664)

-1 EqTotMolStr(61)



Fc(61,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.11823096652664)

-1 EqTotMolStr(61)



Fc(61,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.11823096652664)

-1 EqTotMolStr(61)

model.lst Wed May 30 15:17:17 2018 227


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Fc(61,H2O)

(.LO, .L, .UP, .M = 0, 11138.8529129714, 1000000, 0)

-1 EqTotMolStr(61)



Fc(62,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(62)



Fc(62,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(62)



Fc(62,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(62)



Fc(62,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(62)



Fc(62,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(62)



Fc(62,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -1.44536543134065)

-1 EqTotMolStr(62)



Fc(62,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0604157312578955)

-1 EqTotMolStr(62)




model.lst Wed May 30 15:17:17 2018 228


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Fc(63,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.2226235148203)

-1 EqTotMolStr(63)



Fc(63,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.2226235148203)

-1 EqTotMolStr(63)



Fc(63,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.2226235148203)

-1 EqTotMolStr(63)



Fc(63,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.2226235148203)

-1 EqTotMolStr(63)



Fc(63,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.2226235148203)

-1 EqTotMolStr(63)



Fc(63,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.2226235148203)

-1 EqTotMolStr(63)



Fc(63,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(63)





Fc(64,H2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(64)


model.lst Wed May 30 15:17:17 2018 229


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Fc(64,O2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(64)



Fc(64,N2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(64)



Fc(64,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(64)



Fc(64,CO)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(64)



Fc(64,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, 0.881478515047913)

-1 EqTotMolStr(64)



Fc(64,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0)

-1 EqTotMolStr(64)




Fc(65,H2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(65)



Fc(65,O2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(65)



model.lst Wed May 30 15:17:17 2018 230


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Fc(65,N2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(65)



Fc(65,CH4)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(65)



Fc(65,CO)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(65)



Fc(65,CO2)

(.LO, .L, .UP, .M = 0, 0, 0, -0.118230966526509)

-1 EqTotMolStr(65)



Fc(65,H2O)

(.LO, .L, .UP, .M = 0, 0, 1000000, 0.0502181423142483)

-1 EqTotMolStr(65)



---- T Temperature of stream

T(1)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)

(-1.039226E-5) EqEnthVapStr2(1)

1 EqTP2(1)

1 EqLogP23(1)

1 EqInHPTHPStmTurb(1)

1 EqTRel1PLev(HP,1)

T(2)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)


1 EqTP2(2)

1 EqLogP23(2)

1 EqPTRel1cHPStmTurb(1)

T(3)

(.LO, .L, .UP, .M = 414, 438.169647740304, 581, 0)


model.lst Wed May 30 15:17:17 2018 231


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T Temperature of stream

1 EqTP2(3)

1 EqLogP23(3)


T(4)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


1 EqTP2(4)

1 EqLogP23(4)

T(5)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)


1 EqTP2(5)

1 EqLogP23(5)

1 EqInMPTMPStmTurb(1)

1 EqTRel1PLev(MP,5)

T(6)

(.LO, .L, .UP, .M = 414, 438.169647740304, 581, 0)


1 EqTP2(6)

1 EqLogP23(6)

1 EqPTRel1cMPStmTurb(1)

T(7)

(.LO, .L, .UP, .M = 333, 333.173030851526, 334, 0)


1 EqTP2(7)

1 EqLogP23(7)

T(8)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)

1 EqnTfSatLiqVap(8)

1 EqTEqPump(VP)

T(9)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)

(-9.397077E-6) EqEnthLiqStr(9)

-0.0015 EqTrLiq(9)

-1 EqTEqPump(VP)

T(10)

(.LO, .L, .UP, .M = 469, 485.588337116894, 701, 0)

1 EqnTfSatLiqVap(10)

T(11)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


T(12)

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(.LO, .L, .UP, .M = 414, 438.169647740304, 581, 0)


1 EqTP2(12)

1 EqLogP23(12)

1 EqTRel1PLev(LP,12)

T(13)

(.LO, .L, .UP, .M = 382, 382.476578027229, 383, 0)


1 EqTEqPump(MP)

T(14)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


1 EqTEqPump(HP)

T(15)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


1 EqTEqPump(HRSG)

T(16)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


T(17)

(.LO, .L, .UP, .M = 298.15, 298.15, 298.15, -0.193165569820292)


-0.0015 EqTrLiq(17)

T(18)

(.LO, .L, .UP, .M = 382, 382.476578027229, 383, 0)


-0.0015 EqTrLiq(18)

-1 EqTEqPump(MP)

-1 EqRel3Blr(MP)

T(19)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


-0.0015 EqTrLiq(19)

-1 EqTEqPump(HP)

-1 EqRel3Blr(HP)

T(20)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


-0.0015 EqTrLiq(20)

-1 EqTEqPump(HRSG)

-1 EqRel3Blr(HRSG)

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T(21)

(.LO, .L, .UP, .M = 297, 540.580060386281, 1501, 0)

(-8.144528E-6) EqEnthpyGasStr1(21,H2)

(-8.733170E-6) EqEnthpyGasStr1(21,O2)

(-8.297427E-6) EqEnthpyGasStr1(21,N2)

(-1.348970E-5) EqEnthpyGasStr1(21,CH4)

(-8.367907E-6) EqEnthpyGasStr1(21,CO)

(-1.261576E-5) EqEnthpyGasStr1(21,CO2)

(-9.893712E-6) EqEnthpyGasStr1(21,H2O)

1 EqTCnstrtBlrCmbtr(HP)

1 EqRel2Blr(HP)

T(22)

(.LO, .L, .UP, .M = 297, 393, 1501, 0)








1 EqRel3Blr(HP)

T(23)

(.LO, .L, .UP, .M = 297, 495.588337116896, 1501, 0)








1 EqTCnstrtBlrCmbtr(MP)

1 EqRel2Blr(MP)

T(24)

(.LO, .L, .UP, .M = 297, 392.476578027229, 1501, 0)








1 EqRel3Blr(MP)

T(25)

(.LO, .L, .UP, .M = 469, 485.588337116896, 701, 0)


1 EqTP2(25)

1 EqLogP23(25)

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-1 EqRel2Blr(MP)

1 EqT1

T(26)

(.LO, .L, .UP, .M = 528, 530.580060386281, 795, 0)


1 EqTP2(26)

1 EqLogP23(26)

-1 EqRel2Blr(HP)

1 EqT2

T(27)

(.LO, .L, .UP, .M = 297, 298.15, 1501, 0)








1 Eq3AirStr(27)

T(28)

(.LO, .L, .UP, .M = 297, 298.15, 1501, 0)








1 Eq2SyngasStr(28)

T(29)

(.LO, .L, .UP, .M = 297, 298.15, 1501, 0)








1 Eq3AirStr(29)

T(30)

(.LO, .L, .UP, .M = 297, 298.15, 1501, 0)






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1 Eq2SyngasStr(30)

T(31)

(.LO, .L, .UP, .M = 528, 530.580060386281, 795, 0)


1 EqTP2(31)

1 EqLogP23(31)

T(32)

(.LO, .L, .UP, .M = 469, 485.588337116896, 701, 0)


1 EqTP2(32)

1 EqLogP23(32)

T(33)

(.LO, .L, .UP, .M = 414, 438.169647811269, 581, 0)


1 EqTP2(33)

1 EqLogP23(33)

T(34)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)


1 EqTP2(34)

1 EqLogP23(34)

1 EqTRel1PLev(HP,34)

T(35)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)


1 EqTP2(35)

1 EqLogP23(35)

1 EqTRel1PLev(MP,35)

T(36)

(.LO, .L, .UP, .M = 414, 438.169647740304, 581, 0)


1 EqTP2(36)

1 EqLogP23(36)

1 EqTRel1PLev(LP,36)

T(37)

(.LO, .L, .UP, .M = 528, 530.580060386281, 795, 0)


T(38)

(.LO, .L, .UP, .M = 414, 438.169647740303, 581, 0)


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T(39)

(.LO, .L, .UP, .M = 298, 298.15, 299, 0)








1 Eq3AirStr(39)

1 EqInTGTCmpr(1)

T(40)

(.LO, .L, .UP, .M = 298, 624.925663385689, 704, 0)








1 EqOutTGTCmpr(1)

T(41)

(.LO, .L, .UP, .M = 298, 298.15, 299, 0)








1 Eq2SyngasStr(41)

T(42)

(.LO, .L, .UP, .M = 298, 1500, 1510, 0)








1 EqTCnstrtBlrCmbtr(GT)

1 EqInTGTExpdr(1)

T(43)

(.LO, .L, .UP, .M = 298, 761.291470669467, 1510, 0)




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1 EqOutTGTExpdr(1)

T(44)

(.LO, .L, .UP, .M = 298, 298.15, 299, 0)








1 Eq2SyngasStr(44)

T(45)

(.LO, .L, .UP, .M = 298, 761.291470669467, 1510, 0)








1 EqTCnstrtBlrCmbtr(GTSF)

1 EqRel2Blr(HRSG)

T(46)

(.LO, .L, .UP, .M = 298, 392.476577887812, 1510, 0)








1 EqRel3Blr(HRSG)

T(47)

(.LO, .L, .UP, .M = 528, 695.267448409643, 795, 0)


1 EqTP2(47)

1 EqLogP23(47)

-1 EqRel2Blr(HRSG)

1 EqT3

T(48)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)


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1 EqTP2(48)

1 EqLogP23(48)


T(49)

(.LO, .L, .UP, .M = 469, 485.588337116896, 795, 0)


1 EqTP2(49)

1 EqLogP23(49)

T(50)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)


1 EqTP2(50)

1 EqLogP23(50)


T(51)

(.LO, .L, .UP, .M = 414, 438.169647811269, 701, 0)


1 EqTP2(51)

1 EqLogP23(51)

T(52)

(.LO, .L, .UP, .M = 469, 485.588337116896, 701, 0)


T(53)

(.LO, .L, .UP, .M = 528, 530.580060386281, 795, 0)


T(54)

(.LO, .L, .UP, .M = 528, 530.580060386281, 795, 0)


T(55)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)


1 EqTP2(55)

1 EqLogP23(55)

1 EqInMPTMPStmTurb(2)


T(56)

(.LO, .L, .UP, .M = 414, 460, 581, 0)


1 EqTP2(56)

1 EqLogP23(56)

1 EqPTRel1cMPStmTurb(2)

T(57)

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(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


1 EqTP2(57)

1 EqLogP23(57)

T(58)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)


1 EqTP2(58)

1 EqLogP23(58)



T(59)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)


1 EqTP2(59)

1 EqLogP23(59)


T(60)

(.LO, .L, .UP, .M = 414, 438.169647811269, 581, 0)


1 EqTP2(60)

1 EqLogP23(60)


T(61)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


1 EqTP2(61)

1 EqLogP23(61)

T(62)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)


1 EqTP2(62)

1 EqLogP23(62)



T(63)

(.LO, .L, .UP, .M = 469, 530, 701, 0)


1 EqTP2(63)

1 EqLogP23(63)


T(64)

(.LO, .L, .UP, .M = 414, 460, 581, 0)


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1 EqTP2(64)

1 EqLogP23(64)


T(65)

(.LO, .L, .UP, .M = 333, 333.173030851526, 334, 0)


1 EqTP2(65)

1 EqLogP23(65)

---- P Pressure of stream

P(1)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(1)

1 EqInHPPHPStmTurb(1)

1 EqPRel2PLev(HP,1)

P(2)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(2)

1 EqOutMPPHPStmTurb(1)

1 EqPRel1PLev(MP,2)

P(3)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(3)

1 EqOutLPPHPStmTurb(1)

1 EqPRel1PLev(LP,3)

P(4)

(.LO, .L, .UP, .M = 0.19, 0.2, 0.21, 0)

1 EqTSat(4)

1 EqPr1VacCondTurb(1,4)

P(5)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(5)

1 EqInMPPMPStmTurb(1)

1 EqPRel2PLev(MP,5)

P(6)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(6)

1 EqOutLPPMPStmTurb(1)

1 EqPRel1PLev(LP,6)

P(7)

(.LO, .L, .UP, .M = 0.19, 0.2, 0.21, 0)

1 EqTSat(7)

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P Pressure of stream


P(8)

(.LO, .L, .UP, .M = 0.19, 0.2, 0.21, 0)

1 EqTSat(8)


-1 EqPgePump(VP)

(0.0056) EqWorkPump(VP)

P(9)

(.LO, .L, .UP, .M = 1.4, 1.4, 1.4, 0.380900550349967)

1 EqPgePump(VP)

(-0.0056) EqWorkPump(VP)

P(10)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(10)

-1 EqPRel1StmDmd(MP)

P(11)

(.LO, .L, .UP, .M = 1.39, 1.4, 1.41, 0)

1 EqTSat(11)

1 EqPRel1CondHdr(1)

P(12)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(12)

1 EqPRel2PLev(LP,12)

P(13)

(.LO, .L, .UP, .M = 1.39, 1.4, 1.41, 0)

1 EqTSat(13)

-1 EqPgePump(MP)

(0) EqWorkPump(MP)

1 EqPRel2DeAertr(1,13)

P(14)

(.LO, .L, .UP, .M = 1.39, 1.4, 1.41, 0)

1 EqTSat(14)

-1 EqPgePump(HP)

(0) EqWorkPump(HP)


P(15)

(.LO, .L, .UP, .M = 1.39, 1.4, 1.41, 0)

1 EqTSat(15)

-1 EqPgePump(HRSG)

(0.0106) EqWorkPump(HRSG)


P(16)

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(.LO, .L, .UP, .M = 1.39, 1.4, 1.41, 0)

1 EqTSat(16)


P(18)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqPgePump(MP)

(0) EqWorkPump(MP)

1 EqRel5Blr(MP)

P(19)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqPgePump(HP)

(0) EqWorkPump(HP)

1 EqRel5Blr(HP)

P(20)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqPgePump(HRSG)

(-0.0106) EqWorkPump(HRSG)

1 EqRel5Blr(HRSG)

P(21)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

1 EqOutPBlrCmbtr1(HP,27)

1 EqOutPBlrCmbtr1(HP,28)

1 EqRel4Blr(HP)

P(22)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

-1 EqRel4Blr(HP)

P(23)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

1 EqOutPBlrCmbtr1(MP,29)

1 EqOutPBlrCmbtr1(MP,30)

1 EqRel4Blr(MP)

P(24)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

-1 EqRel4Blr(MP)

P(25)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(25)

1 EqPRel1PLev(MP,25)

-1 EqRel5Blr(MP)

-1 EqRel6Blr(MP)

P(26)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

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1 EqTSat(26)

1 EqPRel1PLev(HP,26)

-1 EqRel5Blr(HP)

-1 EqRel6Blr(HP)

P(27)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

-1 EqOutPBlrCmbtr1(HP,27)

1 Eq2AirStr(27)

P(28)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

-1 EqOutPBlrCmbtr1(HP,28)

P(29)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

-1 EqOutPBlrCmbtr1(MP,29)

1 Eq2AirStr(29)

P(30)

(.LO, .L, .UP, .M = 0.95, 1.01325, 1.15, 0)

-1 EqOutPBlrCmbtr1(MP,30)

P(31)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(31)


P(32)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(32)


P(33)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(33)


P(34)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(34)


1 EqPRel1StmDmd(HP)

P(35)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(35)


1 EqPRel1StmDmd(MP)

P(36)

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(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(36)


1 EqPRel1StmDmd(LP)

P(37)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(37)

-1 EqPRel1StmDmd(HP)

P(38)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(38)

-1 EqPRel1StmDmd(LP)

P(39)

(.LO, .L, .UP, .M = 0.99, 1.01325, 1.1, 0)

1 Eq2AirStr(39)

1 EqInPGTCmpr(1)

P(40)

(.LO, .L, .UP, .M = 0.99, 20, 20, 0)

-1 EqOutPBlrCmbtr1(GT,40)

1 EqOutPGTCmpr(1)

P(41)

(.LO, .L, .UP, .M = 0.99, 20, 20, 0)

-1 EqOutPBlrCmbtr1(GT,41)

P(42)

(.LO, .L, .UP, .M = 0.99, 20, 20, 0)

1 EqOutPBlrCmbtr1(GT,40)

1 EqOutPBlrCmbtr1(GT,41)

1 EqInPGTExpdr(1)

P(43)

(.LO, .L, .UP, .M = 1.3, 1.3, 20, 0)

-1 EqOutPBlrCmbtr1(GTSF,43)

1 EqOutPGTExpdr(1)

P(44)

(.LO, .L, .UP, .M = 1.3, 1.3, 20, 0)

-1 EqOutPBlrCmbtr1(GTSF,44)

P(45)

(.LO, .L, .UP, .M = 1.3, 1.3, 20, 0)

1 EqOutPBlrCmbtr1(GTSF,43)

1 EqOutPBlrCmbtr1(GTSF,44)

1 EqRel4Blr(HRSG)

P(46)

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(.LO, .L, .UP, .M = 1.3, 1.3, 20, 0)

-1 EqRel4Blr(HRSG)

P(47)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(47)


-1 EqRel5Blr(HRSG)

-1 EqRel6Blr(HRSG)

P(48)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(48)


P(49)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(49)


P(50)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(50)


P(51)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(51)


P(52)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(52)

1 EqRel6Blr(MP)

P(53)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(53)

1 EqRel6Blr(HP)

P(54)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(54)

1 EqRel6Blr(HRSG)

P(55)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(55)

1 EqInMPPMPStmTurb(2)


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P(56)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(56)

1 EqOutLPPMPStmTurb(2)


P(57)

(.LO, .L, .UP, .M = 0.19, 0.2, 0.21, 0)

1 EqTSat(57)


P(58)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(58)



P(59)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(59)



P(60)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(60)



P(61)

(.LO, .L, .UP, .M = 0.19, 0.2, 0.21, 0)

1 EqTSat(61)


P(62)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

1 EqTSat(62)



P(63)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

1 EqTSat(63)



P(64)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

1 EqTSat(64)



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P(65)

(.LO, .L, .UP, .M = 0.19, 0.2, 0.21, 0)

1 EqTSat(65)


---- TrP2

TrP2(1)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(1)

(64.2852) EqLatHtVapP2(1,H2O)

TrP2(2)

(.LO, .L, .UP, .M = 0, 0.750372161879212, +INF, 0)

1 EqTrP2(2)


TrP2(3)

(.LO, .L, .UP, .M = 0, 0.677096793133225, +INF, 0)

1 EqTrP2(3)


TrP2(4)

(.LO, .L, .UP, .M = 0, 0.51484714175617, +INF, 0)

1 EqTrP2(4)


TrP2(5)

(.LO, .L, .UP, .M = 0, 0.750372161879212, +INF, 0)

1 EqTrP2(5)


TrP2(6)

(.LO, .L, .UP, .M = 0, 0.677096793133225, +INF, 0)

1 EqTrP2(6)


TrP2(7)

(.LO, .L, .UP, .M = 0, 0.514847141766765, +INF, 0)

1 EqTrP2(7)


TrP2(8)

(.LO, .L, .UP, .M = 0, 0.51484714175617, +INF, 0)

1 EqTrP2(8)


TrP2(10)

(.LO, .L, .UP, .M = 0, 0.750372161879212, +INF, 0)

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TrP2

1 EqTrP2(10)


TrP2(11)

(.LO, .L, .UP, .M = 0, 0.591035151959902, +INF, 0)

1 EqTrP2(11)


TrP2(12)

(.LO, .L, .UP, .M = 0, 0.677096793133225, +INF, 0)

1 EqTrP2(12)


TrP2(13)

(.LO, .L, .UP, .M = 0, 0.591035152175343, +INF, 0)

1 EqTrP2(13)


TrP2(14)

(.LO, .L, .UP, .M = 0, 0.591035151959903, +INF, 0)

1 EqTrP2(14)


TrP2(15)

(.LO, .L, .UP, .M = 0, 0.591035151959903, +INF, 0)

1 EqTrP2(15)


TrP2(25)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(25)


TrP2(26)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(26)


TrP2(31)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(31)


TrP2(32)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(32)


TrP2(33)

(.LO, .L, .UP, .M = 0, 0.677096793242886, +INF, 0)

1 EqTrP2(33)

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TrP2


TrP2(34)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(34)


TrP2(35)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(35)


TrP2(36)

(.LO, .L, .UP, .M = 0, 0.677096793133225, +INF, 0)

1 EqTrP2(36)


TrP2(37)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(37)


TrP2(38)

(.LO, .L, .UP, .M = 0, 0.677096793133224, +INF, 0)

1 EqTrP2(38)


TrP2(47)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(47)


TrP2(48)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(48)


TrP2(49)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(49)


TrP2(50)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(50)


TrP2(51)

(.LO, .L, .UP, .M = 0, 0.677096793242886, +INF, 0)

1 EqTrP2(51)


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TrP2

TrP2(52)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(52)


TrP2(53)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(53)


TrP2(54)

(.LO, .L, .UP, .M = 0, 0.819897177362015, +INF, 0)

1 EqTrP2(54)


TrP2(55)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(55)


TrP2(56)

(.LO, .L, .UP, .M = 0, 0.677096793242886, +INF, 0)

1 EqTrP2(56)


TrP2(57)

(.LO, .L, .UP, .M = 0, 0.51484714175617, +INF, 0)

1 EqTrP2(57)


TrP2(58)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(58)


TrP2(59)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(59)


TrP2(60)

(.LO, .L, .UP, .M = 0, 0.677096793242886, +INF, 0)

1 EqTrP2(60)


TrP2(61)

(.LO, .L, .UP, .M = 0, 0.51484714175617, +INF, 0)

1 EqTrP2(61)


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TrP2

TrP2(62)

(.LO, .L, .UP, .M = 0, 0.819897177362016, +INF, 0)

1 EqTrP2(62)


TrP2(63)

(.LO, .L, .UP, .M = 0, 0.750372161879215, +INF, 0)

1 EqTrP2(63)


TrP2(64)

(.LO, .L, .UP, .M = 0, 0.677096793242886, +INF, 0)

1 EqTrP2(64)


TrP2(65)

(.LO, .L, .UP, .M = 0, 0.514847141766765, +INF, 0)

1 EqTrP2(65)


---- LatHtVapP2

LatHtVapP2(1,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)

0.0003 EqEnthSatLiq(1)

1 EqLatHtVapP2(1,H2O)

LatHtVapP2(2,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010268, 50, 0)



LatHtVapP2(3,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752495816, 50, 0)



LatHtVapP2(4,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286060959, 50, 0)



LatHtVapP2(5,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010268, 50, 0)



LatHtVapP2(6,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752495816, 50, 0)


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LatHtVapP2


LatHtVapP2(7,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286058191, 50, 0)



LatHtVapP2(8,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286060959, 50, 0)



LatHtVapP2(10,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010268, 50, 0)




(0.5876) EqHtReqStmDmd(MP)

LatHtVapP2(11,H2O)

(.LO, .L, .UP, .M = 25, 40.354274163495, 50, 0)



LatHtVapP2(12,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752495816, 50, 0)



LatHtVapP2(13,H2O)

(.LO, .L, .UP, .M = 25, 40.3542741567203, 50, 0)



LatHtVapP2(14,H2O)

(.LO, .L, .UP, .M = 25, 40.354274163495, 50, 0)



LatHtVapP2(15,H2O)

(.LO, .L, .UP, .M = 25, 40.354274163495, 50, 0)



LatHtVapP2(25,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(26,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)

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LatHtVapP2



LatHtVapP2(31,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(32,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(33,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752452137, 50, 0)



LatHtVapP2(34,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(35,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(36,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752495816, 50, 0)



LatHtVapP2(37,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)




(0.1661) EqHtReqStmDmd(HP)

LatHtVapP2(38,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752495816, 50, 0)




(1.3402) EqHtReqStmDmd(LP)

LatHtVapP2(47,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



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LatHtVapP2

LatHtVapP2(48,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(49,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(50,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(51,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752452137, 50, 0)



LatHtVapP2(52,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(53,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(54,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(55,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(56,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752452137, 50, 0)



LatHtVapP2(57,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286060959, 50, 0)



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LatHtVapP2

LatHtVapP2(58,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(59,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(60,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752452137, 50, 0)



LatHtVapP2(61,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286060959, 50, 0)



LatHtVapP2(62,H2O)

(.LO, .L, .UP, .M = 25, 30.1020843953285, 50, 0)



LatHtVapP2(63,H2O)

(.LO, .L, .UP, .M = 25, 34.0392555010267, 50, 0)



LatHtVapP2(64,H2O)

(.LO, .L, .UP, .M = 25, 37.3087752452137, 50, 0)



LatHtVapP2(65,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286058191, 50, 0)



---- Wetns

Wetns(1)

(.LO, .L, .UP, .M = 0, 0, 1, 905.901588102403)

(0.01) EqEnthP2Str(1)

1 EqLogP21(1)

1 EqLogP22(1)

Wetns(2)

(.LO, .L, .UP, .M = 0, 0, 1, 0)

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Wetns


1 EqLogP21(2)

1 EqLogP22(2)

1 EqWetCnst1HPStmTurb(1)

1 EqLogMode6HPStmTurb(1)

Wetns(3)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(3)

1 EqLogP22(3)



Wetns(4)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(4)

1 EqLogP22(4)

1 EqPTRel3HPStmTurb(1)

Wetns(5)

(.LO, .L, .UP, .M = 0, 0, 1, 770.442149240164)


1 EqLogP21(5)

1 EqLogP22(5)

Wetns(6)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(6)

1 EqLogP22(6)

1 EqWetCnst1MPStmTurb(1)

1 EqLogMode4MPStmTurb(1)

Wetns(7)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(7)

1 EqLogP22(7)

1 EqPTRel2MPStmTurb(1)

Wetns(12)

(.LO, .L, .UP, .M = 0, 0.416370897536405, 1, 0)


1 EqLogP21(12)

1 EqLogP22(12)

Wetns(25)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)


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Wetns

1 EqLogP21(25)

1 EqLogP22(25)

Wetns(26)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)


1 EqLogP21(26)

1 EqLogP22(26)

Wetns(31)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(31)

1 EqLogP22(31)

Wetns(32)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(32)

1 EqLogP22(32)

Wetns(33)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(33)

1 EqLogP22(33)

Wetns(34)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(34)

1 EqLogP22(34)

Wetns(35)

(.LO, .L, .UP, .M = 0, 0, 1, 92.3928694835694)


1 EqLogP21(35)

1 EqLogP22(35)

Wetns(36)

(.LO, .L, .UP, .M = 0, 0.0001, 1, 0)


1 EqLogP21(36)

1 EqLogP22(36)

Wetns(47)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(47)

1 EqLogP22(47)

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Wetns

Wetns(48)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)


1 EqLogP21(48)

1 EqLogP22(48)

Wetns(49)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(49)

1 EqLogP22(49)

Wetns(50)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(50)

1 EqLogP22(50)

Wetns(51)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(51)

1 EqLogP22(51)

Wetns(55)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)


1 EqLogP21(55)

1 EqLogP22(55)

Wetns(56)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)


1 EqLogP21(56)

1 EqLogP22(56)

1 EqWetCnst1MPStmTurb(2)


Wetns(57)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(57)

1 EqLogP22(57)


Wetns(58)

(.LO, .L, .UP, .M = 0, 0, 1, 7485.11312650258)


1 EqLogP21(58)

1 EqLogP22(58)

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Wetns

Wetns(59)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(59)

1 EqLogP22(59)



Wetns(60)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(60)

1 EqLogP22(60)



Wetns(61)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(61)

1 EqLogP22(61)


Wetns(62)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)


1 EqLogP21(62)

1 EqLogP22(62)

Wetns(63)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(63)

1 EqLogP22(63)



Wetns(64)

(.LO, .L, .UP, .M = 0, 0, 1, 0)


1 EqLogP21(64)

1 EqLogP22(64)



Wetns(65)

(.LO, .L, .UP, .M = 0, 0.15, 1, 0)


1 EqLogP21(65)

1 EqLogP22(65)


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Wetns

---- TSat

TSat(1)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)

(-9.864288E-6) EqEnthSatLiq(1)

(-0.7398) EqTSat(1)

-1 EqTP2(1)

-1 EqLogP23(1)

-0.0015 EqTrP2(1)

TSat(2)

(.LO, .L, .UP, .M = 469, 485.588337116894, 526, 0)


(-0.3958) EqTSat(2)

-1 EqTP2(2)

-1 EqLogP23(2)

-0.0015 EqTrP2(2)

TSat(3)

(.LO, .L, .UP, .M = 414, 438.169647740304, 456, 0)


(-0.1735) EqTSat(3)

-1 EqTP2(3)

-1 EqLogP23(3)

-0.0015 EqTrP2(3)

TSat(4)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


(-0.0092) EqTSat(4)

-1 EqTP2(4)

-1 EqLogP23(4)

-0.0015 EqTrP2(4)

TSat(5)

(.LO, .L, .UP, .M = 469, 485.588337116894, 526, 0)


(-0.3958) EqTSat(5)

-1 EqTP2(5)

-1 EqLogP23(5)

-0.0015 EqTrP2(5)

TSat(6)

(.LO, .L, .UP, .M = 414, 438.169647740304, 456, 0)


(-0.1735) EqTSat(6)

-1 EqTP2(6)

-1 EqLogP23(6)

-0.0015 EqTrP2(6)

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TSat

TSat(7)

(.LO, .L, .UP, .M = 333, 333.173030851526, 334, 0)


(-0.0092) EqTSat(7)

-1 EqTP2(7)

-1 EqLogP23(7)

-0.0015 EqTrP2(7)

TSat(8)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


(-0.0092) EqTSat(8)

-0.0015 EqTrP2(8)

-1 EqnTfSatLiqVap(8)

TSat(10)

(.LO, .L, .UP, .M = 469, 485.588337116894, 526, 0)


(-0.3958) EqTSat(10)

-0.0015 EqTrP2(10)


TSat(11)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


(-0.0472) EqTSat(11)

-0.0015 EqTrP2(11)


TSat(12)

(.LO, .L, .UP, .M = 414, 438.169647740304, 456, 0)


(-0.1735) EqTSat(12)

-1 EqTP2(12)

-1 EqLogP23(12)

-0.0015 EqTrP2(12)

TSat(13)

(.LO, .L, .UP, .M = 382, 382.476578027229, 383, 0)


(-0.0472) EqTSat(13)

-0.0015 EqTrP2(13)


TSat(14)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


(-0.0472) EqTSat(14)

-0.0015 EqTrP2(14)


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TSat

TSat(15)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)


(-0.0472) EqTSat(15)

-0.0015 EqTrP2(15)


TSat(16)

(.LO, .L, .UP, .M = 382, 382.476577887812, 383, 0)

(-0.0472) EqTSat(16)


(-9.489659E-6) EqEnthSatVap(16)

TSat(25)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(25)

-1 EqTP2(25)

-1 EqLogP23(25)

-0.0015 EqTrP2(25)

TSat(26)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(26)

-1 EqTP2(26)

-1 EqLogP23(26)

-0.0015 EqTrP2(26)

TSat(31)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(31)

-1 EqTP2(31)

-1 EqLogP23(31)

-0.0015 EqTrP2(31)

TSat(32)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(32)

-1 EqTP2(32)

-1 EqLogP23(32)

-0.0015 EqTrP2(32)

TSat(33)

(.LO, .L, .UP, .M = 414, 438.169647811269, 456, 0)


(-0.1735) EqTSat(33)

-1 EqTP2(33)

model.lst Wed May 30 15:17:17 2018 263


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TSat

-1 EqLogP23(33)

-0.0015 EqTrP2(33)

TSat(34)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(34)

-1 EqTP2(34)

-1 EqLogP23(34)

-0.0015 EqTrP2(34)

TSat(35)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(35)

-1 EqTP2(35)

-1 EqLogP23(35)

-0.0015 EqTrP2(35)

TSat(36)

(.LO, .L, .UP, .M = 414, 438.169647740304, 456, 0)


(-0.1735) EqTSat(36)

-1 EqTP2(36)

-1 EqLogP23(36)

-0.0015 EqTrP2(36)

TSat(37)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(37)

-0.0015 EqTrP2(37)


TSat(38)

(.LO, .L, .UP, .M = 414, 438.169647740303, 456, 0)


(-0.1735) EqTSat(38)

-0.0015 EqTrP2(38)


TSat(47)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(47)

-1 EqTP2(47)

-1 EqLogP23(47)

-0.0015 EqTrP2(47)

TSat(48)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)

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TSat


(-0.7398) EqTSat(48)

-1 EqTP2(48)

-1 EqLogP23(48)

-0.0015 EqTrP2(48)

TSat(49)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(49)

-1 EqTP2(49)

-1 EqLogP23(49)

-0.0015 EqTrP2(49)

TSat(50)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(50)

-1 EqTP2(50)

-1 EqLogP23(50)

-0.0015 EqTrP2(50)

TSat(51)

(.LO, .L, .UP, .M = 414, 438.169647811269, 456, 0)


(-0.1735) EqTSat(51)

-1 EqTP2(51)

-1 EqLogP23(51)

-0.0015 EqTrP2(51)

TSat(52)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(52)

-0.0015 EqTrP2(52)


TSat(53)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(53)

-0.0015 EqTrP2(53)


TSat(54)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(54)

-0.0015 EqTrP2(54)


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TSat

TSat(55)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(55)

-1 EqTP2(55)

-1 EqLogP23(55)

-0.0015 EqTrP2(55)

TSat(56)

(.LO, .L, .UP, .M = 414, 438.169647811269, 456, 0)


(-0.1735) EqTSat(56)

-1 EqTP2(56)

-1 EqLogP23(56)

-0.0015 EqTrP2(56)

TSat(57)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


(-0.0092) EqTSat(57)

-1 EqTP2(57)

-1 EqLogP23(57)

-0.0015 EqTrP2(57)

TSat(58)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(58)

-1 EqTP2(58)

-1 EqLogP23(58)

-0.0015 EqTrP2(58)

TSat(59)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(59)

-1 EqTP2(59)

-1 EqLogP23(59)

-0.0015 EqTrP2(59)

TSat(60)

(.LO, .L, .UP, .M = 414, 438.169647811269, 456, 0)


(-0.1735) EqTSat(60)

-1 EqTP2(60)

-1 EqLogP23(60)

-0.0015 EqTrP2(60)

TSat(61)

(.LO, .L, .UP, .M = 333, 333.17303084467, 334, 0)


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TSat

(-0.0092) EqTSat(61)

-1 EqTP2(61)

-1 EqLogP23(61)

-0.0015 EqTrP2(61)

TSat(62)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)


(-0.7398) EqTSat(62)

-1 EqTP2(62)

-1 EqLogP23(62)

-0.0015 EqTrP2(62)

TSat(63)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)


(-0.3958) EqTSat(63)

-1 EqTP2(63)

-1 EqLogP23(63)

-0.0015 EqTrP2(63)

TSat(64)

(.LO, .L, .UP, .M = 414, 438.169647811269, 456, 0)


(-0.1735) EqTSat(64)

-1 EqTP2(64)

-1 EqLogP23(64)

-0.0015 EqTrP2(64)

TSat(65)

(.LO, .L, .UP, .M = 333, 333.173030851526, 334, 0)


(-0.0092) EqTSat(65)

-1 EqTP2(65)

-1 EqLogP23(65)

-0.0015 EqTrP2(65)

---- TrLiq

TrLiq(9)

(.LO, .L, .UP, .M = 0, 0.51484714175617, +INF, 0)

1 EqTrLiq(9)

(26.1225) EqLatHtVapLiq(9,H2O)

TrLiq(17)

(.LO, .L, .UP, .M = 0, 0.460726592802064, +INF, 0)

1 EqTrLiq(17)


TrLiq(18)

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TrLiq

(.LO, .L, .UP, .M = 0, 0.591035152175343, +INF, 0)

1 EqTrLiq(18)


TrLiq(19)

(.LO, .L, .UP, .M = 0, 0.591035151959903, +INF, 0)

1 EqTrLiq(19)


TrLiq(20)

(.LO, .L, .UP, .M = 0, 0.591035151959902, +INF, 0)

1 EqTrLiq(20)


---- LatHtVapLiq

LatHtVapLiq(9,H2O)

(.LO, .L, .UP, .M = 25, 42.5369286060959, 50, 0)

0.0003 EqEnthLiqStr(9)

1 EqLatHtVapLiq(9,H2O)

LatHtVapLiq(17,H2O)

(.LO, .L, .UP, .M = 25, 43.8694330427688, 50, 0)



LatHtVapLiq(18,H2O)

(.LO, .L, .UP, .M = 25, 40.3542741567203, 50, 0)



LatHtVapLiq(19,H2O)

(.LO, .L, .UP, .M = 25, 40.354274163495, 50, 0)



LatHtVapLiq(20,H2O)

(.LO, .L, .UP, .M = 25, 40.354274163495, 50, 0)



---- Y Binary variable

Y(1)

(.LO, .L, .UP, .M = 0, 1, 1, 0.001)

-701 EqPTRel1fHPStmTurb(1)

701 EqPTRel1gHPStmTurb(1)

-701 EqPTRel1hHPStmTurb(1)

701 EqPTRel1iHPStmTurb(1)

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Y Binary variable

701 EqPTRel1jHPStmTurb(1)

-701 EqPTRel1kHPStmTurb(1)

1 EqLogMode8HPStmTurb(1,MPBkPr)

1 EqLogMode8HPStmTurb(1,MPExt)

1 EqLogMode8HPStmTurb(1,LPBkPr)

1 EqLogMode8HPStmTurb(1,LPExt)

1 EqLogMode8HPStmTurb(1,VPCond)

-1.000000E+8 EqLogBnd4HPStmTurb(1,1)

-0.001 obj

Y(5)

(.LO, .L, .UP, .M = 0, 1, 1, 631.809837430946)

-581 EqPTRel1fMPStmTurb(1)

581 EqPTRel1gMPStmTurb(1)

-581 EqPTRel1hMPStmTurb(1)

581 EqPTRel1iMPStmTurb(1)

581 EqPTRel1jMPStmTurb(1)

-581 EqPTRel1kMPStmTurb(1)

1 EqLogMode5MPStmTurb(1,LPBkPr)

1 EqLogMode5MPStmTurb(1,LPExt)

1 EqLogMode5MPStmTurb(1,VPCond)

-1.000000E+8 EqLogBnd3MPStmTurb(1,5)

-0.001 obj

Y(55)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-581 EqPTRel1fMPStmTurb(2)


-581 EqPTRel1hMPStmTurb(2)



-581 EqPTRel1kMPStmTurb(2)

1 EqLogMode5MPStmTurb(2,LPBkPr)

1 EqLogMode5MPStmTurb(2,LPExt)

1 EqLogMode5MPStmTurb(2,VPCond)

-1.000000E+8 EqLogBnd3MPStmTurb(2,55)

-0.001 obj

Y(58)

(.LO, .L, .UP, .M = 0, 1, 1, 1972.31022380108)












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Y Binary variable


-0.001 obj

Y(62)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)













-0.001 obj

---- YP2 binary variable for 2 phase water streams

YP2(1)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(1)

-0.0001 EqLogP22(1)

500 EqLogP23(1)

-0.001 obj

YP2(2)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(2)

-0.0001 EqLogP22(2)

500 EqLogP23(2)

-0.001 obj

YP2(3)

(.LO, .L, .UP, .M = 0, 1, 1, 4451.54059996568)

-1 EqLogP21(3)

-0.0001 EqLogP22(3)

500 EqLogP23(3)

-0.001 obj

YP2(4)

(.LO, .L, .UP, .M = 1, 1, 1, 0.001)

-1 EqLogP21(4)

-0.0001 EqLogP22(4)

500 EqLogP23(4)

-0.001 obj

YP2(5)

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YP2 binary variable for 2 phase water streams

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(5)

-0.0001 EqLogP22(5)

500 EqLogP23(5)

-0.001 obj

YP2(6)

(.LO, .L, .UP, .M = 0, 1, 1, 364.867243264622)

-1 EqLogP21(6)

-0.0001 EqLogP22(6)

500 EqLogP23(6)

-0.001 obj

YP2(7)

(.LO, .L, .UP, .M = 1, 1, 1, 0.001)

-1 EqLogP21(7)

-0.0001 EqLogP22(7)

500 EqLogP23(7)

-0.001 obj

YP2(12)

(.LO, .L, .UP, .M = 0, 1, 1, 0.001)

-1 EqLogP21(12)

-0.0001 EqLogP22(12)

500 EqLogP23(12)

-0.001 obj

YP2(25)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(25)

-0.0001 EqLogP22(25)

500 EqLogP23(25)

-0.001 obj

YP2(26)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(26)

-0.0001 EqLogP22(26)

500 EqLogP23(26)

-0.001 obj

YP2(31)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(31)

-0.0001 EqLogP22(31)

500 EqLogP23(31)

-0.001 obj

YP2(32)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(32)

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-0.0001 EqLogP22(32)

500 EqLogP23(32)

-0.001 obj

YP2(33)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(33)

-0.0001 EqLogP22(33)

500 EqLogP23(33)

-0.001 obj

YP2(34)

(.LO, .L, .UP, .M = 0, 0, 0, -136.986286371361)

-1 EqLogP21(34)

-0.0001 EqLogP22(34)

500 EqLogP23(34)

-0.001 obj

YP2(35)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(35)

-0.0001 EqLogP22(35)

500 EqLogP23(35)

-0.001 obj

YP2(36)

(.LO, .L, .UP, .M = 0, 1, 1, 0.001)

-1 EqLogP21(36)

-0.0001 EqLogP22(36)

500 EqLogP23(36)

-0.001 obj

YP2(47)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(47)

-0.0001 EqLogP22(47)

500 EqLogP23(47)

-0.001 obj

YP2(48)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(48)

-0.0001 EqLogP22(48)

500 EqLogP23(48)

-0.001 obj

YP2(49)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(49)

-0.0001 EqLogP22(49)

500 EqLogP23(49)

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-0.001 obj

YP2(50)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(50)

-0.0001 EqLogP22(50)

500 EqLogP23(50)

-0.001 obj

YP2(51)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(51)

-0.0001 EqLogP22(51)

500 EqLogP23(51)

-0.001 obj

YP2(55)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(55)

-0.0001 EqLogP22(55)

500 EqLogP23(55)

-0.001 obj

YP2(56)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(56)

-0.0001 EqLogP22(56)

500 EqLogP23(56)

-0.001 obj

YP2(57)

(.LO, .L, .UP, .M = 1, 1, 1, 0.001)

-1 EqLogP21(57)

-0.0001 EqLogP22(57)

500 EqLogP23(57)

-0.001 obj

YP2(58)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(58)

-0.0001 EqLogP22(58)

500 EqLogP23(58)

-0.001 obj

YP2(59)

(.LO, .L, .UP, .M = 0, 0, 1, -2896.68326855543)

-1 EqLogP21(59)

-0.0001 EqLogP22(59)

500 EqLogP23(59)

-0.001 obj

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YP2(60)

(.LO, .L, .UP, .M = 0, 0, 1, -777.76838504849)

-1 EqLogP21(60)

-0.0001 EqLogP22(60)

500 EqLogP23(60)

-0.001 obj

YP2(61)

(.LO, .L, .UP, .M = 1, 1, 1, 0.001)

-1 EqLogP21(61)

-0.0001 EqLogP22(61)

500 EqLogP23(61)

-0.001 obj

YP2(62)

(.LO, .L, .UP, .M = 0, 0, 0, 0.001)

-1 EqLogP21(62)

-0.0001 EqLogP22(62)

500 EqLogP23(62)

-0.001 obj

YP2(63)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(63)

-0.0001 EqLogP22(63)

500 EqLogP23(63)

-0.001 obj

YP2(64)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogP21(64)

-0.0001 EqLogP22(64)

500 EqLogP23(64)

-0.001 obj

YP2(65)

(.LO, .L, .UP, .M = 1, 1, 1, 0.001)

-1 EqLogP21(65)

-0.0001 EqLogP22(65)

500 EqLogP23(65)

-0.001 obj

---- H Enthalpy of stream

H(1)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthP2Str(1)



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H Enthalpy of stream

H(2)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthP2Str(2)

(3639.7833) EqMPWorkHPStmTurb(1)


(0) EqEgyBalPLev(MP)

H(3)

(.LO, .L, .UP, .M = -0.09, -0.0673995157623354, 0, 0)

1 EqEnthP2Str(3)


(0) EqVPWorkHPStmTurb(1)


H(4)

(.LO, .L, .UP, .M = -0.09, -0.0686147825047606, 0, 0)

1 EqEnthP2Str(4)


(0) EqEnthBalVacCondTurb(1)

H(5)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthP2Str(5)



H(6)

(.LO, .L, .UP, .M = -0.09, -0.0673995157623354, 0, 0)

1 EqEnthP2Str(6)

(1766.1992) EqLPWorkMPStmTurb(1)

(0) EqVPWorkMPStmTurb(1)


H(7)

(.LO, .L, .UP, .M = -0.09, -0.0686147825046847, 0, 0)

1 EqEnthP2Str(7)



H(8)

(.LO, .L, .UP, .M = -0.09, -0.0786582239812, 0, 0)

1 EqEnthSatLiq1(8)


H(9)

(.LO, .L, .UP, .M = -0.09, -0.0786582239811999, 0, 0)

1 EqEnthLiqStr(9)


H(10)

(.LO, .L, .UP, .M = -0.09, -0.074841536139202, 0, 0)

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1 EqEnthSatLiq1(10)


H(11)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthSatLiq1(11)


H(12)

(.LO, .L, .UP, .M = -0.09, -0.0701600635260063, 0, 0)

1 EqEnthP2Str(12)



H(13)

(.LO, .L, .UP, .M = -0.09, -0.0775864176800003, 0, 0)

1 EqEnthSatLiq1(13)

(0) EqEnthBalDeAertr(1)

H(14)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthSatLiq1(14)

(0) EqEnthBalDeAertr(1)

H(15)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthSatLiq1(15)


H(16)

(.LO, .L, .UP, .M = -0.09, -0.0663768970822343, 0, 0)

1 EqEnthSatVap1(16)


H(17)

(.LO, .L, .UP, .M = -0.09, -0.0793565091785469, 0, 0)

1 EqEnthLiqStr(17)


H(18)

(.LO, .L, .UP, .M = -0.09, -0.0775864176800003, 0, 0)

1 EqEnthLiqStr(18)

(0) EqWtrEgyBalBlr(MP)

H(19)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthLiqStr(19)

(0) EqWtrEgyBalBlr(HP)

H(20)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

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1 EqEnthLiqStr(20)


H(25)

(.LO, .L, .UP, .M = -0.09, -0.0653861873889167, 0, 0)

1 EqEnthP2Str(25)



H(26)

(.LO, .L, .UP, .M = -0.09, -0.0649452630740801, 0, 0)

1 EqEnthP2Str(26)

(0) EqEgyBalPLev(HP)


H(31)

(.LO, .L, .UP, .M = -0.09, -0.0649452630740801, 0, 0)

1 EqEnthP2Str(31)


H(32)

(.LO, .L, .UP, .M = -0.09, -0.0653861873889167, 0, 0)

1 EqEnthP2Str(32)


H(33)

(.LO, .L, .UP, .M = -0.09, -0.0658449834595872, 0, 0)

1 EqEnthP2Str(33)

(0) EqEgyBalPLev(LP)

H(34)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthP2Str(34)


(598.025) EqEgyBalStmDmd(HP)

H(35)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthP2Str(35)


(2115.4164) EqEgyBalStmDmd(MP)

H(36)

(.LO, .L, .UP, .M = -0.09, -0.0658460198151376, 0, 0)

1 EqEnthP2Str(36)


(4825.0847) EqEgyBalStmDmd(LP)

H(37)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq1(37)

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H(38)

(.LO, .L, .UP, .M = -0.09, -0.0762085321407089, 0, 0)

1 EqEnthSatLiq1(38)


H(47)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthP2Str(47)



H(48)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthP2Str(48)


(0) EqEgyBalVlv(HPMP)

H(49)

(.LO, .L, .UP, .M = -0.09, -0.0653861873889167, 0, 0)

1 EqEnthP2Str(49)


(0) EqEgyBalVlv(HPMP)

H(50)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthP2Str(50)


(0) EqEgyBalVlv(MPLP)

H(51)

(.LO, .L, .UP, .M = -0.09, -0.0658449834595872, 0, 0)

1 EqEnthP2Str(51)


(0) EqEgyBalVlv(MPLP)

H(52)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq1(52)


H(53)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq1(53)


H(54)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838936, 0, 0)

1 EqEnthSatLiq1(54)


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H(55)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthP2Str(55)

(0) EqLPWorkMPStmTurb(2)


H(56)

(.LO, .L, .UP, .M = -0.09, -0.0656344842591389, 0, 0)

1 EqEnthP2Str(56)

(0) EqLPWorkMPStmTurb(2)



H(57)

(.LO, .L, .UP, .M = -0.09, -0.0686147825047606, 0, 0)

1 EqEnthP2Str(57)



H(58)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthP2Str(58)



H(59)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthP2Str(59)

(16385.9504) EqMPWorkHPStmTurb(2)



H(60)

(.LO, .L, .UP, .M = -0.09, -0.0658449834595872, 0, 0)

1 EqEnthP2Str(60)




H(61)

(.LO, .L, .UP, .M = -0.09, -0.0686147825047606, 0, 0)

1 EqEnthP2Str(61)


(-11138.8529) EqEnthBalVacCondTurb(1)

H(62)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthP2Str(62)

(0) EqMPWorkHPStmTurb(3)


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H(63)

(.LO, .L, .UP, .M = -0.09, -0.0649509844655109, 0, 0)

1 EqEnthP2Str(63)

(0) EqMPWorkHPStmTurb(3)

(0) EqLPWorkHPStmTurb(3)


H(64)

(.LO, .L, .UP, .M = -0.09, -0.0656344842591389, 0, 0)

1 EqEnthP2Str(64)

(0) EqLPWorkHPStmTurb(3)



H(65)

(.LO, .L, .UP, .M = -0.09, -0.0686147825046847, 0, 0)

1 EqEnthP2Str(65)



---- HVap

HVap(1)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthVapStr2(1)

(-1) EqEnthP2Str(1)

HVap(2)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthVapStr2(2)

(-1) EqEnthP2Str(2)

HVap(3)

(.LO, .L, .UP, .M = -0.09, -0.0658449834602695, 0, 0)

1 EqEnthVapStr2(3)

(-0.85) EqEnthP2Str(3)

HVap(4)

(.LO, .L, .UP, .M = -0.09, -0.0668424104795066, 0, 0)

1 EqEnthVapStr2(4)


HVap(5)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthVapStr2(5)

(-1) EqEnthP2Str(5)

HVap(6)

(.LO, .L, .UP, .M = -0.09, -0.0658449834602695, 0, 0)

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HVap

1 EqEnthVapStr2(6)


HVap(7)

(.LO, .L, .UP, .M = -0.09, -0.0668424104794422, 0, 0)

1 EqEnthVapStr2(7)


HVap(12)

(.LO, .L, .UP, .M = -0.09, -0.0658449834602695, 0, 0)

1 EqEnthVapStr2(12)


HVap(25)

(.LO, .L, .UP, .M = -0.09, -0.0653861873889167, 0, 0)

1 EqEnthVapStr2(25)

(-1) EqEnthP2Str(25)

HVap(26)

(.LO, .L, .UP, .M = -0.09, -0.0649452630740801, 0, 0)

1 EqEnthVapStr2(26)


HVap(31)

(.LO, .L, .UP, .M = -0.09, -0.0649452630740801, 0, 0)

1 EqEnthVapStr2(31)


HVap(32)

(.LO, .L, .UP, .M = -0.09, -0.0653861873889167, 0, 0)

1 EqEnthVapStr2(32)


HVap(33)

(.LO, .L, .UP, .M = -0.09, -0.0658449834595872, 0, 0)

1 EqEnthVapStr2(33)


HVap(34)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthVapStr2(34)


HVap(35)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthVapStr2(35)


HVap(36)

(.LO, .L, .UP, .M = -0.09, -0.0658449834602695, 0, 0)

1 EqEnthVapStr2(36)

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HVap


HVap(47)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthVapStr2(47)


HVap(48)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthVapStr2(48)


HVap(49)

(.LO, .L, .UP, .M = -0.09, -0.0653861873889167, 0, 0)

1 EqEnthVapStr2(49)


HVap(50)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthVapStr2(50)


HVap(51)

(.LO, .L, .UP, .M = -0.09, -0.0658449834595872, 0, 0)

1 EqEnthVapStr2(51)


HVap(55)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthVapStr2(55)


HVap(56)

(.LO, .L, .UP, .M = -0.09, -0.0656344842591389, 0, 0)

1 EqEnthVapStr2(56)


HVap(57)

(.LO, .L, .UP, .M = -0.09, -0.0668424104795066, 0, 0)

1 EqEnthVapStr2(57)


HVap(58)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthVapStr2(58)


HVap(59)

(.LO, .L, .UP, .M = -0.09, -0.0645685780167178, 0, 0)

1 EqEnthVapStr2(59)


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HVap

HVap(60)

(.LO, .L, .UP, .M = -0.09, -0.0658449834595872, 0, 0)

1 EqEnthVapStr2(60)


HVap(61)

(.LO, .L, .UP, .M = -0.09, -0.0668424104795066, 0, 0)

1 EqEnthVapStr2(61)


HVap(62)

(.LO, .L, .UP, .M = -0.09, -0.0632783912521576, 0, 0)

1 EqEnthVapStr2(62)


HVap(63)

(.LO, .L, .UP, .M = -0.09, -0.0649509844655109, 0, 0)

1 EqEnthVapStr2(63)


HVap(64)

(.LO, .L, .UP, .M = -0.09, -0.0656344842591389, 0, 0)

1 EqEnthVapStr2(64)


HVap(65)

(.LO, .L, .UP, .M = -0.09, -0.0668424104794422, 0, 0)

1 EqEnthVapStr2(65)


---- HSatLiq

HSatLiq(1)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(1)

(0) EqEnthP2Str(1)

HSatLiq(2)

(.LO, .L, .UP, .M = -0.09, -0.074841536139202, 0, 0)

1 EqEnthSatLiq(2)

(0) EqEnthP2Str(2)

HSatLiq(3)

(.LO, .L, .UP, .M = -0.09, -0.0762085321407089, 0, 0)

1 EqEnthSatLiq(3)


HSatLiq(4)

(.LO, .L, .UP, .M = -0.09, -0.0786582239812, 0, 0)

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HSatLiq

1 EqEnthSatLiq(4)


HSatLiq(5)

(.LO, .L, .UP, .M = -0.09, -0.074841536139202, 0, 0)

1 EqEnthSatLiq(5)

(0) EqEnthP2Str(5)

HSatLiq(6)

(.LO, .L, .UP, .M = -0.09, -0.0762085321407089, 0, 0)

1 EqEnthSatLiq(6)


HSatLiq(7)

(.LO, .L, .UP, .M = -0.09, -0.0786582239810586, 0, 0)

1 EqEnthSatLiq(7)


HSatLiq(8)

(.LO, .L, .UP, .M = -0.09, -0.0786582239812, 0, 0)

1 EqEnthSatLiq(8)

-1 EqEnthSatLiq1(8)

HSatLiq(10)

(.LO, .L, .UP, .M = -0.09, -0.074841536139202, 0, 0)

1 EqEnthSatLiq(10)

-1 EqEnthSatLiq1(10)

HSatLiq(11)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthSatLiq(11)


HSatLiq(12)

(.LO, .L, .UP, .M = -0.09, -0.0762085321407089, 0, 0)

1 EqEnthSatLiq(12)


HSatLiq(13)

(.LO, .L, .UP, .M = -0.09, -0.0775864176800003, 0, 0)

1 EqEnthSatLiq(13)


HSatLiq(14)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthSatLiq(14)


HSatLiq(15)

(.LO, .L, .UP, .M = -0.09, -0.0775864176832051, 0, 0)

1 EqEnthSatLiq(15)

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HSatLiq


HSatLiq(25)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(25)

(0) EqEnthP2Str(25)

HSatLiq(26)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(26)

(0) EqEnthP2Str(26)

HSatLiq(31)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(31)

(0) EqEnthP2Str(31)

HSatLiq(32)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(32)

(0) EqEnthP2Str(32)

HSatLiq(33)

(.LO, .L, .UP, .M = -0.09, -0.0762085321388132, 0, 0)

1 EqEnthSatLiq(33)

(0) EqEnthP2Str(33)

HSatLiq(34)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(34)

(0) EqEnthP2Str(34)

HSatLiq(35)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(35)

(0) EqEnthP2Str(35)

HSatLiq(36)

(.LO, .L, .UP, .M = -0.09, -0.0762085321407089, 0, 0)

1 EqEnthSatLiq(36)


HSatLiq(37)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(37)


HSatLiq(38)

(.LO, .L, .UP, .M = -0.09, -0.0762085321407089, 0, 0)

1 EqEnthSatLiq(38)


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HSatLiq

HSatLiq(47)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(47)

(0) EqEnthP2Str(47)

HSatLiq(48)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(48)

(0) EqEnthP2Str(48)

HSatLiq(49)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(49)

(0) EqEnthP2Str(49)

HSatLiq(50)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(50)

(0) EqEnthP2Str(50)

HSatLiq(51)

(.LO, .L, .UP, .M = -0.09, -0.0762085321388132, 0, 0)

1 EqEnthSatLiq(51)

(0) EqEnthP2Str(51)

HSatLiq(52)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(52)


HSatLiq(53)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(53)


HSatLiq(54)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838936, 0, 0)

1 EqEnthSatLiq(54)


HSatLiq(55)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(55)

(0) EqEnthP2Str(55)

HSatLiq(56)

(.LO, .L, .UP, .M = -0.09, -0.0762085321388132, 0, 0)

1 EqEnthSatLiq(56)

(0) EqEnthP2Str(56)

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HSatLiq

HSatLiq(57)

(.LO, .L, .UP, .M = -0.09, -0.0786582239811999, 0, 0)

1 EqEnthSatLiq(57)


HSatLiq(58)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(58)

(0) EqEnthP2Str(58)

HSatLiq(59)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(59)

(0) EqEnthP2Str(59)

HSatLiq(60)

(.LO, .L, .UP, .M = -0.09, -0.0762085321388132, 0, 0)

1 EqEnthSatLiq(60)

(0) EqEnthP2Str(60)

HSatLiq(61)

(.LO, .L, .UP, .M = -0.09, -0.0786582239811999, 0, 0)

1 EqEnthSatLiq(61)


HSatLiq(62)

(.LO, .L, .UP, .M = -0.09, -0.0733069531838935, 0, 0)

1 EqEnthSatLiq(62)

(0) EqEnthP2Str(62)

HSatLiq(63)

(.LO, .L, .UP, .M = -0.09, -0.0748415361392019, 0, 0)

1 EqEnthSatLiq(63)

(0) EqEnthP2Str(63)

HSatLiq(64)

(.LO, .L, .UP, .M = -0.09, -0.0762085321388132, 0, 0)

1 EqEnthSatLiq(64)

(0) EqEnthP2Str(64)

HSatLiq(65)

(.LO, .L, .UP, .M = -0.09, -0.0786582239810586, 0, 0)

1 EqEnthSatLiq(65)


---- HSatVap

HSatVap(16)

(.LO, .L, .UP, .M = -0.09, -0.0663768970822343, 0, 0)

1 EqEnthSatVap(16)

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HSatVap

-1 EqEnthSatVap1(16)

---- Hc

Hc(21,H2)

(.LO, .L, .UP, .M = -0.001, 0.00196192420252093, 0.011, 0)

1 EqEnthpyGasStr1(21,H2)


(0) EqGasEgyBalBlr(HP)

Hc(21,O2)

(.LO, .L, .UP, .M = -0.001, 0.00204533880433055, 0.012, 0)

1 EqEnthpyGasStr1(21,O2)



Hc(21,N2)

(.LO, .L, .UP, .M = -0.001, 0.0019792817775278, 0.012, 0)

1 EqEnthpyGasStr1(21,N2)



Hc(21,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0178721026759565, 0.0026, 0)

1 EqEnthpyGasStr1(21,CH4)



Hc(21,CO)

(.LO, .L, .UP, .M = -0.032, -0.0287148794735374, -0.0193, 0)

1 EqEnthpyGasStr1(21,CO)



Hc(21,CO2)

(.LO, .L, .UP, .M = -0.11, -0.106513160723588, -0.0913, 0)

1 EqEnthpyGasStr1(21,CO2)



Hc(21,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0648464734303417, -0.053, 0)

1 EqEnthpyGasStr1(21,H2O)



Hc(22,H2)

(.LO, .L, .UP, .M = -0.001, 0.000763461498861121, 0.011, 0)



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Hc

Hc(22,O2)

(.LO, .L, .UP, .M = -0.001, 0.000784212267803189, 0.012, 0)



Hc(22,N2)

(.LO, .L, .UP, .M = -0.001, 0.000767960009045014, 0.012, 0)



Hc(22,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0196919561496707, 0.0026, 0)



Hc(22,CO)

(.LO, .L, .UP, .M = -0.032, -0.0299333471445078, -0.0193, 0)



Hc(22,CO2)

(.LO, .L, .UP, .M = -0.11, -0.108281327671871, -0.0913, 0)



Hc(22,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0662769175797148, -0.053, 0)



Hc(23,H2)

(.LO, .L, .UP, .M = -0.001, 0.00159574278372965, 0.011, 0)



(0) EqGasEgyBalBlr(MP)

Hc(23,O2)

(.LO, .L, .UP, .M = -0.001, 0.00165505241110473, 0.012, 0)




Hc(23,N2)

(.LO, .L, .UP, .M = -0.001, 0.00160730410628413, 0.012, 0)




Hc(23,CH4)

(.LO, .L, .UP, .M = -0.022, -0.018462681064419, 0.0026, 0)

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Hc




Hc(23,CO)

(.LO, .L, .UP, .M = -0.032, -0.0290897239253213, -0.0193, 0)




Hc(23,CO2)

(.LO, .L, .UP, .M = -0.11, -0.107072466036317, -0.0913, 0)




Hc(23,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0652886755962375, -0.053, 0)




Hc(24,H2)

(.LO, .L, .UP, .M = -0.001, 0.000759228542169931, 0.011, 0)



Hc(24,O2)

(.LO, .L, .UP, .M = -0.001, 0.000779833439508448, 0.012, 0)



Hc(24,N2)

(.LO, .L, .UP, .M = -0.001, 0.000763704300320578, 0.012, 0)



Hc(24,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0196978342919161, 0.0026, 0)



Hc(24,CO)

(.LO, .L, .UP, .M = -0.032, -0.0299376169786605, -0.0193, 0)



Hc(24,CO2)

(.LO, .L, .UP, .M = -0.11, -0.108287243349511, -0.0913, 0)



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Hc

Hc(24,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0662818959725452, -0.053, 0)



Hc(27,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)



Hc(27,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(27,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(27,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)



Hc(27,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)



Hc(27,CO2)

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)



Hc(27,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)



Hc(28,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)



Hc(28,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



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Hc

Hc(28,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(28,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)



Hc(28,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)



Hc(28,CO2)

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)



Hc(28,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)



Hc(29,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)



Hc(29,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(29,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(29,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)



Hc(29,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)



Hc(29,CO2)

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Hc

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)



Hc(29,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)



Hc(30,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)



Hc(30,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(30,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(30,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)



Hc(30,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)



Hc(30,CO2)

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)



Hc(30,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)



Hc(39,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)


(0) EqWorkGTCmpr(1)

Hc(39,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)

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Hc



Hc(39,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(39,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)


(0) EqWorkGTCmpr(1)

Hc(39,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)


(0) EqWorkGTCmpr(1)

Hc(39,CO2)

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)


(0) EqWorkGTCmpr(1)

Hc(39,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)


(0) EqWorkGTCmpr(1)

Hc(40,H2)

(.LO, .L, .UP, .M = -0.001, 0.00264965602091713, 0.011, 0)



(0) EqWorkGTCmpr(1)

Hc(40,O2)

(.LO, .L, .UP, .M = -0.001, 0.00279122781038525, 0.012, 0)




Hc(40,N2)

(.LO, .L, .UP, .M = -0.001, 0.0026842386842132, 0.012, 0)




Hc(40,CH4)

(.LO, .L, .UP, .M = -0.022, -0.016675949084017, 0.0026, 0)



(0) EqWorkGTCmpr(1)

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Hc

Hc(40,CO)

(.LO, .L, .UP, .M = -0.032, -0.0280029454734525, -0.0193, 0)



(0) EqWorkGTCmpr(1)

Hc(40,CO2)

(.LO, .L, .UP, .M = -0.11, -0.105421752109749, -0.0913, 0)



(0) EqWorkGTCmpr(1)

Hc(40,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0640010568196236, -0.053, 0)



(0) EqWorkGTCmpr(1)

Hc(41,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)



Hc(41,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(41,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(41,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)



Hc(41,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)



Hc(41,CO2)

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)



Hc(41,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)

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Hc



Hc(42,H2)

(.LO, .L, .UP, .M = -0.001, 0.0100794789383741, 0.011, 0)



(0) EqWorkGTExpdr(1)

Hc(42,O2)

(.LO, .L, .UP, .M = -0.001, 0.0112775227252278, 0.012, 0)




Hc(42,N2)

(.LO, .L, .UP, .M = -0.001, 0.0106703509663167, 0.012, 0)




Hc(42,CH4)

(.LO, .L, .UP, .M = -0.022, 0.00132189024000543, 0.0026, 0)




Hc(42,CO)

(.LO, .L, .UP, .M = -0.032, -0.0199094246120686, -0.0193, 0)




Hc(42,CO2)

(.LO, .L, .UP, .M = -0.11, -0.0921940581391073, -0.0913, 0)




Hc(42,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0537956073668386, -0.053, 0)




Hc(43,H2)

(.LO, .L, .UP, .M = -0.001, 0.00376527481036826, 0.011, 0)




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Hc

Hc(43,O2)

(.LO, .L, .UP, .M = -0.001, 0.00403508431008718, 0.012, 0)




Hc(43,N2)

(.LO, .L, .UP, .M = -0.001, 0.00384782458318875, 0.012, 0)




Hc(43,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0144963214618929, 0.0026, 0)




Hc(43,CO)

(.LO, .L, .UP, .M = -0.032, -0.0268242574641663, -0.0193, 0)




Hc(43,CO2)

(.LO, .L, .UP, .M = -0.11, -0.103554934344382, -0.0913, 0)




Hc(43,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0625847155763706, -0.053, 0)




Hc(44,H2)

(.LO, .L, .UP, .M = -0.001, 0, 0.011, 0)



Hc(44,O2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



Hc(44,N2)

(.LO, .L, .UP, .M = -0.001, 0, 0.012, 0)



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Hc

Hc(44,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0207, 0.0026, 0)



Hc(44,CO)

(.LO, .L, .UP, .M = -0.032, -0.0307027777777778, -0.0193, 0)



Hc(44,CO2)

(.LO, .L, .UP, .M = -0.11, -0.109308333333333, -0.0913, 0)



Hc(44,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0671705555555556, -0.053, 0)



Hc(45,H2)

(.LO, .L, .UP, .M = -0.001, 0.00376527481036826, 0.011, 0)



(0) EqGasEgyBalBlr(HRSG)

Hc(45,O2)

(.LO, .L, .UP, .M = -0.001, 0.00403508431008718, 0.012, 0)




Hc(45,N2)

(.LO, .L, .UP, .M = -0.001, 0.00384782458318875, 0.012, 0)




Hc(45,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0144963214618929, 0.0026, 0)




Hc(45,CO)

(.LO, .L, .UP, .M = -0.032, -0.0268242574641663, -0.0193, 0)




Hc(45,CO2)

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Hc

(.LO, .L, .UP, .M = -0.11, -0.103554934344382, -0.0913, 0)




Hc(45,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0625847155763706, -0.053, 0)




Hc(46,H2)

(.LO, .L, .UP, .M = -0.001, 0.000759228541042472, 0.011, 0)



Hc(46,O2)

(.LO, .L, .UP, .M = -0.001, 0.000779833438342193, 0.012, 0)



Hc(46,N2)

(.LO, .L, .UP, .M = -0.001, 0.000763704299187067, 0.012, 0)



Hc(46,CH4)

(.LO, .L, .UP, .M = -0.022, -0.0196978342934813, 0.0026, 0)



Hc(46,CO)

(.LO, .L, .UP, .M = -0.032, -0.0299376169797978, -0.0193, 0)



Hc(46,CO2)

(.LO, .L, .UP, .M = -0.11, -0.108287243351087, -0.0913, 0)



Hc(46,H2O)

(.LO, .L, .UP, .M = -0.068, -0.0662818959738712, -0.053, 0)



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---- InHPPHPStmTurb Inlet HP Pressure for expander of HP Steam turbine

InHPPHPStmTurb(1)

(.LO, .L, .UP, .M = 45, 45, 80, 0)

-1 EqInHPPHPStmTurb(1)

(3.1349) EqPTRel1HPStmTurb(1)

InHPPHPStmTurb(2)

(.LO, .L, .UP, .M = 45, 45, 80, 0)



InHPPHPStmTurb(3)

(.LO, .L, .UP, .M = 45, 45, 80, 0)



---- InHPTHPStmTurb Inlet HP Temperature for expander of HP Steam turbine

InHPTHPStmTurb(1)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)

-1 EqInHPTHPStmTurb(1)

(-0.8177) EqPTRel1HPStmTurb(1)

InHPTHPStmTurb(2)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)



InHPTHPStmTurb(3)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)



---- OutMPPHPStmTurb Outlet MP Pressure for expander of HP Steam turbine

OutMPPHPStmTurb(1)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

-1 EqOutMPPHPStmTurb(1)



OutMPPHPStmTurb(2)

(.LO, .L, .UP, .M = 15, 20, 40, 0)




OutMPPHPStmTurb(3)

(.LO, .L, .UP, .M = 15, 20, 40, 0)


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OutMPPHPStmTurb Outlet MP Pressure for expander of HP Steam turbine



---- OutLPPHPStmTurb Outlet LP Pressure for expander of HP Steam turbine

OutLPPHPStmTurb(1)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

-1 EqOutLPPHPStmTurb(1)


OutLPPHPStmTurb(2)

(.LO, .L, .UP, .M = 4, 7, 10, 0)



OutLPPHPStmTurb(3)

(.LO, .L, .UP, .M = 4, 7, 10, 0)



---- OutMPTHPStmTurb Outlet MP Temperature for expander of HP Steam turbine

OutMPTHPStmTurb(1)

(.LO, .L, .UP, .M = 273, 568.549477042195, 701, 0)


1 EqPTRel1aHPStmTurb(1)


OutMPTHPStmTurb(2)

(.LO, .L, .UP, .M = 273, 568.549477042195, 701, 0)




OutMPTHPStmTurb(3)

(.LO, .L, .UP, .M = 273, 568.549477042195, 701, 0)




---- OutLPTHPStmTurb Outlet LP Temperature for expander of HP Steam turbine

OutLPTHPStmTurb(1)

(.LO, .L, .UP, .M = 273, 438.169647740304, 581, 0)



OutLPTHPStmTurb(2)

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OutLPTHPStmTurb Outlet LP Temperature for expander of HP Steam turbine

(.LO, .L, .UP, .M = 273, 438.169647740304, 581, 0)



OutLPTHPStmTurb(3)

(.LO, .L, .UP, .M = 273, 438.169647740304, 581, 0)



---- MPWorkHPStmTurb MP expnasion work of HP Steam turbine

MPWorkHPStmTurb(1)

(.LO, .L, .UP, .M = 0, 4.69600018650443, +INF, 0)

1 EqMPWorkHPStmTurb(1)

-1 EqTotWorkHPStmTurb(1)

MPWorkHPStmTurb(2)

(.LO, .L, .UP, .M = 0, 21.1409362668376, +INF, 0)



MPWorkHPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



---- LPWorkHPStmTurb LP expnasion work of HP Steam turbine

LPWorkHPStmTurb(1)

(.LO, .L, .UP, .M = 0, 10.3039998134956, +INF, 0)

1 EqLPWorkHPStmTurb(1)


LPWorkHPStmTurb(2)

(.LO, .L, .UP, .M = 0, 15.9606008744675, +INF, 0)



LPWorkHPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



---- VPWorkHPStmTurb VP expnasion work of HP Steam turbine

VPWorkHPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqVPWorkHPStmTurb(1)

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VPWorkHPStmTurb VP expnasion work of HP Steam turbine


VPWorkHPStmTurb(2)

(.LO, .L, .UP, .M = 0, 30.8523841626758, +INF, 0)



VPWorkHPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



---- TotWorkHPStmTurb Total work of HP Steam turbine

TotWorkHPStmTurb(1)

(.LO, .L, .UP, .M = 0, 15, +INF, 0)

1 EqTotWorkHPStmTurb(1)

1 Eqstpd7(1)

TotWorkHPStmTurb(2)

(.LO, .L, .UP, .M = 0, 67.953921303981, +INF, 0)


1 Eqstpd7(2)

TotWorkHPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 Eqstpd7(3)

---- Dum1HPStmTurb

Dum1HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)

-1 EqPTRel2aHPStmTurb(1)

-1 EqPTRel2dHPStmTurb(1)

1 EqPTRel2hHPStmTurb(1)

Dum1HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)




Dum1HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, EPS)




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---- Dum2HPStmTurb

Dum2HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



Dum2HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, EPS)



Dum2HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)



---- Dum3HPStmTurb

Dum3HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 460, +INF, 0)

-1 EqPTRel2bHPStmTurb(1)

1 EqPTRel2kHPStmTurb(1)

Dum3HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 459.999999929035, +INF, 0)



Dum3HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, EPS)



---- Dum4HPStmTurb

Dum4HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 9.92134148318586)


-1 EqPTRel2eHPStmTurb(1)


Dum4HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 7.09649725649797E-8, +INF, 0)




Dum4HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 460, +INF, 0)


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Dum4HPStmTurb



---- Dum5HPStmTurb

Dum5HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)

-1 EqPTRel2cHPStmTurb(1)

1 EqPTRel2dHPStmTurb(1)

1 EqPTRel2fHPStmTurb(1)

Dum5HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)




Dum5HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)




---- Dum6HPStmTurb

Dum6HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqPTRel2eHPStmTurb(1)


Dum6HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 7.09649725649797E-8, +INF, 0)




Dum6HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 460, +INF, 0)




---- Dum11HPStmTurb

Dum11HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 568.549477042195, +INF, 0)


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Dum11HPStmTurb



Dum11HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 568.549477042195, +INF, 0)




Dum11HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)




---- Dum22HPStmTurb

Dum22HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



Dum22HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



Dum22HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 568.549477042195, +INF, 0)



---- Dum33HPStmTurb

Dum33HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 530, +INF, 0)



Dum33HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 530, +INF, 0)



Dum33HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



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---- Dum44HPStmTurb

Dum44HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)




Dum44HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 2.81356522653506)




Dum44HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 530, +INF, 0)




---- Dum55HPStmTurb

Dum55HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 568.549477042195, +INF, 0)




Dum55HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 568.549477042195, +INF, 0)




Dum55HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 0, +INF, EPS)




---- Dum66HPStmTurb

Dum66HPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, EPS)




Dum66HPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


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Dum66HPStmTurb



Dum66HPStmTurb(3)

(.LO, .L, .UP, .M = 0, 530, +INF, 0)




---- YModeHPStmTurb

YModeHPStmTurb(1,MPBkPr)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)



-1 EqLogMode8HPStmTurb(1,MPBkPr)

-1.000000E+8 EqLogBnd1HPStmTurb(1)

-0.001 obj

YModeHPStmTurb(1,MPExt)

(.LO, .L, .UP, .M = 0, 1, 1, 0.001)

-1 EqLogMode1HPStmTurb(1)



-1 EqLogMode8HPStmTurb(1,MPExt)


-0.001 obj

YModeHPStmTurb(1,LPBkPr)

(.LO, .L, .UP, .M = 0, 1, 1, 0.001)

-1 EqPTRel2mHPStmTurb(1)




-1 EqLogMode8HPStmTurb(1,LPBkPr)


-0.001 obj

YModeHPStmTurb(1,LPExt)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqPTRel2lHPStmTurb(1)




-1 EqLogMode8HPStmTurb(1,LPExt)


-0.001 obj

YModeHPStmTurb(1,VPCond)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

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YModeHPStmTurb

-1 EqPTRel2nHPStmTurb(1)




-1 EqLogMode8HPStmTurb(1,VPCond)


-0.001 obj


(.LO, .L, .UP, .M = 0, 0, 1, EPS)






(.LO, .L, .UP, .M = 0, 1, 1, EPS)







(.LO, .L, .UP, .M = 0, 0, 1, EPS)








(.LO, .L, .UP, .M = 0, 1, 1, EPS)








(.LO, .L, .UP, .M = 0, 1, 1, EPS)








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YModeHPStmTurb

(.LO, .L, .UP, .M = 0, 0, 1, -5351869.78335683)






(.LO, .L, .UP, .M = 0, 0, 1, -5351869.78335683)







(.LO, .L, .UP, .M = 0, 0, 1, EPS)








(.LO, .L, .UP, .M = 0, 0, 1, EPS)








(.LO, .L, .UP, .M = 0, 0, 1, EPS)







---- YLP

YLP(1)

(.LO, .L, .UP, .M = 0, 1, 1, 5764.29940173099)






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YLP


1 EqPTRel2lHPStmTurb(1)

1 EqPTRel2mHPStmTurb(1)

1 EqPTRel2nHPStmTurb(1)

YLP(2)

(.LO, .L, .UP, .M = 0, 1, 1, EPS)










YLP(3)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)










---- InMPPMPStmTurb Inlet MP Pressure for expander of MP Steam turbine

InMPPMPStmTurb(1)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

-1 EqInMPPMPStmTurb(1)

(5.4359) EqPTRel1MPStmTurb(1)

InMPPMPStmTurb(2)

(.LO, .L, .UP, .M = 15, 20, 40, 0)

-1 EqInMPPMPStmTurb(2)

(5.4359) EqPTRel1MPStmTurb(2)

---- InMPTMPStmTurb Inlet MP Temperature for expander of MP Steam turbine

InMPTMPStmTurb(1)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)

-1 EqInMPTMPStmTurb(1)

(-0.7707) EqPTRel1MPStmTurb(1)

InMPTMPStmTurb(2)

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InMPTMPStmTurb Inlet MP Temperature for expander of MP Steam turbine

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)

-1 EqInMPTMPStmTurb(2)


---- OutLPPMPStmTurb Outlet LP Pressure for expander of MP Steam turbine

OutLPPMPStmTurb(1)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

-1 EqOutLPPMPStmTurb(1)


OutLPPMPStmTurb(2)

(.LO, .L, .UP, .M = 4, 7, 10, 0)

-1 EqOutLPPMPStmTurb(2)


---- OutLPTMPStmTurb Outlet LP Temperature for expander of HP Steam turbine

OutLPTMPStmTurb(1)

(.LO, .L, .UP, .M = 273, 438.169647740304, 581, 0)


1 EqPTRel1aMPStmTurb(1)

OutLPTMPStmTurb(2)

(.LO, .L, .UP, .M = 273, 438.169647740304, 581, 0)


1 EqPTRel1aMPStmTurb(2)

---- LPWorkMPStmTurb LP expnasion work of MP Steam turbine

LPWorkMPStmTurb(1)

(.LO, .L, .UP, .M = 0, 5, +INF, 0)

1 EqLPWorkMPStmTurb(1)

-1 EqTotWorkMPStmTurb(1)

LPWorkMPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqLPWorkMPStmTurb(2)


---- VPWorkMPStmTurb VP expnasion work of HP Steam turbine

VPWorkMPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqVPWorkMPStmTurb(1)


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VPWorkMPStmTurb VP expnasion work of HP Steam turbine

VPWorkMPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqVPWorkMPStmTurb(2)


---- TotWorkMPStmTurb Total work of HP Steam turbine

TotWorkMPStmTurb(1)

(.LO, .L, .UP, .M = 0, 5, +INF, 0)

1 EqTotWorkMPStmTurb(1)

1 Eqstpd8(1)

TotWorkMPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqTotWorkMPStmTurb(2)

1 Eqstpd8(2)

---- Dum11MPStmTurb

Dum11MPStmTurb(1)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)

-1 EqPTRel1aMPStmTurb(1)

-1 EqPTRel1dMPStmTurb(1)

1 EqPTRel1hMPStmTurb(1)

Dum11MPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


-1 EqPTRel1dMPStmTurb(2)

1 EqPTRel1hMPStmTurb(2)

---- Dum22MPStmTurb

Dum22MPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)



Dum22MPStmTurb(2)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)



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---- Dum33MPStmTurb

Dum33MPStmTurb(1)

(.LO, .L, .UP, .M = 0, 460, +INF, 0)

-1 EqPTRel1bMPStmTurb(1)

1 EqPTRel1kMPStmTurb(1)

Dum33MPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqPTRel1kMPStmTurb(2)

---- Dum44MPStmTurb

Dum44MPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


-1 EqPTRel1eMPStmTurb(1)


Dum44MPStmTurb(2)

(.LO, .L, .UP, .M = 0, 460, +INF, 0)


-1 EqPTRel1eMPStmTurb(2)


---- Dum55MPStmTurb

Dum55MPStmTurb(1)

(.LO, .L, .UP, .M = 0, 438.169647740304, +INF, 0)

-1 EqPTRel1cMPStmTurb(1)

1 EqPTRel1dMPStmTurb(1)

1 EqPTRel1fMPStmTurb(1)

Dum55MPStmTurb(2)

(.LO, .L, .UP, .M = 0, 0, +INF, EPS)


1 EqPTRel1dMPStmTurb(2)

1 EqPTRel1fMPStmTurb(2)

---- Dum66MPStmTurb

Dum66MPStmTurb(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 1.08745066683467)


1 EqPTRel1eMPStmTurb(1)


Dum66MPStmTurb(2)

(.LO, .L, .UP, .M = 0, 460, +INF, 0)

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Dum66MPStmTurb


1 EqPTRel1eMPStmTurb(2)


---- YModeMPStmTurb

YModeMPStmTurb(1,LPBkPr)

(.LO, .L, .UP, .M = 0, 1, 1, 0.001)



-1 EqLogMode5MPStmTurb(1,LPBkPr)

-1.000000E+8 EqLogBnd1MPStmTurb(1)

-0.001 obj

YModeMPStmTurb(1,LPExt)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)

-1 EqLogMode1MPStmTurb(1)



-1 EqLogMode5MPStmTurb(1,LPExt)


-0.001 obj

YModeMPStmTurb(1,VPCond)

(.LO, .L, .UP, .M = 0, 0, 1, 0.001)



-1 EqLogMode5MPStmTurb(1,VPCond)


-0.001 obj

YModeMPStmTurb(2,LPBkPr)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)



-1 EqLogMode5MPStmTurb(2,LPBkPr)


YModeMPStmTurb(2,LPExt)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-1 EqLogMode1MPStmTurb(2)



-1 EqLogMode5MPStmTurb(2,LPExt)


YModeMPStmTurb(2,VPCond)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)



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YModeMPStmTurb

-1 EqLogMode5MPStmTurb(2,VPCond)


---- HtLdVacCondTurb

HtLdVacCondTurb(1)

(.LO, .L, .UP, .M = 0, 111.872417346094, +INF, 0)

1 EqEnthBalVacCondTurb(1)

1 EqMassFCW(1)

---- MassFCW

MassFCW

(.LO, .L, .UP, .M = 0, 1336.90747306518, +INF, 0)

-0.0837 EqMassFCW(1)

-0.0007 EqWorkPumpVCT(1)

-0.0968 obj

---- WorkPumpVCT

WorkPumpVCT

(.LO, .L, .UP, .M = 0, 0.922466156414975, +INF, 0)

1 EqWorkPumpVCT(1)

1 Eqstpd4

---- WorkPump

WorkPump(VP)

(.LO, .L, .UP, .M = 0, 0.00668331174778287, +INF, 0)

1 EqWorkPump(VP)

1 Eqstpd4

WorkPump(MP)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqWorkPump(MP)

1 Eqstpd4

WorkPump(HP)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqWorkPump(HP)

1 Eqstpd4

WorkPump(HRSG)

(.LO, .L, .UP, .M = 0, 0.463503029404848, +INF, 0)

1 EqWorkPump(HRSG)

1 Eqstpd4

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---- Dum1BlrCmbtr

Dum1BlrCmbtr(MP,H2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(MP,O2)

1 EqCompMolBalBlrCmbtr(MP,H2O)

1 EqDum1BlrCmbtr(MP,H2)

0.575 EqExcessO2BlrCmbtr(MP)

Dum1BlrCmbtr(MP,O2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqCompMolBalBlrCmbtr(MP,O2)

1 EqDum1BlrCmbtr(MP,O2)

1 EqExcessO2BlrCmbtr(MP)

Dum1BlrCmbtr(MP,N2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqCompMolBalBlrCmbtr(MP,N2)

1 EqDum1BlrCmbtr(MP,N2)

Dum1BlrCmbtr(MP,CH4)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-2 EqCompMolBalBlrCmbtr(MP,O2)

1 EqCompMolBalBlrCmbtr(MP,CO2)


1 EqDum1BlrCmbtr(MP,CH4)


Dum1BlrCmbtr(MP,CO)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(MP,O2)


1 EqDum1BlrCmbtr(MP,CO)


Dum1BlrCmbtr(MP,CO2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqDum1BlrCmbtr(MP,CO2)

Dum1BlrCmbtr(MP,H2O)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqDum1BlrCmbtr(MP,H2O)

Dum1BlrCmbtr(HP,H2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(HP,O2)

1 EqCompMolBalBlrCmbtr(HP,H2O)

1 EqDum1BlrCmbtr(HP,H2)

0.575 EqExcessO2BlrCmbtr(HP)

Dum1BlrCmbtr(HP,O2)

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Dum1BlrCmbtr

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqCompMolBalBlrCmbtr(HP,O2)

1 EqDum1BlrCmbtr(HP,O2)

1 EqExcessO2BlrCmbtr(HP)

Dum1BlrCmbtr(HP,N2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqCompMolBalBlrCmbtr(HP,N2)

1 EqDum1BlrCmbtr(HP,N2)

Dum1BlrCmbtr(HP,CH4)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-2 EqCompMolBalBlrCmbtr(HP,O2)

1 EqCompMolBalBlrCmbtr(HP,CO2)


1 EqDum1BlrCmbtr(HP,CH4)


Dum1BlrCmbtr(HP,CO)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(HP,O2)


1 EqDum1BlrCmbtr(HP,CO)


Dum1BlrCmbtr(HP,CO2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqDum1BlrCmbtr(HP,CO2)

Dum1BlrCmbtr(HP,H2O)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqDum1BlrCmbtr(HP,H2O)

Dum1BlrCmbtr(GT,H2)

(.LO, .L, .UP, .M = 0, 5338.12355237439, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(GT,O2)

1 EqCompMolBalBlrCmbtr(GT,H2O)

1 EqDum1BlrCmbtr(GT,H2)

0.575 EqExcessO2BlrCmbtr(GT)

Dum1BlrCmbtr(GT,O2)

(.LO, .L, .UP, .M = 0, 18171.4005610171, +INF, 0)

1 EqCompMolBalBlrCmbtr(GT,O2)

1 EqDum1BlrCmbtr(GT,O2)

1 EqExcessO2BlrCmbtr(GT)

Dum1BlrCmbtr(GT,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, +INF, 0)

1 EqCompMolBalBlrCmbtr(GT,N2)

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Dum1BlrCmbtr

1 EqDum1BlrCmbtr(GT,N2)

Dum1BlrCmbtr(GT,CH4)

(.LO, .L, .UP, .M = 0, 970.567918613525, +INF, 0)

-2 EqCompMolBalBlrCmbtr(GT,O2)

1 EqCompMolBalBlrCmbtr(GT,CO2)


1 EqDum1BlrCmbtr(GT,CH4)


Dum1BlrCmbtr(GT,CO)

(.LO, .L, .UP, .M = 0, 2911.70375584058, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(GT,O2)


1 EqDum1BlrCmbtr(GT,CO)


Dum1BlrCmbtr(GT,CO2)

(.LO, .L, .UP, .M = 0, 485.283959306763, +INF, 0)


1 EqDum1BlrCmbtr(GT,CO2)

Dum1BlrCmbtr(GT,H2O)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)


1 EqDum1BlrCmbtr(GT,H2O)

Dum1BlrCmbtr(GTSF,H2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(GTSF,O2)

1 EqCompMolBalBlrCmbtr(GTSF,H2O)

1 EqDum1BlrCmbtr(GTSF,H2)

0.575 EqExcessO2BlrCmbtr(GTSF)

Dum1BlrCmbtr(GTSF,O2)

(.LO, .L, .UP, .M = 0, 12105.3510696826, +INF, 0)

1 EqCompMolBalBlrCmbtr(GTSF,O2)

1 EqDum1BlrCmbtr(GTSF,O2)

1 EqExcessO2BlrCmbtr(GTSF)

Dum1BlrCmbtr(GTSF,N2)

(.LO, .L, .UP, .M = 0, 68359.0783009692, +INF, 0)

1 EqCompMolBalBlrCmbtr(GTSF,N2)

1 EqDum1BlrCmbtr(GTSF,N2)

Dum1BlrCmbtr(GTSF,CH4)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-2 EqCompMolBalBlrCmbtr(GTSF,O2)

1 EqCompMolBalBlrCmbtr(GTSF,CO2)


1 EqDum1BlrCmbtr(GTSF,CH4)

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Dum1BlrCmbtr


Dum1BlrCmbtr(GTSF,CO)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.5 EqCompMolBalBlrCmbtr(GTSF,O2)


1 EqDum1BlrCmbtr(GTSF,CO)


Dum1BlrCmbtr(GTSF,CO2)

(.LO, .L, .UP, .M = 0, 4367.55563376086, +INF, 0)


1 EqDum1BlrCmbtr(GTSF,CO2)

Dum1BlrCmbtr(GTSF,H2O)

(.LO, .L, .UP, .M = 0, 7279.25938960144, +INF, 0)


1 EqDum1BlrCmbtr(GTSF,H2O)

---- QBlr Heat exchanged

QBlr(MP)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 EqGasEgyBalBlr(MP)

1 EqWtrEgyBalBlr(MP)

QBlr(HP)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 EqGasEgyBalBlr(HP)

1 EqWtrEgyBalBlr(HP)

QBlr(HRSG)

(.LO, .L, .UP, .M = 0, 297.81493259253, +INF, 0)

-1 EqGasEgyBalBlr(HRSG)

1 EqWtrEgyBalBlr(HRSG)

---- POpr operating pressure of header

POpr(MP)

(.LO, .L, .UP, .M = 20, 20, 20, 16.9061532831351)

1 EqTSat2(MP)

-1 EqPRel1PLev(MP,2)








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POpr operating pressure of header



POpr(HP)

(.LO, .L, .UP, .M = 45, 45, 45, -30.436061476341)

1 EqTSat2(HP)

-1 EqPRel1PLev(HP,26)








POpr(LP)

(.LO, .L, .UP, .M = 7, 7, 7, 134.340180861686)

1 EqTSat2(LP)

-1 EqPRel1PLev(LP,3)









---- TOpr operating temperature of header

TOpr(MP)

(.LO, .L, .UP, .M = 469, 568.549477042195, 701, 0)

1 EqUBTOpr(MP)

1 EqLBTOpr(MP)

-1 EqTRel1PLev(MP,5)




-1 EqT1

TOpr(HP)

(.LO, .L, .UP, .M = 528, 695.267448409642, 795, 0)

1 EqUBTOpr(HP)

1 EqLBTOpr(HP)

-1 EqTRel1PLev(HP,1)





-1 EqT2

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TOpr operating temperature of header

-1 EqT3

TOpr(LP)

(.LO, .L, .UP, .M = 414, 438.169647740304, 581, 0)

1 EqUBTOpr(LP)

1 EqLBTOpr(LP)

-1 EqTRel1PLev(LP,12)

-1 EqTRel1PLev(LP,36)

---- TSatOpr Heat exchanged

TSatOpr(MP)

(.LO, .L, .UP, .M = 469, 485.588337116896, 526, 0)

(-0.3958) EqTSat2(MP)

-1 EqUBTOpr(MP)

-1 EqLBTOpr(MP)

TSatOpr(HP)

(.LO, .L, .UP, .M = 528, 530.580060386281, 570, 0)

(-0.7398) EqTSat2(HP)

-1 EqUBTOpr(HP)

-1 EqLBTOpr(HP)

TSatOpr(LP)

(.LO, .L, .UP, .M = 414, 438.169647740304, 456, 0)

(-0.1735) EqTSat2(LP)

-1 EqUBTOpr(LP)

-1 EqLBTOpr(LP)

---- WasteH

WasteH(MP)

(.LO, .L, .UP, .M = 0, 1.73158450813642, +INF, 0)

-1 EqEgyBalStmDmd(MP)

1 EqPen1StmDmd(MP)

WasteH(HP)

(.LO, .L, .UP, .M = 0, 0.997331135516397, +INF, 0)

-1 EqEgyBalStmDmd(HP)

1 EqPen1StmDmd(HP)

WasteH(LP)

(.LO, .L, .UP, .M = 0, 0, +INF, 13.4301126153083)

-1 EqEgyBalStmDmd(LP)

1 EqPen1StmDmd(LP)

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---- MassFCW1

MassFCW1(MP)

(.LO, .L, .UP, .M = 0, 20.6929315025863, +INF, 0)

-0.0837 EqPen1StmDmd(MP)

MassFCW1(HP)

(.LO, .L, .UP, .M = 0, 11.9183931108556, +INF, 0)

-0.0837 EqPen1StmDmd(HP)

MassFCW1(LP)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-0.0837 EqPen1StmDmd(LP)

---- WorkFan

WorkFan

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

1 EqWorkFan

1 Eqstpd4

---- InPGTCmpr Inlet Pressure for compressor

InPGTCmpr(1)

(.LO, .L, .UP, .M = 0.99, 1.01325, 1.1, 0)

-1 EqInPGTCmpr(1)

(153.0291) EqPTRelGTCmpr(1)

-1 EqPRelGtCmpr(1)

---- OutPGTCmpr Outlet Pressure for compressor

OutPGTCmpr(1)

(.LO, .L, .UP, .M = 0.99, 20, 20, -224.761386939264)

-1 EqOutPGTCmpr(1)

(-7.7528) EqPTRelGTCmpr(1)

1 EqPRelGtCmpr(1)

---- InTGTCmpr Inlet Temperature for compressor

InTGTCmpr(1)

(.LO, .L, .UP, .M = 298, 298.15, 299, 0)

-1 EqInTGTCmpr(1)

(-2.096) EqPTRelGTCmpr(1)

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---- OutTGTCmpr Outlet Temperature for compressor

OutTGTCmpr(1)

(.LO, .L, .UP, .M = 298, 624.925663385689, 704, 0)

-1 EqOutTGTCmpr(1)

1 EqPTRelGTCmpr(1)

---- WorkGTCmpr Ideal compressor work

WorkGTCmpr(1)

(.LO, .L, .UP, .M = 0, 234.212600992182, +INF, 0)

1 EqWorkGTCmpr(1)

1 EqWorkGT

---- InPGTExpdr Inlet Pressure for expander

InPGTExpdr(1)

(.LO, .L, .UP, .M = 0.99, 20, 20, 0)

-1 EqInPGTExpdr(1)

(9.4446) EqPTRelGTExpdr(1)

-1 EqPRelGTExpdr(1)

---- OutPGTExpdr Outlet Pressure for expander

OutPGTExpdr(1)

(.LO, .L, .UP, .M = 1.3, 1.3, 20, 5575.74363544757)

-1 EqOutPGTExpdr(1)

(-145.3014) EqPTRelGTExpdr(1)

1 EqPRelGTExpdr(1)

---- InTGTExpdr Inlet Temperature for expander

InTGTExpdr(1)

(.LO, .L, .UP, .M = 298, 1500, 1510, 0)

-1 EqInTGTExpdr(1)

(-0.5075) EqPTRelGTExpdr(1)

---- OutTGTExpdr Outlet Temperature for expander

OutTGTExpdr(1)

(.LO, .L, .UP, .M = 298, 761.291470669467, 1510, 0)

-1 EqOutTGTExpdr(1)

1 EqPTRelGTExpdr(1)

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---- WorkGTExpdr Ideal expander work

WorkGTExpdr(1)

(.LO, .L, .UP, .M = 0, 667.651332185769, +INF, 0)

1 EqWorkGTExpdr(1)

-1 EqWorkGT

---- WorkGT

WorkGT

(.LO, .L, .UP, .M = 0, 433.438731193587, +INF, 0)

1 EqWorkGT

-1 Eqstpd4

---- MDE

MDE(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 30.180461170002)

1 Eqstpd4

-1 Eqstpd5(1)

1 Eqstpd10(1)

MDE(2)

(.LO, .L, .UP, .M = 0, 0, +INF, 20.731964417794)

1 Eqstpd4

-1 Eqstpd5(2)

1 Eqstpd10(2)

---- WHPTE

WHPTE(1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 Eqstpd4

-1 Eqstpd7(1)

1 Eqstpd11(1)

WHPTE(2)

(.LO, .L, .UP, .M = 0, 67.953921303981, +INF, 0)

-1 Eqstpd4

-1 Eqstpd7(2)

1 Eqstpd11(2)

WHPTE(3)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 Eqstpd4

-1 Eqstpd7(3)

1 Eqstpd11(3)

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---- MDC

MDC(1)

(.LO, .L, .UP, .M = 0, 5, +INF, 0)

-1 Eqstpd5(1)

1 Eqstpd6(1)

1 Eqstpd9(1)

MDC(2)

(.LO, .L, .UP, .M = 0, 15, +INF, 0)

-1 Eqstpd5(2)

1 Eqstpd6(2)

1 Eqstpd9(2)

---- WHPTM

WHPTM(1,1)

(.LO, .L, .UP, .M = 0, 0, +INF, 9.44849675220797)

-1 Eqstpd6(1)

-1 Eqstpd7(1)

1 Eqstpd12(1,1)

WHPTM(1,2)

(.LO, .L, .UP, .M = 0, 15, +INF, 0)

-1 Eqstpd6(2)

-1 Eqstpd7(1)

1 Eqstpd12(1,2)

WHPTM(2,1)

(.LO, .L, .UP, .M = 0, 0, +INF, 30.180461170002)

-1 Eqstpd6(1)

-1 Eqstpd7(2)

1 Eqstpd12(2,1)

WHPTM(2,2)

(.LO, .L, .UP, .M = 0, 0, +INF, 20.731964417794)

-1 Eqstpd6(2)

-1 Eqstpd7(2)

1 Eqstpd12(2,2)

WHPTM(3,1)

(.LO, .L, .UP, .M = 0, 0, +INF, 9.44849675220797)

-1 Eqstpd6(1)

-1 Eqstpd7(3)

1 Eqstpd12(3,1)

WHPTM(3,2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 Eqstpd6(2)

-1 Eqstpd7(3)

1 Eqstpd12(3,2)

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---- WMPTM

WMPTM(1,1)

(.LO, .L, .UP, .M = 0, 5, +INF, 0)

-1 Eqstpd6(1)

-1 Eqstpd8(1)

1 Eqstpd13(1,1)

WMPTM(1,2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 Eqstpd6(2)

-1 Eqstpd8(1)

1 Eqstpd13(1,2)

WMPTM(2,1)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 Eqstpd6(1)

-1 Eqstpd8(2)

1 Eqstpd13(2,1)

WMPTM(2,2)

(.LO, .L, .UP, .M = 0, 0, +INF, 0)

-1 Eqstpd6(2)

-1 Eqstpd8(2)

1 Eqstpd13(2,2)

---- YMD

YMD(1)

(.LO, .L, .UP, .M = 0, 1, 1, EPS)

-100 Eqstpd9(1)

100 Eqstpd10(1)

YMD(2)

(.LO, .L, .UP, .M = 0, 1, 1, EPS)

-100 Eqstpd9(2)

100 Eqstpd10(2)

---- YWHPTE

YWHPTE(1)

(.LO, .L, .UP, .M = 0, 0, 1, -16585.5715342352)

-800 Eqstpd11(1)

1 Eqstpd14

1 Eqstpd16(1)

YWHPTE(2)

(.LO, .L, .UP, .M = 0, 1, 1, EPS)

-800 Eqstpd11(2)

1 Eqstpd14

1 Eqstpd16(2)

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YWHPTE

YWHPTE(3)

(.LO, .L, .UP, .M = 0, 0, 1, -16585.5715342352)

-800 Eqstpd11(3)

1 Eqstpd14

1 Eqstpd16(3)

---- YWHPTM

YWHPTM(1,1)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-100 Eqstpd12(1,1)

1 Eqstpd15(1)

1 Eqstpd16(1)

YWHPTM(1,2)

(.LO, .L, .UP, .M = 0, 1, 1, EPS)

-100 Eqstpd12(1,2)

1 Eqstpd15(2)

1 Eqstpd16(1)

YWHPTM(2,1)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-100 Eqstpd12(2,1)

1 Eqstpd15(1)

1 Eqstpd16(2)

YWHPTM(2,2)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-100 Eqstpd12(2,2)

1 Eqstpd15(2)

1 Eqstpd16(2)

YWHPTM(3,1)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-100 Eqstpd12(3,1)

1 Eqstpd15(1)

1 Eqstpd16(3)

YWHPTM(3,2)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-100 Eqstpd12(3,2)

1 Eqstpd15(2)

1 Eqstpd16(3)

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---- YWMPTM

YWMPTM(1,1)

(.LO, .L, .UP, .M = 0, 1, 1, EPS)

-100 Eqstpd13(1,1)

1 Eqstpd15(1)

1 Eqstpd17(1)

YWMPTM(1,2)

(.LO, .L, .UP, .M = 0, 0, 1, -944.849675220797)

-100 Eqstpd13(1,2)

1 Eqstpd15(2)

1 Eqstpd17(1)

YWMPTM(2,1)

(.LO, .L, .UP, .M = 0, 0, 1, EPS)

-100 Eqstpd13(2,1)

1 Eqstpd15(1)

1 Eqstpd17(2)

YWMPTM(2,2)

(.LO, .L, .UP, .M = 0, 0, 1, -944.849675220797)

-100 Eqstpd13(2,2)

1 Eqstpd15(2)

1 Eqstpd17(2)

---- Z

Z

(.LO, .L, .UP, .M = -INF, 36579.9434091524, +INF, 0)

1 obj

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Model Statistics SOLVE TEST4a Using MINLP From line 2276

MODEL STATISTICS

BLOCKS OF EQUATIONS 193 SINGLE EQUATIONS 1,275

BLOCKS OF VARIABLES 88 SINGLE VARIABLES 1,309

NON ZERO ELEMENTS 4,007 NON LINEAR N-Z 913

DERIVATIVE POOL 20 CONSTANT POOL 65

CODE LENGTH 7,036 DISCRETE VARIABLES 62

GENERATION TIME = 0.037 SECONDS 4 MB 24.4.1 r50296 LEX-LEG

EXECUTION TIME = 0.039 SECONDS 4 MB 24.4.1 r50296 LEX-LEG

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Solution Report SOLVE TEST4a Using MINLP From line 2276

S O L V E S U M M A R Y

MODEL TEST4a OBJECTIVE Z

TYPE MINLP DIRECTION MINIMIZE

SOLVER DICOPT FROM LINE 2276

**** SOLVER STATUS 1 Normal Completion

**** MODEL STATUS 8 Integer Solution

**** OBJECTIVE VALUE 5226.2818

RESOURCE USAGE, LIMIT 2.030 1000.000

ITERATION COUNT, LIMIT 11410 20000

EVALUATION ERRORS 0 0

------------------------------------------------------------------

Dicopt 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

------------------------------------------------------------------

Aldo Vecchietti and Ignacio E. Grossmann

Engineering Design Research Center

Carnegie Mellon University

Pittsburgh, Pennsylvania 15213

------------------------------------------------------------------

Reading parameter(s) from "/var/www/html/interfaces/cgi-bin/steam/dicopt.opt"

>> *maxcycles 40

>> infeasder 1

>>

>> * binary corresponding to infeasible NLP subproblems are rejected

>> *continue 0

>>

>> * iteration limit for NLPS

>>

>> *stop 0

Finished reading from "/var/www/html/interfaces/cgi-bin/steam/dicopt.opt"

CONOPT 3 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

C O N O P T 3 version 3.16D

Copyright (C) ARKI Consulting and Development A/S

Bagsvaerdvej 246 A

DK-2880 Bagsvaerd, Denmark

** Optimal solution. Reduced gradient less than tolerance.

CONOPT time Total 0.083 seconds

of which: Function evaluations 0.037 = 44.6%

1st Derivative evaluations 0.006 = 7.2%

IBM ILOG CPLEX 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

--- GAMS/Cplex licensed for continuous and discrete problems.

Cplex 12.6.1.0

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The search will stop after 10000 nodes.

Unable to load names.

MIP status(101): integer optimal solution

Cplex Time: 0.06sec (det. 26.71 ticks)

Fixing integer variables, and solving final LP...

Fixed MIP status(1): optimal


Proven optimal solution.

MIP Solution: 5131.515236 (327 iterations, 44 nodes)

Final Solve: 5131.515236 (115 iterations)

Best possible: 5131.515236

Absolute gap: 0.000000

Relative gap: 0.000000

--- DICOPT: Setting up next NLP




Bagsvaerdvej 246 A


** Infeasible solution. Reduced gradient less than tolerance.




--- WARNING : infeasder option is on,

--- problem will keep running even when infeasible NLPs are given

--- GMO Resort Time 0ms



Cplex 12.6.1.0









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Bagsvaerdvej 246 A



The feasibility tolerance (Rtnwmi) is 4.00000E-10

It may be relaxed with option:

Rtnwmi=x.xx









Cplex 12.6.1.0













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Bagsvaerdvej 246 A









Cplex 12.6.1.0


















Bagsvaerdvej 246 A



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Cplex 12.6.1.0


















Bagsvaerdvej 246 A









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Cplex 12.6.1.0


















Bagsvaerdvej 246 A











Cplex 12.6.1.0






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Bagsvaerdvej 246 A











Cplex 12.6.1.0














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Bagsvaerdvej 246 A











Cplex 12.6.1.0


















Bagsvaerdvej 246 A


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Cplex 12.6.1.0


















Bagsvaerdvej 246 A









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Cplex 12.6.1.0


















Bagsvaerdvej 246 A






--- DICOPT: Stopped on NLP worsening

The search was stopped because the objective function

of the NLP subproblems started to deteriorate.

--- DICOPT: Best integer solution found: 5226.281783

---- EQU EqTotMolStr Total mass balance for stream (Total Mole flow = sum of component Mole f

low)

LOWER LEVEL UPPER MARGINAL

1 . . . -2.8914

2 . . . -0.0680

3 . . . 2.9051

4 . . . -0.1092

5 . . . -0.0151

model.lst Wed May 30 15:17:17 2018 340


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EQU EqTotMolStr Total mass balance for stream (Total Mole flow = sum of component Mole f

low)


6 . . . 2.8958

7 . . . 0.1871

8 . . . 0.1252

9 . . . 3.4705

10 . . . -0.5986

11 . . . 3.4232

12 . . . EPS

13 . . . -3.4227

14 . . . -3.4220

15 . . . -3.4220

16 . . . -2.9286

17 . . . 3.5070

18 . . . 3.7488

19 . . . 3.5539

20 . . . 3.5539

21 . . . -0.0390

22 . . . EPS

23 . . . -0.0369

24 . . . EPS

25 . . . -3.1536

26 . . . EPS

27 . . . 0.0043

28 . . . EPS

29 . . . 0.0043

30 . . . EPS

31 . . . 2.9675

32 . . . EPS

33 . . . 2.9051

34 . . . -2.8914

35 . . . EPS

36 . . . EPS

37 . . . -0.6666

38 . . . -3.4232

39 . . . EPS

40 . . . EPS

41 . . . EPS

42 . . . EPS

43 . . . EPS

44 . . . EPS

45 . . . EPS

46 . . . EPS

47 . . . EPS

48 . . . -2.8914

49 . . . EPS

50 . . . 2.8245

51 . . . .

52 . . . -3.8361

53 . . . -3.6418

54 . . . -3.6418

model.lst Wed May 30 15:17:17 2018 341


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EQU EqTotMolStr Total mass balance for stream (Total Mole flow = sum of component Mole f

low)


55 . . . -0.0151

56 . . . 2.8958

57 . . . 0.1871

58 . . . -2.8914

59 . . . EPS

60 . . . 2.9737

61 . . . 0.1720

62 . . . -2.8914

63 . . . 0.0201

64 . . . 2.8958

65 . . . 0.1720

---- EQU EqEnthpyGasStr1


21.H2 -0.0023 -0.0023 -0.0023 EPS

21.O2 -0.0024 -0.0024 -0.0024 EPS

21.N2 -0.0024 -0.0024 -0.0024 EPS

21.CH4 -0.0235 -0.0235 -0.0235 EPS

21.CO -0.0331 -0.0331 -0.0331 EPS

21.CO2 -0.1119 -0.1119 -0.1119 EPS

21.H2O -0.0699 -0.0699 -0.0699 EPS

22.H2 -0.0023 -0.0023 -0.0023 EPS

22.O2 -0.0024 -0.0024 -0.0024 EPS

22.N2 -0.0024 -0.0024 -0.0024 EPS

22.CH4 -0.0235 -0.0235 -0.0235 EPS

22.CO -0.0331 -0.0331 -0.0331 EPS

22.CO2 -0.1119 -0.1119 -0.1119 EPS

22.H2O -0.0699 -0.0699 -0.0699 EPS

23.H2 -0.0023 -0.0023 -0.0023 EPS

23.O2 -0.0024 -0.0024 -0.0024 EPS

23.N2 -0.0024 -0.0024 -0.0024 EPS

23.CH4 -0.0235 -0.0235 -0.0235 EPS

23.CO -0.0331 -0.0331 -0.0331 EPS

23.CO2 -0.1119 -0.1119 -0.1119 EPS

23.H2O -0.0699 -0.0699 -0.0699 EPS

24.H2 -0.0023 -0.0023 -0.0023 EPS

24.O2 -0.0024 -0.0024 -0.0024 EPS

24.N2 -0.0024 -0.0024 -0.0024 EPS

24.CH4 -0.0235 -0.0235 -0.0235 EPS

24.CO -0.0331 -0.0331 -0.0331 EPS

24.CO2 -0.1119 -0.1119 -0.1119 EPS

24.H2O -0.0699 -0.0699 -0.0699 EPS

27.H2 -0.0023 -0.0023 -0.0023 EPS

27.O2 -0.0024 -0.0024 -0.0024 EPS

27.N2 -0.0024 -0.0024 -0.0024 EPS

27.CH4 -0.0235 -0.0235 -0.0235 EPS

27.CO -0.0331 -0.0331 -0.0331 EPS

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EQU EqEnthpyGasStr1


27.CO2 -0.1119 -0.1119 -0.1119 EPS

27.H2O -0.0699 -0.0699 -0.0699 EPS

28.H2 -0.0023 -0.0023 -0.0023 EPS

28.O2 -0.0024 -0.0024 -0.0024 EPS

28.N2 -0.0024 -0.0024 -0.0024 EPS

28.CH4 -0.0235 -0.0235 -0.0235 EPS

28.CO -0.0331 -0.0331 -0.0331 EPS

28.CO2 -0.1119 -0.1119 -0.1119 EPS

28.H2O -0.0699 -0.0699 -0.0699 EPS

29.H2 -0.0023 -0.0023 -0.0023 EPS

29.O2 -0.0024 -0.0024 -0.0024 EPS

29.N2 -0.0024 -0.0024 -0.0024 EPS

29.CH4 -0.0235 -0.0235 -0.0235 EPS

29.CO -0.0331 -0.0331 -0.0331 EPS

29.CO2 -0.1119 -0.1119 -0.1119 EPS

29.H2O -0.0699 -0.0699 -0.0699 EPS

30.H2 -0.0023 -0.0023 -0.0023 EPS

30.O2 -0.0024 -0.0024 -0.0024 EPS

30.N2 -0.0024 -0.0024 -0.0024 EPS

30.CH4 -0.0235 -0.0235 -0.0235 EPS

30.CO -0.0331 -0.0331 -0.0331 EPS

30.CO2 -0.1119 -0.1119 -0.1119 EPS

30.H2O -0.0699 -0.0699 -0.0699 EPS

39.H2 -0.0023 -0.0023 -0.0023 EPS

39.O2 -0.0024 -0.0024 -0.0024 -118193.1993

39.N2 -0.0024 -0.0024 -0.0024 -444631.5594

39.CH4 -0.0235 -0.0235 -0.0235 EPS

39.CO -0.0331 -0.0331 -0.0331 EPS

39.CO2 -0.1119 -0.1119 -0.1119 EPS

39.H2O -0.0699 -0.0699 -0.0699 EPS

40.H2 -0.0023 -0.0023 -0.0023 EPS

40.O2 -0.0024 -0.0024 -0.0024 17258.1809

40.N2 -0.0024 -0.0024 -0.0024 64923.6330

40.CH4 -0.0235 -0.0235 -0.0235 EPS

40.CO -0.0331 -0.0331 -0.0331 EPS

40.CO2 -0.1119 -0.1119 -0.1119 EPS

40.H2O -0.0699 -0.0699 -0.0699 EPS

41.H2 -0.0023 -0.0023 -0.0023 -29651.1872

41.O2 -0.0024 -0.0024 -0.0024 EPS

41.N2 -0.0024 -0.0024 -0.0024 EPS

41.CH4 -0.0235 -0.0235 -0.0235 -5391.1249

41.CO -0.0331 -0.0331 -0.0331 -16173.3748

41.CO2 -0.1119 -0.1119 -0.1119 -2695.5625

41.H2O -0.0699 -0.0699 -0.0699 EPS

42.H2 -0.0023 -0.0023 -0.0023 EPS

42.O2 -0.0024 -0.0024 -0.0024 -11496.9861

42.N2 -0.0024 -0.0024 -0.0024 -64923.6330

42.CH4 -0.0235 -0.0235 -0.0235 EPS

42.CO -0.0331 -0.0331 -0.0331 EPS

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EQU EqEnthpyGasStr1


42.CO2 -0.1119 -0.1119 -0.1119 -4148.0603

42.H2O -0.0699 -0.0699 -0.0699 -6913.4338

43.H2 -0.0023 -0.0023 -0.0023 EPS

43.O2 -0.0024 -0.0024 -0.0024 10456.5392

43.N2 -0.0024 -0.0024 -0.0024 59048.2159

43.CH4 -0.0235 -0.0235 -0.0235 EPS

43.CO -0.0331 -0.0331 -0.0331 EPS

43.CO2 -0.1119 -0.1119 -0.1119 3772.6718

43.H2O -0.0699 -0.0699 -0.0699 6287.7864

44.H2 -0.0023 -0.0023 -0.0023 -4861.6262

44.O2 -0.0024 -0.0024 -0.0024 EPS

44.N2 -0.0024 -0.0024 -0.0024 EPS

44.CH4 -0.0235 -0.0235 -0.0235 -883.9320

44.CO -0.0331 -0.0331 -0.0331 -2651.7961

44.CO2 -0.1119 -0.1119 -0.1119 -441.9660

44.H2O -0.0699 -0.0699 -0.0699 EPS

45.H2 -0.0023 -0.0023 -0.0023 EPS

45.O2 -0.0024 -0.0024 -0.0024 EPS

45.N2 -0.0024 -0.0024 -0.0024 EPS

45.CH4 -0.0235 -0.0235 -0.0235 EPS

45.CO -0.0331 -0.0331 -0.0331 EPS

45.CO2 -0.1119 -0.1119 -0.1119 EPS

45.H2O -0.0699 -0.0699 -0.0699 EPS

46.H2 -0.0023 -0.0023 -0.0023 EPS

46.O2 -0.0024 -0.0024 -0.0024 62756.3592

46.N2 -0.0024 -0.0024 -0.0024 385583.3436

46.CH4 -0.0235 -0.0235 -0.0235 EPS

46.CO -0.0331 -0.0331 -0.0331 EPS

46.CO2 -0.1119 -0.1119 -0.1119 28613.1449

46.H2O -0.0699 -0.0699 -0.0699 47688.5748

---- EQU EqEnthVapStr2


1 -0.0699 -0.0699 -0.0699 EPS

2 -0.0699 -0.0699 -0.0699 EPS

3 -0.0699 -0.0699 -0.0699 EPS

4 -0.0699 -0.0699 -0.0699 EPS

5 -0.0699 -0.0699 -0.0699 EPS

6 -0.0699 -0.0699 -0.0699 EPS

7 -0.0699 -0.0699 -0.0699 EPS

12 -0.0699 -0.0699 -0.0699 EPS

25 -0.0699 -0.0699 -0.0699 EPS

26 -0.0699 -0.0699 -0.0699 EPS

31 -0.0699 -0.0699 -0.0699 EPS

32 -0.0699 -0.0699 -0.0699 EPS

33 -0.0699 -0.0699 -0.0699 EPS

34 -0.0699 -0.0699 -0.0699 27325.4312

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EQU EqEnthVapStr2


35 -0.0699 -0.0699 -0.0699 EPS

36 -0.0699 -0.0699 -0.0699 EPS

47 -0.0699 -0.0699 -0.0699 EPS

48 -0.0699 -0.0699 -0.0699 EPS

49 -0.0699 -0.0699 -0.0699 EPS

50 -0.0699 -0.0699 -0.0699 EPS

51 -0.0699 -0.0699 -0.0699 EPS

55 -0.0699 -0.0699 -0.0699 EPS

56 -0.0699 -0.0699 -0.0699 EPS

57 -0.0699 -0.0699 -0.0699 EPS

58 -0.0699 -0.0699 -0.0699 -21333.8717

59 -0.0699 -0.0699 -0.0699 111461.6715

60 -0.0699 -0.0699 -0.0699 6799.0912

61 -0.0699 -0.0699 -0.0699 EPS

62 -0.0699 -0.0699 -0.0699 EPS

63 -0.0699 -0.0699 -0.0699 EPS

64 -0.0699 -0.0699 -0.0699 EPS

65 -0.0699 -0.0699 -0.0699 EPS

---- EQU EqEnthSatLiq


1 -0.0699 -0.0699 -0.0699 EPS

2 -0.0699 -0.0699 -0.0699 EPS

3 -0.0699 -0.0699 -0.0699 EPS

4 -0.0699 -0.0699 -0.0699 EPS

5 -0.0699 -0.0699 -0.0699 EPS

6 -0.0699 -0.0699 -0.0699 EPS

7 -0.0699 -0.0699 -0.0699 EPS

8 -0.0699 -0.0699 -0.0699 EPS

10 -0.0699 -0.0699 -0.0699 EPS

11 -0.0699 -0.0699 -0.0699 -153780.5492

12 -0.0699 -0.0699 -0.0699 EPS

13 -0.0699 -0.0699 -0.0699 EPS

14 -0.0699 -0.0699 -0.0699 EPS

15 -0.0699 -0.0699 -0.0699 165878.0567

25 -0.0699 -0.0699 -0.0699 EPS

26 -0.0699 -0.0699 -0.0699 EPS

31 -0.0699 -0.0699 -0.0699 EPS

32 -0.0699 -0.0699 -0.0699 EPS

33 -0.0699 -0.0699 -0.0699 EPS

34 -0.0699 -0.0699 -0.0699 EPS

35 -0.0699 -0.0699 -0.0699 EPS

36 -0.0699 -0.0699 -0.0699 EPS

37 -0.0699 -0.0699 -0.0699 EPS

38 -0.0699 -0.0699 -0.0699 34061.7416

47 -0.0699 -0.0699 -0.0699 EPS

48 -0.0699 -0.0699 -0.0699 EPS

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EQU EqEnthSatLiq


49 -0.0699 -0.0699 -0.0699 EPS

50 -0.0699 -0.0699 -0.0699 EPS

51 -0.0699 -0.0699 -0.0699 EPS

52 -0.0699 -0.0699 -0.0699 EPS

53 -0.0699 -0.0699 -0.0699 EPS

54 -0.0699 -0.0699 -0.0699 5153.6619

55 -0.0699 -0.0699 -0.0699 EPS

56 -0.0699 -0.0699 -0.0699 EPS

57 -0.0699 -0.0699 -0.0699 EPS

58 -0.0699 -0.0699 -0.0699 EPS

59 -0.0699 -0.0699 -0.0699 EPS

60 -0.0699 -0.0699 -0.0699 1199.8396

61 -0.0699 -0.0699 -0.0699 EPS

62 -0.0699 -0.0699 -0.0699 EPS

63 -0.0699 -0.0699 -0.0699 EPS

64 -0.0699 -0.0699 -0.0699 EPS

65 -0.0699 -0.0699 -0.0699 EPS

---- EQU EqTSat


1 . . . EPS

2 . . . EPS

3 . . . -8.8855

4 . . . EPS

5 . . . EPS

6 . . . EPS

7 . . . EPS

8 . . . EPS

10 . . . -7.2625

11 . . . 74.9386

12 . . . EPS

13 . . . EPS

14 . . . EPS

15 . . . -91.1730

16 . . . -0.1677

25 . . . EPS

26 . . . EPS

31 . . . EPS

32 . . . EPS

33 . . . EPS

34 . . . EPS

35 . . . EPS

36 . . . EPS

37 . . . -1.7783

38 . . . -5.6895

47 . . . EPS

48 . . . EPS

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EQU EqTSat


49 . . . EPS

50 . . . EPS

51 . . . EPS

52 . . . EPS

53 . . . EPS

54 . . . -0.2610

55 . . . EPS

56 . . . EPS

57 . . . EPS

58 . . . EPS

59 . . . EPS

60 . . . -0.5614

61 . . . EPS

62 . . . EPS

63 . . . EPS

64 . . . EPS

65 . . . EPS

---- EQU EqEnthP2Str Enthalpy of 2 phase stream


1 . . . EPS

2 . . . EPS

3 . . . EPS

4 . . . EPS

5 . . . EPS

6 . . . EPS

7 . . . EPS

12 . . . EPS

25 . . . EPS

26 . . . EPS

31 . . . .

32 . . . .

33 . . . EPS

34 . . . 27325.4312

35 . . . EPS

36 . . . EPS

47 . . . EPS

48 . . . EPS

49 . . . .

50 . . . EPS

51 . . . EPS

55 . . . EPS

56 . . . .

57 . . . EPS

58 . . . -21333.8717

59 . . . 111461.6715

60 . . . 7998.9308

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EQU EqEnthP2Str Enthalpy of 2 phase stream


61 . . . EPS

62 . . . EPS

63 . . . EPS

64 . . . .

65 . . . EPS

---- EQU EqTP2


1 . 164.6874 +INF .

2 . 82.9611 +INF .

3 . . +INF 1.5419

4 . . +INF EPS

5 . 82.9611 +INF .

6 . 21.8304 +INF .

7 . . +INF .

12 . . +INF EPS

25 . . +INF EPS

26 . . +INF EPS

31 . . +INF EPS

32 . . +INF EPS

33 . . +INF EPS

34 . 164.6874 +INF .

35 . 82.9611 +INF .

36 . . +INF .

47 . 164.6874 +INF .

48 . 164.6874 +INF .

49 . . +INF EPS

50 . 82.9611 +INF .

51 . 130.3798 +INF .

55 . 82.9611 +INF .

56 . 21.8304 +INF .

57 . . +INF EPS

58 . 164.6874 +INF .

59 . 82.9611 +INF .

60 . . +INF 0.0654

61 . . +INF EPS

62 . 164.6874 +INF .

63 . 44.4117 +INF .

64 . 21.8304 +INF .

65 . . +INF EPS

model.lst Wed May 30 15:17:17 2018 348


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---- EQU EqLogP21


1 -INF . . EPS

2 -INF . . .

3 -INF . . .

4 -INF -0.8500 . .

5 -INF . . EPS

6 -INF . . .

7 -INF -0.8500 . .

12 -INF -0.1330 . .

25 -INF . . .

26 -INF . . .

31 -INF . . EPS

32 -INF . . EPS

33 -INF . . EPS

34 -INF . . -274.0348

35 -INF . . EPS

36 -INF -0.9999 . .

47 -INF . . EPS

48 -INF . . .

49 -INF . . EPS

50 -INF . . .

51 -INF . . .

55 -INF . . .

56 -INF . . .

57 -INF -0.8500 . .

58 -INF . . .

59 -INF . . -1145.0411

60 -INF -0.8500 . .

61 -INF -0.8500 . .

62 -INF . . .

63 -INF . . EPS

64 -INF . . EPS

65 -INF -0.8500 . .

---- EQU EqLogP22


1 . . +INF .

2 . . +INF .

3 . . +INF .

4 . 0.1499 +INF .

5 . . +INF .

6 . . +INF .

7 . 0.1499 +INF .

12 . 0.8669 +INF .

25 . . +INF .

26 . . +INF .

31 . . +INF .

32 . . +INF .

model.lst Wed May 30 15:17:17 2018 349


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EQU EqLogP22


33 . . +INF .

34 . . +INF .

35 . . +INF .

36 . . +INF .

47 . . +INF .

48 . . +INF .

49 . . +INF .

50 . . +INF .

51 . . +INF .

55 . . +INF .

56 . . +INF .

57 . 0.1499 +INF .

58 . . +INF .

59 . . +INF .

60 . 0.1499 +INF .

61 . 0.1499 +INF .

62 . . +INF .

63 . . +INF .

64 . . +INF .

65 . 0.1499 +INF .

---- EQU EqLogP23


1 -INF 164.6874 500.0000 .

2 -INF 82.9611 500.0000 .

3 -INF . 500.0000 .

4 -INF 500.0000 500.0000 .

5 -INF 82.9611 500.0000 .

6 -INF 21.8304 500.0000 .

7 -INF 500.0000 500.0000 EPS

12 -INF 500.0000 500.0000 .

25 -INF . 500.0000 .

26 -INF . 500.0000 .

31 -INF . 500.0000 .

32 -INF . 500.0000 .

33 -INF . 500.0000 .

34 -INF 164.6874 500.0000 .

35 -INF 82.9611 500.0000 .

36 -INF 500.0000 500.0000 .

47 -INF 164.6874 500.0000 .

48 -INF 164.6874 500.0000 .

49 -INF . 500.0000 .

50 -INF 82.9611 500.0000 .

51 -INF 130.3798 500.0000 .

55 -INF 82.9611 500.0000 .

56 -INF 21.8304 500.0000 .

57 -INF 500.0000 500.0000 .

model.lst Wed May 30 15:17:17 2018 350


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EQU EqLogP23


58 -INF 164.6874 500.0000 .

59 -INF 82.9611 500.0000 .

60 -INF 500.0000 500.0000 .

61 -INF 500.0000 500.0000 .

62 -INF 164.6874 500.0000 .

63 -INF 44.4117 500.0000 .

64 -INF 21.8304 500.0000 .

65 -INF 500.0000 500.0000 .

---- EQU EqTrP2


1 . . . EPS

2 . . . EPS

3 . . . EPS

4 . . . EPS

5 . . . EPS

6 . . . EPS

7 . . . EPS

8 . . . EPS

10 . . . 1860.3491

11 . . . -1343.2689

12 . . . EPS

13 . . . EPS

14 . . . EPS

15 . . . 1448.9403

25 . . . EPS

26 . . . EPS

31 . . . EPS

32 . . . EPS

33 . . . EPS

34 . . . EPS

35 . . . EPS

36 . . . EPS

37 . . . 851.3267

38 . . . 426.9753

47 . . . EPS

48 . . . EPS

49 . . . EPS

50 . . . EPS

51 . . . EPS

52 . . . EPS

53 . . . EPS

54 . . . 92.0290

55 . . . EPS

56 . . . EPS

57 . . . EPS

58 . . . EPS

model.lst Wed May 30 15:17:17 2018 351


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EQU EqTrP2


59 . . . EPS

60 . . . 13.2754

61 . . . EPS

62 . . . EPS

63 . . . EPS

64 . . . EPS

65 . . . EPS

---- EQU EqLatHtVapP2


1 .H2O . . . EPS

2 .H2O . . . EPS

3 .H2O . . . EPS

4 .H2O . . . EPS

5 .H2O . . . EPS

6 .H2O . . . EPS

7 .H2O . . . EPS

8 .H2O . . . EPS

10.H2O . . . -37.2018

11.H2O . . . 42.7168

12.H2O . . . EPS

13.H2O . . . EPS

14.H2O . . . EPS

15.H2O . . . -46.0772

25.H2O . . . EPS

26.H2O . . . EPS

31.H2O . . . EPS

32.H2O . . . EPS

33.H2O . . . EPS

34.H2O . . . EPS

35.H2O . . . EPS

36.H2O . . . EPS

37.H2O . . . -13.2430

38.H2O . . . -10.7196

47.H2O . . . EPS

48.H2O . . . EPS

49.H2O . . . EPS

50.H2O . . . EPS

51.H2O . . . EPS

52.H2O . . . EPS

53.H2O . . . EPS

54.H2O . . . -1.4316

55.H2O . . . EPS

56.H2O . . . EPS

57.H2O . . . EPS

58.H2O . . . EPS

59.H2O . . . EPS

model.lst Wed May 30 15:17:17 2018 352


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EQU EqLatHtVapP2


60.H2O . . . -0.3333

61.H2O . . . EPS

62.H2O . . . EPS

63.H2O . . . EPS

64.H2O . . . EPS

65.H2O . . . EPS

---- EQU EqEnthSatLiq1


8 . . . EPS

10 . . . EPS

11 . . . -153780.5492

13 . . . EPS

14 . . . EPS

15 . . . 165878.0567

37 . . . EPS

38 . . . 34061.7416

52 . . . EPS

53 . . . EPS

54 . . . 5153.6619

---- EQU EqnTfSatLiqVap


8 . . . EPS

10 . . . EPS

11 . . . EPS

13 . . . EPS

14 . . . EPS

15 . . . 0.4877

16 . . . EPS

37 . . . EPS

38 . . . EPS

52 . . . EPS

53 . . . EPS

54 . . . EPS

---- EQU EqEnthLiqStr


9 -0.0699 -0.0699 -0.0699 EPS

17 -0.0699 -0.0699 -0.0699 -5809.8998

18 -0.0699 -0.0699 -0.0699 EPS

19 -0.0699 -0.0699 -0.0699 EPS

20 -0.0699 -0.0699 -0.0699 -171788.7312

model.lst Wed May 30 15:17:17 2018 353


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---- EQU EqTrLiq


9 . . . EPS

17 . . . -37.4869

18 . . . EPS

19 . . . EPS

20 . . . -1500.5699

---- EQU EqLatHtVapLiq


9 .H2O . . . EPS

17.H2O . . . 1.6139

18.H2O . . . EPS

19.H2O . . . EPS

20.H2O . . . 47.7191

---- EQU EqEnthSatVap


16 -0.0699 -0.0699 -0.0699 833.5581

---- EQU EqEnthSatVap1


16 . . . 833.5581

---- EQU EqCompMolBalHPStmTurb Component mol balance


1.H2 . . . .

1.O2 . . . .

1.N2 . . . .

1.CH4 . . . .

1.CO . . . .

1.CO2 . . . .

1.H2O . . . 0.7505

2.H2 . . . .

2.O2 . . . .

2.N2 . . . .

2.CH4 . . . .

2.CO . . . .

2.CO2 . . . .

2.H2O . . . 0.4693

3.H2 . . . .

3.O2 . . . .

3.N2 . . . .

model.lst Wed May 30 15:17:17 2018 354


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EQU EqCompMolBalHPStmTurb Component mol balance


3.CH4 . . . .

3.CO . . . .

3.CO2 . . . .

3.H2O . . . 0.4693

---- EQU EqInHPPHPStmTurb Equating inlet HP Pressure to that of corresponding HP stream


1 . . . -3.7252

2 . . . 3.4865

3 . . . EPS

---- EQU EqInHPTHPStmTurb Equating inlet HP temperature to that of corresponding HP stream


1 . . . 0.9717

2 . . . -0.9095

3 . . . EPS

---- EQU EqOutMPPHPStmTurb Equatiing outlet MP Pressure to that of corresponding MP stream


1 . . . EPS

2 . . . -7.8447

3 . . . EPS

---- EQU EqOutLPPHPStmTurb Equatiing outlet LP Pressure to that of corresponding LP stream


1 . . . 23.9480

2 . . . EPS

3 . . . EPS

---- EQU EqPTRel1HPStmTurb P T relationship for compression from high to medium pressure


1 . . . -1.1883

2 . . . 1.1122

3 . . . EPS

model.lst Wed May 30 15:17:17 2018 355


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---- EQU EqPTRel1aHPStmTurb


1 . . . EPS

2 . . . -1.1122

3 . . . EPS

---- EQU EqPTRel1bHPStmTurb


1 -530.0000 -530.0000 -530.0000 EPS

2 -530.0000 -530.0000 -530.0000 EPS

3 -530.0000 -530.0000 -530.0000 EPS

---- EQU EqPTRel1cHPStmTurb


1 . . . EPS

2 . . . 1.1122

3 . . . EPS

---- EQU EqPTRel1dHPStmTurb


1 . . . EPS

2 . . . 1.1122

3 . . . EPS

---- EQU EqPTRel1eHPStmTurb


1 . . . EPS

2 . . . 1.1122

3 . . . EPS

---- EQU EqPTRel1fHPStmTurb


1 -INF -132.4505 . .

2 -INF -132.4505 . .

3 -INF . . .

model.lst Wed May 30 15:17:17 2018 356


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---- EQU EqPTRel1gHPStmTurb


1 -INF 701.0000 701.0000 EPS

2 -INF 701.0000 701.0000 .

3 -INF 530.0000 701.0000 .

---- EQU EqPTRel1hHPStmTurb


1 -INF -132.4505 . .

2 -INF -132.4505 . .

3 -INF . . .

---- EQU EqPTRel1iHPStmTurb


1 -INF 701.0000 701.0000 .

2 -INF 701.0000 701.0000 .

3 -INF 530.0000 701.0000 .

---- EQU EqPTRel1jHPStmTurb


1 -INF 701.0000 701.0000 .

2 -INF 701.0000 701.0000 -1.1122

3 -INF 568.5495 701.0000 .

---- EQU EqPTRel1kHPStmTurb


1 -INF -171.0000 . .

2 -INF -171.0000 . .

3 -INF . . EPS

---- EQU EqPTRel2HPStmTurb


1 . . . -1.5419

2 . . . EPS

3 . . . EPS

model.lst Wed May 30 15:17:17 2018 357


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---- EQU EqPTRel2aHPStmTurb


1 . . . 1.5419

2 . . . EPS

3 . . . EPS

---- EQU EqPTRel2bHPStmTurb


1 -460.0000 -460.0000 -460.0000 EPS

2 -460.0000 -460.0000 -460.0000 EPS

3 -460.0000 -460.0000 -460.0000 EPS

---- EQU EqPTRel2cHPStmTurb


1 . . . -1.5419

2 . . . EPS

3 . . . EPS

---- EQU EqPTRel2dHPStmTurb


1 . . . -1.5419

2 . . . EPS

3 . . . EPS

---- EQU EqPTRel2eHPStmTurb


1 . . . EPS

2 . . . EPS

3 . . . EPS

---- EQU EqPTRel2fHPStmTurb


1 -INF -142.8304 . .

2 -INF -142.8304 . .

3 -INF . . .

model.lst Wed May 30 15:17:17 2018 358


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---- EQU EqPTRel2gHPStmTurb


1 -INF 581.0000 581.0000 -1.5419

2 -INF 581.0000 581.0000 .

3 -INF 460.0000 581.0000 .

---- EQU EqPTRel2hHPStmTurb


1 -INF -142.8304 . .

2 -INF -142.8304 . .

3 -INF . . .

---- EQU EqPTRel2iHPStmTurb


1 -INF 581.0000 581.0000 .

2 -INF 581.0000 581.0000 .

3 -INF 460.0000 581.0000 .

---- EQU EqPTRel2jHPStmTurb


1 -INF 581.0000 581.0000 .

2 -INF 581.0000 581.0000 .

3 -INF 438.1696 581.0000 .

---- EQU EqPTRel2kHPStmTurb


1 -INF -121.0000 . .

2 -INF -121.0000 . .

3 -INF . . .

---- EQU EqPTRel2lHPStmTurb


1 . 1.0000 +INF .

2 . 1.0000 +INF .

3 . . +INF .

model.lst Wed May 30 15:17:17 2018 359


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---- EQU EqPTRel2mHPStmTurb


1 . 1.0000 +INF .

2 . . +INF .

3 . . +INF .

---- EQU EqPTRel2nHPStmTurb


1 . 1.0000 +INF .

2 . 1.0000 +INF .

3 . . +INF .

---- EQU EqPTRel3HPStmTurb


1 0.1500 0.1500 0.1500 EPS

2 0.1500 0.1500 0.1500 EPS

3 0.1500 0.1500 0.1500 EPS

---- EQU EqMPWorkHPStmTurb


1 . . . EPS

2 . . . -52.6902

3 . . . -52.6902

---- EQU EqLPWorkHPStmTurb


1 . . . EPS

2 . . . -52.6902

3 . . . -52.6902

---- EQU EqVPWorkHPStmTurb


1 . . . EPS

2 . . . -52.6902

3 . . . -52.6902

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---- EQU EqTotWorkHPStmTurb


1 . . . .

2 . . . -52.6902

3 . . . -52.6902

---- EQU EqWetCnst1HPStmTurb


1 -INF . 0.1500 .

2 -INF . 0.1500 .

3 -INF . 0.1500 .

---- EQU EqWetCnst2HPStmTurb


1 -INF . 0.1500 .

2 -INF 0.1500 0.1500 -82.8973

3 -INF . 0.1500 .

---- EQU EqLogMode1HPStmTurb


1 . . +INF .

2 . . +INF .

3 . . +INF .



1 . . +INF .

2 . . +INF .

3 . . +INF .



1 -INF . 1.0000 .

2 -INF 1.0000 1.0000 .

3 -INF . 1.0000 .

model.lst Wed May 30 15:17:17 2018 361


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1 -INF 1.0000 1.0000 .

2 -INF 1.0000 1.0000 .

3 -INF . 1.0000 .



1 -INF 1.0000 1.0000 .

2 -INF 1.0000 1.0000 .

3 -INF . 1.0000 .



1 -INF . 1.0000 .

2 -INF 1.0000 1.0000 .

3 -INF . 1.0000 .



1 -INF . 1.0000 .

2 -INF 0.1500 1.0000 .

3 -INF . 1.0000 .



1.MPBkPr . . +INF .

1.MPExt . 1.0000 +INF .

1.LPBkPr . 1.0000 +INF .

1.LPExt . 1.0000 +INF .

1.VPCond . 1.0000 +INF .

2.MPBkPr . 1.0000 +INF .

2.MPExt . . +INF .

2.LPBkPr . . +INF .

2.LPExt . 1.0000 +INF .

2.VPCond . 1.0000 +INF .

3.MPBkPr . . +INF .

3.MPExt . . +INF .

3.LPBkPr . . +INF .

3.LPExt . . +INF .

3.VPCond . . +INF .

model.lst Wed May 30 15:17:17 2018 362


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---- EQU EqLogBnd1HPStmTurb


1 -INF -1.000000E+8 . .

2 -INF -0.999979E+8 . .

3 -INF . . -0.0201



1 -INF . . .

2 -INF -0.999991E+8 . .

3 -INF . . .



1 -INF . . .

2 -INF . . -0.2812

3 -INF . . -0.2812



1.1 -INF -1.000000E+8 . .

2.58 -INF -0.999970E+8 . .

3.62 -INF . . .

---- EQU EqCompMolBalMPStmTurb Component mol balance


1.H2 . . . .

1.O2 . . . .

1.N2 . . . .

1.CH4 . . . .

1.CO . . . .

1.CO2 . . . .

1.H2O . . . 0.4542

2.H2 . . . .

2.O2 . . . .

2.N2 . . . .

2.CH4 . . . .

2.CO . . . .

2.CO2 . . . .

2.H2O . . . 0.4542

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---- EQU EqInMPPMPStmTurb Equating inlet HP Pressure to that of corresponding HP stream


1 . . . EPS

2 . . . EPS

---- EQU EqInMPTMPStmTurb Equating inlet HP temperature to that of corresponding HP stream


1 . . . EPS

2 . . . EPS

---- EQU EqOutLPPMPStmTurb Equatiing outlet LP Pressure to that of corresponding LP stream


1 . . . EPS

2 . . . EPS

---- EQU EqPTRel1MPStmTurb


1 . . . EPS

2 . . . EPS

---- EQU EqPTRel1aMPStmTurb


1 . . . EPS

2 . . . EPS

---- EQU EqPTRel1bMPStmTurb


1 -460.0000 -460.0000 -460.0000 EPS

2 -460.0000 -460.0000 -460.0000 EPS

---- EQU EqPTRel1cMPStmTurb


1 . . . EPS

2 . . . EPS

model.lst Wed May 30 15:17:17 2018 364


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---- EQU EqPTRel1dMPStmTurb


1 . . . EPS

2 . . . EPS

---- EQU EqPTRel1eMPStmTurb


1 . . . EPS

2 . . . EPS

---- EQU EqPTRel1fMPStmTurb


1 -INF . . EPS

2 -INF . . .

---- EQU EqPTRel1gMPStmTurb


1 -INF 460.0000 581.0000 .

2 -INF 460.0000 581.0000 .

---- EQU EqPTRel1hMPStmTurb


1 -INF . . .

2 -INF . . .

---- EQU EqPTRel1iMPStmTurb


1 -INF 460.0000 581.0000 .

2 -INF 460.0000 581.0000 .

---- EQU EqPTRel1jMPStmTurb


1 -INF 438.1696 581.0000 .

2 -INF 438.1696 581.0000 .

model.lst Wed May 30 15:17:17 2018 365


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---- EQU EqPTRel1kMPStmTurb


1 -INF . . EPS

2 -INF . . EPS

---- EQU EqPTRel2MPStmTurb


1 0.1500 0.1500 0.1500 EPS

2 0.1500 0.1500 0.1500 EPS

---- EQU EqLPWorkMPStmTurb


1 . . . -52.6902

2 . . . -52.6902

---- EQU EqVPWorkMPStmTurb


1 . . . -52.6902

2 . . . -52.6902

---- EQU EqTotWorkMPStmTurb


1 . . . -52.6902

2 . . . -52.6902

---- EQU EqWetCnst1MPStmTurb


1 -INF . 0.1500 .

2 -INF . 0.1500 .

---- EQU EqLogMode1MPStmTurb


1 . . +INF .

2 . . +INF .

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1 -INF . 1.0000 .

2 -INF . 1.0000 .



1 -INF . 1.0000 .

2 -INF . 1.0000 .



1 -INF . 1.0000 .

2 -INF . 1.0000 .



1.LPBkPr . . +INF .

1.LPExt . . +INF .

1.VPCond . . +INF .

2.LPBkPr . . +INF .

2.LPExt . . +INF .

2.VPCond . . +INF .

---- EQU EqLogBnd1MPStmTurb


1 -INF . . .

2 -INF . . .



1 -INF . . -0.2963

2 -INF . . -0.2963



1.5 -INF . . .

2.55 -INF . . .

model.lst Wed May 30 15:17:17 2018 367


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---- EQU EqCompMolBalVacCondTurb Component mass bal


1.H2 . . . .

1.O2 . . . .

1.N2 . . . .

1.CH4 . . . .

1.CO . . . .

1.CO2 . . . .

1.H2O . . . 0.6412

---- EQU EqEnthBalVacCondTurb Energy balance


1 . . . 1.5917

---- EQU EqMassFCW calculate mass flowrate of cooling water (kg per s)


1 . . . -1.5917

---- EQU EqPr1VacCondTurb equates Vacuum pressure to pressure of inlet stream


1.4 0.2000 0.2000 0.2000 EPS

1.7 0.2000 0.2000 0.2000 EPS

1.57 0.2000 0.2000 0.2000 EPS

1.61 0.2000 0.2000 0.2000 EPS

1.65 0.2000 0.2000 0.2000 EPS

---- EQU EqPr2VacCondTurb equates Vacuum pressure to pressure of outlet stream


1.8 0.2000 0.2000 0.2000 EPS

---- EQU EqWorkPumpVCT Work for vacuum pump in MW (mass is kg per s)


1 . . . 52.6902

---- EQU EqCompMolBalPump Component mass bal


VP .H2 . . . .

VP .O2 . . . .

VP .N2 . . . .

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EQU EqCompMolBalPump Component mass bal


VP .CH4 . . . .

VP .CO . . . .

VP .CO2 . . . .

VP .H2O . . . 0.7665

MP .H2 . . . .

MP .O2 . . . .

MP .N2 . . . .

MP .CH4 . . . .

MP .CO . . . .

MP .CO2 . . . .

MP .H2O . . . 0.0873

HP .H2 . . . .

HP .O2 . . . .

HP .N2 . . . .

HP .CH4 . . . .

HP .CO . . . .

HP .CO2 . . . .

HP .H2O . . . 0.0879

HRSG.H2 . . . .

HRSG.O2 . . . .

HRSG.N2 . . . .

HRSG.CH4 . . . .

HRSG.CO . . . .

HRSG.CO2 . . . .

HRSG.H2O . . . 0.0879

---- EQU EqTEqPump Tin = Tout


VP . . . EPS

MP . . . EPS

HP . . . EPS

HRSG . . . -0.4877

---- EQU EqPgePump Pout >= Pin


VP . 1.2000 +INF .

MP . 18.6000 +INF .

HP . 43.6000 +INF .

HRSG . 43.6000 +INF .

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---- EQU EqWorkPump Work done by pump


VP . . . 52.6902

MP . . . 52.6902

HP . . . 52.6902

HRSG . . . 52.6902

---- EQU EqCompMolBalCondHdr Component mass bal


1.H2 . . . .

1.O2 . . . .

1.N2 . . . .

1.CH4 . . . .

1.CO . . . .

1.CO2 . . . .

1.H2O . . . 0.0839

---- EQU EqPRel1CondHdr Pressure of outlet stream equals the pressure of header


1 1.4000 1.4000 1.4000 -74.9386

---- EQU EqCompMolBalDeAertr


1.H2 . . . .

1.O2 . . . .

1.N2 . . . .

1.CH4 . . . .

1.CO . . . .

1.CO2 . . . .

1.H2O . . . 3.5099

---- EQU EqEnthBalDeAertr


1 . . . 44.1207

---- EQU EqVentVapDeAertr


1 . . . 0.5813

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---- EQU EqPRel1DeAertr


1.16 1.4000 1.4000 1.4000 0.1677

---- EQU EqPRel2DeAertr


1.13 1.4000 1.4000 1.4000 EPS

1.14 1.4000 1.4000 1.4000 EPS

1.15 1.4000 1.4000 1.4000 91.0739

---- EQU EqCompMolBalBlrCmbtr Component mol balance


MP .H2 . . . 0.0046

MP .O2 . . . 0.0038

MP .N2 . . . 0.0044

MP .CH4 . . . 0.9346

MP .CO . . . 1.3986

MP .CO2 . . . 4.9575

MP .H2O . . . 3.0494

HP .H2 . . . 0.0046

HP .O2 . . . 0.0037

HP .N2 . . . 0.0044

HP .CH4 . . . 0.9339

HP .CO . . . 1.3989

HP .CO2 . . . 4.9574

HP .H2O . . . 3.0496

GT .H2 . . . 3.0976

GT .O2 . . . 0.0229

GT .N2 . . . 0.0203

GT .CH4 . . . 11.1880

GT .CO . . . 5.0003

GT .CO2 . . . 4.9633

GT .H2O . . . 3.0526

GTSF.H2 . . . -0.0347

GTSF.O2 . . . -0.0356

GTSF.N2 . . . -0.0349

GTSF.CH4 . . . 0.9000

GTSF.CO . . . 1.3679

GTSF.CO2 . . . 4.9479

GTSF.H2O . . . 3.0286

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---- EQU EqDum1BlrCmbtr Dummy (calculates inlet flow for particular component)


MP .H2 . . . -3.0475

MP .O2 . . . -0.0038

MP .N2 . . . -0.0044

MP .CH4 . . . -11.0488

MP .CO . . . -4.9556

MP .CO2 . . . -4.9575

MP .H2O . . . -3.0494

HP .H2 . . . -3.0477

HP .O2 . . . -0.0037

HP .N2 . . . -0.0044

HP .CH4 . . . -11.0491

HP .CO . . . -4.9556

HP .CO2 . . . -4.9574

HP .H2O . . . -3.0496

GT .H2 . . . -3.0412

GT .O2 . . . -0.0229

GT .N2 . . . -0.0203

GT .CH4 . . . -11.0228

GT .CO . . . -4.9518

GT .CO2 . . . -4.9633

GT .H2O . . . -3.0526

GTSF.H2 . . . -3.0464

GTSF.O2 . . . 0.0356

GTSF.N2 . . . 0.0349

GTSF.CH4 . . . -11.0764

GTSF.CO . . . -4.9658

GTSF.CO2 . . . -4.9479

GTSF.H2O . . . -3.0286

---- EQU EqEgyBalBlrCmbtr Energy balance for combustor


MP . . . 45.4109

HP . . . 45.4184

GT . . . 44.9965

GTSF . . . 45.6928

---- EQU EqOutPBlrCmbtr1 Equality of pressure


MP .29 . . . EPS

MP .30 . . . EPS

HP .27 . . . EPS

HP .28 . . . EPS

GT .40 . . . -5.4366

GT .41 . . . EPS

GTSF.43 . . . EPS

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EQU EqOutPBlrCmbtr1 Equality of pressure


GTSF.44 . . . EPS

---- EQU EqExcessO2BlrCmbtr constraint for excess O2


MP . . +INF .

HP . . +INF .

GT . 3104.3220 +INF .

GTSF . 1633.3912 +INF .

---- EQU EqTCnstrtBlrCmbtr Constraint for maximum allowable temperature


MP -INF 495.5883 1500.0000 .

HP -INF 540.5801 1500.0000 .

GT -INF 1500.0000 1500.0000 -0.5329

GTSF -INF 904.1618 1500.0000 .

---- EQU Eq1AirStr


27 . . . -0.0002

29 . . . -0.0001

39 . . . 0.0004

---- EQU Eq2AirStr


27 1.0133 1.0133 1.0133 EPS

29 1.0133 1.0133 1.0133 EPS

39 1.0133 1.0133 1.0133 -107.3109

---- EQU Eq3AirStr


27 298.1500 298.1500 298.1500 EPS

29 298.1500 298.1500 298.1500 EPS

39 298.1500 298.1500 298.1500 -3.0848

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---- EQU Eq1SyngasStr


28 . . . 0.1834

30 . . . 0.1836

41 . . . 0.1899

44 . . . 0.1847

---- EQU Eq1aSyngasStr


28 . . . -0.3264

30 . . . -0.3267

41 . . . -0.3356

44 . . . -0.3282

---- EQU Eq1bSyngasStr


28 . . . -0.0329

30 . . . -0.0327

41 . . . -0.0153

44 . . . -0.0545

---- EQU Eq2SyngasStr


28 298.1500 298.1500 298.1500 EPS

30 298.1500 298.1500 298.1500 EPS

41 298.1500 298.1500 298.1500 -0.4500

44 298.1500 298.1500 298.1500 -0.0738


---- EQU EqWorkFan . . . 52.6902

---- EQU EqTSat2


MP . . . EPS

HP . . . EPS

LP . . . EPS

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---- EQU EqUBTOpr


MP -INF 82.9611 175.0000 .

HP -INF 164.6874 225.0000 .

LP -INF . 125.0000 .

---- EQU EqLBTOpr


MP . 82.9611 +INF .

HP . 164.6874 +INF .

LP . . +INF .

---- EQU EqCompMolBalPLev


MP.H2 . . . .

MP.O2 . . . .

MP.N2 . . . .

MP.CH4 . . . .

MP.CO . . . .

MP.CO2 . . . .

MP.H2O . . . 0.6825

HP.H2 . . . .

HP.O2 . . . .

HP.N2 . . . .

HP.CH4 . . . .

HP.CO . . . .

HP.CO2 . . . .

HP.H2O . . . 3.6418

LP.H2 . . . .

LP.O2 . . . .

LP.N2 . . . .

LP.CH4 . . . .

LP.CO . . . .

LP.CO2 . . . .

LP.H2O . . . 3.5070

---- EQU EqEgyBalPLev


MP . . . EPS

HP . . . 45.6928

LP . . . 44.1207

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---- EQU EqPRel1PLev


MP.2 . . . EPS

MP.25 . . . EPS

MP.32 . . . EPS

MP.49 . . . EPS

MP.59 . . . 7.8447

MP.63 . . . EPS

HP.26 . . . EPS

HP.31 . . . EPS

HP.47 . . . 0.3600

LP.3 . . . -15.0625

LP.6 . . . EPS

LP.33 . . . EPS

LP.51 . . . EPS

LP.56 . . . EPS

LP.60 . . . 0.5614

LP.64 . . . EPS

---- EQU EqPRel2PLev


MP.5 . . . EPS

MP.35 . . . 7.2625

MP.50 . . . EPS

MP.55 . . . EPS

HP.1 . . . 3.7252

HP.34 . . . 1.7783

HP.48 . . . EPS

HP.58 . . . -3.4865

HP.62 . . . EPS

LP.12 . . . EPS

LP.36 . . . 5.6895

---- EQU EqTRel1PLev


MP.5 . . . EPS

MP.35 . . . EPS

MP.50 . . . EPS

MP.55 . . . EPS

HP.1 . . . -0.9717

HP.34 . . . 0.2840

HP.48 . . . EPS

HP.58 . . . 0.6878

HP.62 . . . EPS

LP.12 . . . EPS

LP.36 . . . EPS

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---- EQU EqGasMolBalBlr


MP .H2 . . . -0.0368

MP .O2 . . . -0.0378

MP .N2 . . . -0.0370

MP .CH4 . . . 0.9498

MP .CO . . . 1.4437

MP .CO2 . . . 5.2225

MP .H2O . . . 3.1966

HP .H2 . . . -0.0349

HP .O2 . . . -0.0358

HP .N2 . . . -0.0351

HP .CH4 . . . 0.8998

HP .CO . . . 1.3677

HP .CO2 . . . 4.9477

HP .H2O . . . 3.0284

HRSG.H2 . . . -0.0347

HRSG.O2 . . . -0.0356

HRSG.N2 . . . -0.0349

HRSG.CH4 . . . 0.9000

HRSG.CO . . . 1.3679

HRSG.CO2 . . . 4.9479

HRSG.H2O . . . 3.0286

---- EQU EqWtrMolBalBlr


MP .H2 . . . .

MP .O2 . . . .

MP .N2 . . . .

MP .CH4 . . . .

MP .CO . . . .

MP .CO2 . . . .

MP .H2O . . . 3.8361

HP .H2 . . . .

HP .O2 . . . .

HP .N2 . . . .

HP .CH4 . . . .

HP .CO . . . .

HP .CO2 . . . .

HP .H2O . . . 3.6418

HRSG.H2 . . . .

HRSG.O2 . . . .

HRSG.N2 . . . .

HRSG.CH4 . . . .

HRSG.CO . . . .

HRSG.CO2 . . . .

HRSG.H2O . . . 3.6418

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---- EQU EqGasEgyBalBlr


MP . . . 48.2307

HP . . . 45.6928

HRSG . . . 45.6928

---- EQU EqWtrEgyBalBlr


MP . . . 48.2307

HP . . . 45.6928

HRSG . . . 45.6928

---- EQU EqBlowdown


MP . . . 0.2264

HP . . . 0.2922

HRSG . . . 0.2922

---- EQU EqRel2Blr


MP 10.0000 10.0000 +INF EPS

HP 10.0000 10.0000 +INF EPS

HRSG 10.0000 208.8944 +INF .

---- EQU EqRel3Blr


MP 10.0000 10.5234 +INF EPS

HP 10.0000 10.5234 +INF EPS

HRSG 10.0000 10.0000 +INF 4.4367

---- EQU EqRel4Blr


MP . . . EPS

HP . . . EPS

HRSG . . . EPS

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---- EQU EqRel5Blr


MP . . . EPS

HP . . . EPS

HRSG . . . 0.0990

---- EQU EqRel6Blr


MP . . . EPS

HP . . . EPS

HRSG . . . 0.2610


---- EQU EqT1 -INF -82.9611 175.0000 .

---- EQU EqT2 -INF -164.6874 225.0000 .

---- EQU EqT3 -INF -1.36424E-12 225.0000 .

---- EQU EqCompMolBalStmDmd


MP.H2 . . . .

MP.O2 . . . .

MP.N2 . . . .

MP.CH4 . . . .

MP.CO . . . .

MP.CO2 . . . .

MP.H2O . . . 0.6825

HP.H2 . . . .

HP.O2 . . . .

HP.N2 . . . .

HP.CH4 . . . .

HP.CO . . . .

HP.CO2 . . . .

HP.H2O . . . 0.7505

LP.H2 . . . .

LP.O2 . . . .

LP.N2 . . . .

LP.CH4 . . . .

LP.CO . . . .

LP.CO2 . . . .

LP.H2O . . . 3.5070

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---- EQU EqEgyBalStmDmd


MP . . . EPS

HP . . . EPS

LP . . . 44.1207

---- EQU EqPRel1StmDmd


MP . . . -7.2625

HP . . . -1.7783

LP . . . -5.6895

---- EQU EqHtReqStmDmd


MP 20.0000 20.0000 +INF 63.3160

HP 5.0000 5.0000 +INF 79.7282

LP 8.0000 8.0000 +INF 49.9873

---- EQU EqPen1StmDmd


MP . . . EPS

HP . . . EPS

LP . . . EPS

---- EQU EqCompMolBalGTCmpr Component mol balance


1.H2 . . . 3.0208

1.O2 . . . 0.0014

1.N2 . . . -0.0004

1.CH4 . . . 11.1511

1.CO . . . 5.1672

1.CO2 . . . 5.7743

1.H2O . . . 3.5451

---- EQU EqOutPGTCmpr Equate outlet P of compressor to that of outlet stream


1 . . . -5.4366

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---- EQU EqOutTGTCmpr Equate outlet T of compressor to that of outlet stream


1 . . . 0.7012

---- EQU EqInPGTCmpr Equate inlet P of compressor to that of inlet stream


1 . . . 107.3109

---- EQU EqInTGTCmpr Equate inlet T of compressor to that of inlet stream


1 . . . -1.4698

---- EQU EqPTRelGTCmpr P-T relationship (adiabatic)


1 . . . 0.7012

---- EQU EqWorkGTCmpr Calculation of work of compression (ideal) (MW)


1 . . . 52.6902

---- EQU EqPRelGtCmpr Pout >= Pin


1 . 18.9868 +INF .

---- EQU EqCompMolBalGTExpdr Component mol balance


1.H2 . . . 3.0201

1.O2 . . . -0.0639

1.N2 . . . -0.0618

1.CH4 . . . 11.1779

1.CO . . . 5.1535

1.CO2 . . . 5.6726

1.H2O . . . 3.4665

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---- EQU EqOutPGTExpdr Equate outlet P of compressor to that of outlet stream


1 . . . EPS

---- EQU EqOutTGTExpdr Equate outlet T of compressor to that of outlet stream


1 . . . 0.7277

---- EQU EqInPGTExpdr Equate inlet P of compressor to that of inlet stream


1 . . . 6.8729

---- EQU EqInTGTExpdr Equate inlet T of compressor to that of inlet stream


1 . . . -0.3693

---- EQU EqPTRelGTExpdr P-T relationship (adiabatic)


1 . . . 0.7277

---- EQU EqWorkGTExpdr Calculation of work of compression (ideal) (MW)


1 . . . -52.6902

---- EQU EqPRelGTExpdr Pout <= Pin


1 -INF -18.7000 . .


---- EQU EqWorkGT . . . -52.6902

---- EQU EqMolBalVlv


HPMP.H2 . . . .

HPMP.O2 . . . .

HPMP.N2 . . . .

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EQU EqMolBalVlv


HPMP.CH4 . . . .

HPMP.CO . . . .

HPMP.CO2 . . . .

HPMP.H2O . . . 0.6825

MPLP.H2 . . . .

MPLP.O2 . . . .

MPLP.N2 . . . .

MPLP.CH4 . . . .

MPLP.CO . . . .

MPLP.CO2 . . . .

MPLP.H2O . . . 3.5070

---- EQU EqEgyBalVlv


HPMP . . . .

MPLP . . . 44.1207


---- EQU Eqstpd2 -INF -4893.7836 . .

---- EQU Eqstpd3 -INF . . .

---- EQU Eqstpd3a -INF . . .

---- EQU Eqstpd4 -INF -30.0000 -30.0000 -52.6902

---- EQU Eqstpd5


1 -10.0000 -10.0000 -10.0000 -52.6902

2 -20.0000 -20.0000 -20.0000 -52.6902

---- EQU Eqstpd6


1 . . . -52.6902

2 . . . -52.6902

---- EQU Eqstpd7


1 . . . EPS

2 . . . 52.6902

3 . . . 52.6902

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---- EQU Eqstpd8


1 . . . 52.6902

2 . . . 52.6902

---- EQU Eqstpd9


1 -INF . . EPS

2 -INF . . EPS

---- EQU Eqstpd10


1 -INF 10.0000 100.0000 .

2 -INF 20.0000 100.0000 .

---- EQU Eqstpd11


1 -INF . . -52.6902

2 -INF -793.4240 . .

3 -INF . . EPS

---- EQU Eqstpd12


1.1 -INF . . -52.6902

1.2 -INF . . -52.6902

2.1 -INF . . .

2.2 -INF . . .

3.1 -INF . . .

3.2 -INF . . .

---- EQU Eqstpd13


1.1 -INF . . .

1.2 -INF . . .

2.1 -INF . . .

2.2 -INF . . EPS

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---- EQU Eqstpd14 -INF 1.0000 1.0000 .

---- EQU Eqstpd15


1 -INF . 1.0000 .

2 -INF . 1.0000 .

---- EQU Eqstpd16


1 -INF . 1.0000 .

2 -INF 1.0000 1.0000 .

3 -INF . 1.0000 .

---- EQU Eqstpd17


1 -INF . 1.0000 .

2 -INF . 1.0000 .


---- EQU obj . . . 1.0000

obj objective function cost in dollar per hr

---- VAR F Flowrate of Stream (kmol per hr)


1 . . 1000000.0000 .

2 . . 1000000.0000 0.0680

3 . . 1000000.0000 .

4 . . 1000000.0000 .

5 . . 1000000.0000 0.0151

6 . . 1000000.0000 .

7 . . 1000000.0000 .

8 . . 1000000.0000 .

9 . . 1000000.0000 .

10 . 2115.4164 1000000.0000 .

11 . 3485.4550 1000000.0000 .

12 . 161.4021 1000000.0000 .

13 . . 1000000.0000 .

14 . . 1000000.0000 .

15 . 3759.6465 1000000.0000 .

16 . 18.8927 1000000.0000 .

17 . 131.6821 1000000.0000 .

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VAR F Flowrate of Stream (kmol per hr)


18 . . 1000000.0000 .

19 . . 1000000.0000 .

20 . 3759.6465 1000000.0000 .

21 . . 1000000.0000 0.0390

22 . . 1000000.0000 .

23 . . 1000000.0000 0.0369

24 . . 1000000.0000 .

25 . . 1000000.0000 .

26 . . 1000000.0000 .

27 . . 1000000.0000 .

28 . . 1000000.0000 .

29 . . 1000000.0000 .

30 . . 1000000.0000 .

31 . . 1000000.0000 .

32 . . 1000000.0000 .

33 . . 1000000.0000 .

34 . 598.0250 1000000.0000 .

35 . 2115.4164 1000000.0000 .

36 . 772.0136 1000000.0000 .

37 . 598.0250 1000000.0000 .

38 . 772.0136 1000000.0000 .

39 . 10681.7773 1000000.0000 .

40 . 10681.7773 1000000.0000 .

41 . 1198.1201 1000000.0000 .

42 . 11370.6963 1000000.0000 .

43 . 11370.6963 1000000.0000 .

44 . 193.4511 1000000.0000 .

45 . 11481.9307 1000000.0000 .

46 . 11481.9307 1000000.0000 .

47 . 3646.8571 1000000.0000 .

48 . . 1000000.0000 .

49 . . 1000000.0000 .

50 . . 1000000.0000 0.0243

51 . . 1000000.0000 .

52 . . 1000000.0000 .

53 . . 1000000.0000 .

54 . 112.7894 1000000.0000 .

55 . . 1000000.0000 0.0151

56 . . 1000000.0000 .

57 . . 1000000.0000 .

58 . 3048.8321 1000000.0000 .

59 . 2115.4164 1000000.0000 .

60 . 933.4157 1000000.0000 .

61 . . 1000000.0000 .

62 . . 1000000.0000 .

63 . . 1000000.0000 .

64 . . 1000000.0000 .

65 . . 1000000.0000 .

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---- VAR Fc Component flowrate of stream


1 .H2 . . . -2.8914

1 .O2 . . . -2.8914

1 .N2 . . . -2.8914

1 .CH4 . . . -2.8914

1 .CO . . . -2.8914

1 .CO2 . . . -2.8914

1 .H2O . . 1000000.0000 .

2 .H2 . . . -0.0680

2 .O2 . . . -0.0680

2 .N2 . . . -0.0680

2 .CH4 . . . -0.0680

2 .CO . . . -0.0680

2 .CO2 . . . -0.0680

2 .H2O . . 1000000.0000 .

3 .H2 . . . 2.9051

3 .O2 . . . 2.9051

3 .N2 . . . 2.9051

3 .CH4 . . . 2.9051

3 .CO . . . 2.9051

3 .CO2 . . . 2.9051

3 .H2O . . 1000000.0000 0.1486

4 .H2 . . . -0.1092

4 .O2 . . . -0.1092

4 .N2 . . . -0.1092

4 .CH4 . . . -0.1092

4 .CO . . . -0.1092

4 .CO2 . . . -0.1092

4 .H2O . . 1000000.0000 .

5 .H2 . . . -0.0151

5 .O2 . . . -0.0151

5 .N2 . . . -0.0151

5 .CH4 . . . -0.0151

5 .CO . . . -0.0151

5 .CO2 . . . -0.0151

5 .H2O . . 1000000.0000 .

6 .H2 . . . 2.8958

6 .O2 . . . 2.8958

6 .N2 . . . 2.8958

6 .CH4 . . . 2.8958

6 .CO . . . 2.8958

6 .CO2 . . . 2.8958

6 .H2O . . 1000000.0000 .

7 .H2 . . . 0.1871

7 .O2 . . . 0.1871

7 .N2 . . . 0.1871

7 .CH4 . . . 0.1871

7 .CO . . . 0.1871

7 .CO2 . . . 0.1871

7 .H2O . . 1000000.0000 .

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VAR Fc Component flowrate of stream


8 .H2 . . . 0.1252

8 .O2 . . . 0.1252

8 .N2 . . . 0.1252

8 .CH4 . . . 0.1252

8 .CO . . . 0.1252

8 .CO2 . . . 0.1252

8 .H2O . . 1000000.0000 .

9 .H2 . . . 3.4705

9 .O2 . . . 3.4705

9 .N2 . . . 3.4705

9 .CH4 . . . 3.4705

9 .CO . . . 3.4705

9 .CO2 . . . 3.4705

9 .H2O . . 1000000.0000 0.7299

10.H2 . . . -0.5986

10.O2 . . . -0.5986

10.N2 . . . -0.5986

10.CH4 . . . -0.5986

10.CO . . . -0.5986

10.CO2 . . . -0.5986

10.H2O . 2115.4164 1000000.0000 .

11.H2 . . . 3.4232

11.O2 . . . 3.4232

11.N2 . . . 3.4232

11.CH4 . . . 3.4232

11.CO . . . 3.4232

11.CO2 . . . 3.4232

11.H2O . 3485.4550 1000000.0000 .

12.H2 . . . EPS

12.O2 . . . EPS

12.N2 . . . EPS

12.CH4 . . . EPS

12.CO . . . EPS

12.CO2 . . . EPS

12.H2O . 161.4021 1000000.0000 .

13.H2 . . . -3.4227

13.O2 . . . -3.4227

13.N2 . . . -3.4227

13.CH4 . . . -3.4227

13.CO . . . -3.4227

13.CO2 . . . -3.4227

13.H2O . . 1000000.0000 .

14.H2 . . . -3.4220

14.O2 . . . -3.4220

14.N2 . . . -3.4220

14.CH4 . . . -3.4220

14.CO . . . -3.4220

14.CO2 . . . -3.4220

14.H2O . . 1000000.0000 .

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15.H2 . . . -3.4220

15.O2 . . . -3.4220

15.N2 . . . -3.4220

15.CH4 . . . -3.4220

15.CO . . . -3.4220

15.CO2 . . . -3.4220

15.H2O . 3759.6465 1000000.0000 .

16.H2 . . . -2.9286

16.O2 . . . -2.9286

16.N2 . . . -2.9286

16.CH4 . . . -2.9286

16.CO . . . -2.9286

16.CO2 . . . -2.9286

16.H2O . 18.8927 1000000.0000 .

17.H2 . . . 3.5070

17.O2 . . . 3.5070

17.N2 . . . 3.5070

17.CH4 . . . 3.5070

17.CO . . . 3.5070

17.CO2 . . . 3.5070

17.H2O . 131.6821 1000000.0000 .

18.H2 . . . 3.7488

18.O2 . . . 3.7488

18.N2 . . . 3.7488

18.CH4 . . . 3.7488

18.CO . . . 3.7488

18.CO2 . . . 3.7488

18.H2O . . 1000000.0000 .

19.H2 . . . 3.5539

19.O2 . . . 3.5539

19.N2 . . . 3.5539

19.CH4 . . . 3.5539

19.CO . . . 3.5539

19.CO2 . . . 3.5539

19.H2O . . 1000000.0000 .

20.H2 . . . 3.5539

20.O2 . . . 3.5539

20.N2 . . . 3.5539

20.CH4 . . . 3.5539

20.CO . . . 3.5539

20.CO2 . . . 3.5539

20.H2O . 3759.6465 1000000.0000 .

21.H2 . . 1000000.0000 .

21.O2 . . 1000000.0000 .

21.N2 . . 1000000.0000 .

21.CH4 . . 1000000.0000 .

21.CO . . 1000000.0000 .

21.CO2 . . 1000000.0000 .

21.H2O . . 1000000.0000 .

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22.H2 . . 1000000.0000 .

22.O2 . . 1000000.0000 .

22.N2 . . 1000000.0000 .

22.CH4 . . 1000000.0000 .

22.CO . . 1000000.0000 .

22.CO2 . . 1000000.0000 .

22.H2O . . 1000000.0000 .

23.H2 . . 1000000.0000 .

23.O2 . . 1000000.0000 .

23.N2 . . 1000000.0000 .

23.CH4 . . 1000000.0000 .

23.CO . . 1000000.0000 .

23.CO2 . . 1000000.0000 .

23.H2O . . 1000000.0000 .

24.H2 . . 1000000.0000 .

24.O2 . . 1000000.0000 .

24.N2 . . 1000000.0000 .

24.CH4 . . 1000000.0000 .

24.CO . . 1000000.0000 .

24.CO2 . . 1000000.0000 .

24.H2O . . 1000000.0000 .

25.H2 . . . -3.1536

25.O2 . . . -3.1536

25.N2 . . . -3.1536

25.CH4 . . . -3.1536

25.CO . . . -3.1536

25.CO2 . . . -3.1536

25.H2O . . 1000000.0000 .

26.H2 . . . EPS

26.O2 . . . EPS

26.N2 . . . EPS

26.CH4 . . . EPS

26.CO . . . EPS

26.CO2 . . . EPS

26.H2O . . 1000000.0000 .

27.H2 . . . -3.0434

27.O2 . . 1000000.0000 .

27.N2 . . 1000000.0000 .

27.CH4 . . . -10.1047

27.CO . . . -3.5568

27.CO2 . . . 0.0115

27.H2O . . . 0.0055

28.H2 . . 1000000.0000 .

28.O2 . . . -0.0037

28.N2 . . . -0.0044

28.CH4 . . 1000000.0000 .

28.CO . . 1000000.0000 .

28.CO2 . . 1000000.0000 .

28.H2O . . . 0.0012

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29.H2 . . . -3.0432

29.O2 . . 1000000.0000 .

29.N2 . . 1000000.0000 .

29.CH4 . . . -10.1045

29.CO . . . -3.5571

29.CO2 . . . 0.0106

29.H2O . . . 0.0052

30.H2 . . 1000000.0000 .

30.O2 . . . -0.0038

30.N2 . . . -0.0044

30.CH4 . . 1000000.0000 .

30.CO . . 1000000.0000 .

30.CO2 . . 1000000.0000 .

30.H2O . . . 0.0009

31.H2 . . . 2.9675

31.O2 . . . 2.9675

31.N2 . . . 2.9675

31.CH4 . . . 2.9675

31.CO . . . 2.9675

31.CO2 . . . 2.9675

31.H2O . . . -0.6743

32.H2 . . . EPS

32.O2 . . . EPS

32.N2 . . . EPS

32.CH4 . . . EPS

32.CO . . . EPS

32.CO2 . . . EPS

32.H2O . . . -0.6825

33.H2 . . . 2.9051

33.O2 . . . 2.9051

33.N2 . . . 2.9051

33.CH4 . . . 2.9051

33.CO . . . 2.9051

33.CO2 . . . 2.9051

33.H2O . . . -0.6019

34.H2 . . . -2.8914

34.O2 . . . -2.8914

34.N2 . . . -2.8914

34.CH4 . . . -2.8914

34.CO . . . -2.8914

34.CO2 . . . -2.8914

34.H2O . 598.0250 1000000.0000 .

35.H2 . . . EPS

35.O2 . . . EPS

35.N2 . . . EPS

35.CH4 . . . EPS

35.CO . . . EPS

35.CO2 . . . EPS

35.H2O . 2115.4164 1000000.0000 .

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36.H2 . . . EPS

36.O2 . . . EPS

36.N2 . . . EPS

36.CH4 . . . EPS

36.CO . . . EPS

36.CO2 . . . EPS

36.H2O . 772.0136 1000000.0000 .

37.H2 . . . -0.6666

37.O2 . . . -0.6666

37.N2 . . . -0.6666

37.CH4 . . . -0.6666

37.CO . . . -0.6666

37.CO2 . . . -0.6666

37.H2O . 598.0250 1000000.0000 .

38.H2 . . . -3.4232

38.O2 . . . -3.4232

38.N2 . . . -3.4232

38.CH4 . . . -3.4232

38.CO . . . -3.4232

38.CO2 . . . -3.4232

38.H2O . 772.0136 1000000.0000 .

39.H2 . . . -3.0208

39.O2 . 2243.1732 1000000.0000 .

39.N2 . 8438.6040 1000000.0000 .

39.CH4 . . . -10.0604

39.CO . . . -3.5495

39.CO2 . . . -0.0149

39.H2O . . . -0.0058

40.H2 . . 1000000.0000 .

40.O2 . 2243.1732 1000000.0000 .

40.N2 . 8438.6040 1000000.0000 .

40.CH4 . . 1000000.0000 .

40.CO . . 1000000.0000 .

40.CO2 . . 1000000.0000 .

40.H2O . . 1000000.0000 .

41.H2 . 658.9660 1000000.0000 .

41.O2 . . . -0.0229

41.N2 . . . -0.0203

41.CH4 . 119.8120 1000000.0000 .

41.CO . 359.4360 1000000.0000 .

41.CO2 . 59.9060 1000000.0000 .

41.H2O . . . -0.0302

42.H2 . . 1000000.0000 .

42.O2 . 1494.3482 1000000.0000 .

42.N2 . 8438.6040 1000000.0000 .

42.CH4 . . 1000000.0000 .

42.CO . . 1000000.0000 .

42.CO2 . 539.1540 1000000.0000 .

42.H2O . 898.5901 1000000.0000 .

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43.H2 . . 1000000.0000 .

43.O2 . 1494.3482 1000000.0000 .

43.N2 . 8438.6040 1000000.0000 .

43.CH4 . . 1000000.0000 .

43.CO . . 1000000.0000 .

43.CO2 . 539.1540 1000000.0000 .

43.H2O . 898.5901 1000000.0000 .

44.H2 . 106.3981 1000000.0000 .

44.O2 . . . 0.0356

44.N2 . . . 0.0349

44.CH4 . 19.3451 1000000.0000 .

44.CO . 58.0353 1000000.0000 .

44.CO2 . 9.6726 1000000.0000 .

44.H2O . . . 0.0406

45.H2 . . 1000000.0000 .

45.O2 . 1373.4412 1000000.0000 .

45.N2 . 8438.6040 1000000.0000 .

45.CH4 . . 1000000.0000 .

45.CO . . 1000000.0000 .

45.CO2 . 626.2070 1000000.0000 .

45.H2O . 1043.6784 1000000.0000 .

46.H2 . . 1000000.0000 .

46.O2 . 1373.4412 1000000.0000 .

46.N2 . 8438.6040 1000000.0000 .

46.CH4 . . 1000000.0000 .

46.CO . . 1000000.0000 .

46.CO2 . 626.2070 1000000.0000 .

46.H2O . 1043.6784 1000000.0000 .

47.H2 . . . EPS

47.O2 . . . EPS

47.N2 . . . EPS

47.CH4 . . . EPS

47.CO . . . EPS

47.CO2 . . . EPS

47.H2O . 3646.8571 1000000.0000 .

48.H2 . . . -2.8914

48.O2 . . . -2.8914

48.N2 . . . -2.8914

48.CH4 . . . -2.8914

48.CO . . . -2.8914

48.CO2 . . . -2.8914

48.H2O . . 1000000.0000 0.0680

49.H2 . . . EPS

49.O2 . . . EPS

49.N2 . . . EPS

49.CH4 . . . EPS

49.CO . . . EPS

49.CO2 . . . EPS

49.H2O . . 1000000.0000 .

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50.H2 . . . 2.8245

50.O2 . . . 2.8245

50.N2 . . . 2.8245

50.CH4 . . . 2.8245

50.CO . . . 2.8245

50.CO2 . . . 2.8245

50.H2O . . 1000000.0000 .

51.H2 . . . EPS

51.O2 . . . EPS

51.N2 . . . EPS

51.CH4 . . . EPS

51.CO . . . EPS

51.CO2 . . . EPS

51.H2O . . 1000000.0000 .

52.H2 . . . -3.8361

52.O2 . . . -3.8361

52.N2 . . . -3.8361

52.CH4 . . . -3.8361

52.CO . . . -3.8361

52.CO2 . . . -3.8361

52.H2O . . 1000000.0000 .

53.H2 . . . -3.6418

53.O2 . . . -3.6418

53.N2 . . . -3.6418

53.CH4 . . . -3.6418

53.CO . . . -3.6418

53.CO2 . . . -3.6418

53.H2O . . 1000000.0000 .

54.H2 . . . -3.6418

54.O2 . . . -3.6418

54.N2 . . . -3.6418

54.CH4 . . . -3.6418

54.CO . . . -3.6418

54.CO2 . . . -3.6418

54.H2O . 112.7894 1000000.0000 .

55.H2 . . . -0.0151

55.O2 . . . -0.0151

55.N2 . . . -0.0151

55.CH4 . . . -0.0151

55.CO . . . -0.0151

55.CO2 . . . -0.0151

55.H2O . . 1000000.0000 .

56.H2 . . . 2.8958

56.O2 . . . 2.8958

56.N2 . . . 2.8958

56.CH4 . . . 2.8958

56.CO . . . 2.8958

56.CO2 . . . 2.8958

56.H2O . . 1000000.0000 .

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57.H2 . . . 0.1871

57.O2 . . . 0.1871

57.N2 . . . 0.1871

57.CH4 . . . 0.1871

57.CO . . . 0.1871

57.CO2 . . . 0.1871

57.H2O . . 1000000.0000 .

58.H2 . . . -2.8914

58.O2 . . . -2.8914

58.N2 . . . -2.8914

58.CH4 . . . -2.8914

58.CO . . . -2.8914

58.CO2 . . . -2.8914

58.H2O . 3048.8321 1000000.0000 .

59.H2 . . . EPS

59.O2 . . . EPS

59.N2 . . . EPS

59.CH4 . . . EPS

59.CO . . . EPS

59.CO2 . . . EPS

59.H2O . 2115.4164 1000000.0000 .

60.H2 . . . 2.9737

60.O2 . . . 2.9737

60.N2 . . . 2.9737

60.CH4 . . . 2.9737

60.CO . . . 2.9737

60.CO2 . . . 2.9737

60.H2O . 933.4157 1000000.0000 .

61.H2 . . . 0.1720

61.O2 . . . 0.1720

61.N2 . . . 0.1720

61.CH4 . . . 0.1720

61.CO . . . 0.1720

61.CO2 . . . 0.1720

61.H2O . . 1000000.0000 .

62.H2 . . . -2.8914

62.O2 . . . -2.8914

62.N2 . . . -2.8914

62.CH4 . . . -2.8914

62.CO . . . -2.8914

62.CO2 . . . -2.8914

62.H2O . . 1000000.0000 .

63.H2 . . . 0.0201

63.O2 . . . 0.0201

63.N2 . . . 0.0201

63.CH4 . . . 0.0201

63.CO . . . 0.0201

63.CO2 . . . 0.0201

63.H2O . . 1000000.0000 .

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64.H2 . . . 2.8958

64.O2 . . . 2.8958

64.N2 . . . 2.8958

64.CH4 . . . 2.8958

64.CO . . . 2.8958

64.CO2 . . . 2.8958

64.H2O . . 1000000.0000 0.0151

65.H2 . . . 0.1720

65.O2 . . . 0.1720

65.N2 . . . 0.1720

65.CH4 . . . 0.1720

65.CO . . . 0.1720

65.CO2 . . . 0.1720

65.H2O . . 1000000.0000 .

---- VAR T Temperature of stream


1 528.0000 695.2674 795.0000 .

2 469.0000 568.5495 701.0000 .

3 414.0000 438.1696 581.0000 .

4 333.0000 333.1730 334.0000 .

5 469.0000 568.5495 701.0000 .

6 414.0000 460.0000 581.0000 .

7 333.0000 333.1730 334.0000 .

8 333.0000 333.1730 334.0000 .

9 333.0000 333.1730 334.0000 .

10 469.0000 485.5883 701.0000 .

11 382.0000 382.4766 383.0000 .

12 414.0000 438.1696 581.0000 .

13 382.0000 382.4766 383.0000 .

14 382.0000 382.4766 383.0000 .

15 382.0000 382.4766 383.0000 .

16 382.0000 382.4766 383.0000 .

17 298.1500 298.1500 298.1500 -0.1122

18 382.0000 382.4766 383.0000 .

19 382.0000 382.4766 383.0000 .

20 382.0000 382.4766 383.0000 .

21 297.0000 540.5801 1501.0000 .

22 297.0000 393.0000 1501.0000 .

23 297.0000 495.5883 1501.0000 .

24 297.0000 393.0000 1501.0000 .

25 469.0000 485.5883 701.0000 .

26 528.0000 530.5801 795.0000 .

27 297.0000 298.1500 1501.0000 .

28 297.0000 298.1500 1501.0000 .

29 297.0000 298.1500 1501.0000 .

30 297.0000 298.1500 1501.0000 .

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VAR T Temperature of stream


31 528.0000 530.5801 795.0000 .

32 469.0000 485.5883 701.0000 .

33 414.0000 438.1696 581.0000 .

34 528.0000 695.2674 795.0000 .

35 469.0000 568.5495 701.0000 .

36 414.0000 438.1696 581.0000 .

37 528.0000 530.5801 795.0000 .

38 414.0000 438.1696 581.0000 .

39 298.0000 298.1500 299.0000 .

40 298.0000 624.9257 704.0000 .

41 298.0000 298.1500 299.0000 .

42 298.0000 1500.0000 1510.0000 .

43 298.0000 761.2915 1510.0000 .

44 298.0000 298.1500 299.0000 .

45 298.0000 904.1618 1510.0000 .

46 298.0000 392.4766 1510.0000 .

47 528.0000 695.2674 795.0000 .

48 528.0000 695.2674 795.0000 .

49 469.0000 485.5883 795.0000 .

50 469.0000 568.5495 701.0000 .

51 414.0000 568.5495 701.0000 .

52 469.0000 485.5883 701.0000 .

53 528.0000 530.5801 795.0000 .

54 528.0000 530.5801 795.0000 .

55 469.0000 568.5495 701.0000 .

56 414.0000 460.0000 581.0000 .

57 333.0000 333.1730 334.0000 .

58 528.0000 695.2674 795.0000 .

59 469.0000 568.5495 701.0000 .

60 414.0000 438.1696 581.0000 .

61 333.0000 333.1730 334.0000 .

62 528.0000 695.2674 795.0000 .

63 469.0000 530.0000 701.0000 .

64 414.0000 460.0000 581.0000 .

65 333.0000 333.1730 334.0000 .

---- VAR P Pressure of stream


1 45.0000 45.0000 80.0000 .

2 15.0000 20.0000 40.0000 .

3 4.0000 7.0000 10.0000 .

4 0.1900 0.2000 0.2100 .

5 15.0000 20.0000 40.0000 .

6 4.0000 7.0000 10.0000 .

7 0.1900 0.2000 0.2100 .

8 0.1900 0.2000 0.2100 .

9 1.4000 1.4000 1.4000 EPS

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VAR P Pressure of stream


10 15.0000 20.0000 40.0000 .

11 1.3900 1.4000 1.4100 .

12 4.0000 7.0000 10.0000 .

13 1.3900 1.4000 1.4100 .

14 1.3900 1.4000 1.4100 .

15 1.3900 1.4000 1.4100 .

16 1.3900 1.4000 1.4100 .

18 15.0000 20.0000 40.0000 .

19 45.0000 45.0000 80.0000 .

20 45.0000 45.0000 80.0000 .

21 0.9500 1.0133 1.1500 .

22 0.9500 1.0133 1.1500 .

23 0.9500 1.0133 1.1500 .

24 0.9500 1.0133 1.1500 .

25 15.0000 20.0000 40.0000 .

26 45.0000 45.0000 80.0000 .

27 0.9500 1.0133 1.1500 .

28 0.9500 1.0133 1.1500 .

29 0.9500 1.0133 1.1500 .

30 0.9500 1.0133 1.1500 .

31 45.0000 45.0000 80.0000 .

32 15.0000 20.0000 40.0000 .

33 4.0000 7.0000 10.0000 .

34 45.0000 45.0000 80.0000 .

35 15.0000 20.0000 40.0000 .

36 4.0000 7.0000 10.0000 .

37 45.0000 45.0000 80.0000 .

38 4.0000 7.0000 10.0000 .

39 0.9900 1.0133 1.1000 .

40 0.9900 20.0000 20.0000 .

41 0.9900 20.0000 20.0000 .

42 0.9900 20.0000 20.0000 -1.4362

43 1.3000 1.3000 20.0000 .

44 1.3000 1.3000 20.0000 .

45 1.3000 1.3000 20.0000 .

46 1.3000 1.3000 20.0000 .

47 45.0000 45.0000 80.0000 .

48 45.0000 45.0000 80.0000 .

49 15.0000 20.0000 40.0000 .

50 15.0000 20.0000 40.0000 .

51 4.0000 7.0000 10.0000 .

52 15.0000 20.0000 40.0000 .

53 45.0000 45.0000 80.0000 .

54 45.0000 45.0000 80.0000 .

55 15.0000 20.0000 40.0000 .

56 4.0000 7.0000 10.0000 .

57 0.1900 0.2000 0.2100 .

58 45.0000 45.0000 80.0000 .

59 15.0000 20.0000 40.0000 .

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VAR P Pressure of stream


60 4.0000 7.0000 10.0000 .

61 0.1900 0.2000 0.2100 .

62 45.0000 45.0000 80.0000 .

63 15.0000 20.0000 40.0000 .

64 4.0000 7.0000 10.0000 .

65 0.1900 0.2000 0.2100 .

---- VAR TrP2


1 . 0.8199 +INF .

2 . 0.7504 +INF .

3 . 0.6771 +INF .

4 . 0.5148 +INF .

5 . 0.7504 +INF .

6 . 0.6771 +INF .

7 . 0.5148 +INF .

8 . 0.5148 +INF .

10 . 0.7504 +INF .

11 . 0.5910 +INF .

12 . 0.6771 +INF .

13 . 0.5910 +INF .

14 . 0.5910 +INF .

15 . 0.5910 +INF .

25 . 0.7504 +INF .

26 . 0.8199 +INF .

31 . 0.8199 +INF .

32 . 0.7504 +INF .

33 . 0.6771 +INF .

34 . 0.8199 +INF .

35 . 0.7504 +INF .

36 . 0.6771 +INF .

37 . 0.8199 +INF .

38 . 0.6771 +INF .

47 . 0.8199 +INF .

48 . 0.8199 +INF .

49 . 0.7504 +INF .

50 . 0.7504 +INF .

51 . 0.6771 +INF .

52 . 0.7504 +INF .

53 . 0.8199 +INF .

54 . 0.8199 +INF .

55 . 0.7504 +INF .

56 . 0.6771 +INF .

57 . 0.5148 +INF .

58 . 0.8199 +INF .

59 . 0.7504 +INF .

60 . 0.6771 +INF .

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VAR TrP2


61 . 0.5148 +INF .

62 . 0.8199 +INF .

63 . 0.7504 +INF .

64 . 0.6771 +INF .

65 . 0.5148 +INF .

---- VAR LatHtVapP2


1 .H2O 25.0000 30.1021 50.0000 .

2 .H2O 25.0000 34.0393 50.0000 .

3 .H2O 25.0000 37.3088 50.0000 .

4 .H2O 25.0000 42.5369 50.0000 .

5 .H2O 25.0000 34.0393 50.0000 .

6 .H2O 25.0000 37.3088 50.0000 .

7 .H2O 25.0000 42.5369 50.0000 .

8 .H2O 25.0000 42.5369 50.0000 .

10.H2O 25.0000 34.0393 50.0000 .

11.H2O 25.0000 40.3543 50.0000 .

12.H2O 25.0000 37.3088 50.0000 .

13.H2O 25.0000 40.3543 50.0000 .

14.H2O 25.0000 40.3543 50.0000 .

15.H2O 25.0000 40.3543 50.0000 .

25.H2O 25.0000 34.0393 50.0000 .

26.H2O 25.0000 30.1021 50.0000 .

31.H2O 25.0000 30.1021 50.0000 .

32.H2O 25.0000 34.0393 50.0000 .

33.H2O 25.0000 37.3088 50.0000 .

34.H2O 25.0000 30.1021 50.0000 .

35.H2O 25.0000 34.0393 50.0000 .

36.H2O 25.0000 37.3088 50.0000 .

37.H2O 25.0000 30.1021 50.0000 .

38.H2O 25.0000 37.3088 50.0000 .

47.H2O 25.0000 30.1021 50.0000 .

48.H2O 25.0000 30.1021 50.0000 .

49.H2O 25.0000 34.0393 50.0000 .

50.H2O 25.0000 34.0393 50.0000 .

51.H2O 25.0000 37.3088 50.0000 .

52.H2O 25.0000 34.0393 50.0000 .

53.H2O 25.0000 30.1021 50.0000 .

54.H2O 25.0000 30.1021 50.0000 .

55.H2O 25.0000 34.0393 50.0000 .

56.H2O 25.0000 37.3088 50.0000 .

57.H2O 25.0000 42.5369 50.0000 .

58.H2O 25.0000 30.1021 50.0000 .

59.H2O 25.0000 34.0393 50.0000 .

60.H2O 25.0000 37.3088 50.0000 .

61.H2O 25.0000 42.5369 50.0000 .

model.lst Wed May 30 15:17:17 2018 400


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VAR LatHtVapP2


62.H2O 25.0000 30.1021 50.0000 .

63.H2O 25.0000 34.0393 50.0000 .

64.H2O 25.0000 37.3088 50.0000 .

65.H2O 25.0000 42.5369 50.0000 .

---- VAR Wetns


1 . . 1.0000 .

2 . . 1.0000 EPS

3 . . 1.0000 EPS

4 . 0.1500 1.0000 .

5 . . 1.0000 .

6 . . 1.0000 EPS

7 . 0.1500 1.0000 .

12 . 0.8670 1.0000 .

25 . . 1.0000 EPS

26 . . 1.0000 EPS

31 . . 1.0000 .

32 . . 1.0000 .

33 . . 1.0000 .

34 . . 1.0000 .

35 . . 1.0000 .

36 . 0.0001 1.0000 .

47 . . 1.0000 .

48 . . 1.0000 EPS

49 . . 1.0000 .

50 . . 1.0000 EPS

51 . . 1.0000 EPS

55 . . 1.0000 EPS

56 . . 1.0000 EPS

57 . 0.1500 1.0000 .

58 . . 1.0000 213.9481

59 . . 1.0000 .

60 . 0.1500 1.0000 .

61 . 0.1500 1.0000 .

62 . . 1.0000 EPS

63 . . 1.0000 .

64 . . 1.0000 .

65 . 0.1500 1.0000 .

---- VAR TSat


1 528.0000 530.5801 570.0000 .

2 469.0000 485.5883 526.0000 .

3 414.0000 438.1696 456.0000 .

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VAR TSat


4 333.0000 333.1730 334.0000 .

5 469.0000 485.5883 526.0000 .

6 414.0000 438.1696 456.0000 .

7 333.0000 333.1730 334.0000 .

8 333.0000 333.1730 334.0000 .

10 469.0000 485.5883 526.0000 .

11 382.0000 382.4766 383.0000 .

12 414.0000 438.1696 456.0000 .

13 382.0000 382.4766 383.0000 .

14 382.0000 382.4766 383.0000 .

15 382.0000 382.4766 383.0000 .

16 382.0000 382.4766 383.0000 .

25 469.0000 485.5883 526.0000 .

26 528.0000 530.5801 570.0000 .

31 528.0000 530.5801 570.0000 .

32 469.0000 485.5883 526.0000 .

33 414.0000 438.1696 456.0000 .

34 528.0000 530.5801 570.0000 .

35 469.0000 485.5883 526.0000 .

36 414.0000 438.1696 456.0000 .

37 528.0000 530.5801 570.0000 .

38 414.0000 438.1696 456.0000 .

47 528.0000 530.5801 570.0000 .

48 528.0000 530.5801 570.0000 .

49 469.0000 485.5883 526.0000 .

50 469.0000 485.5883 526.0000 .

51 414.0000 438.1696 456.0000 .

52 469.0000 485.5883 526.0000 .

53 528.0000 530.5801 570.0000 .

54 528.0000 530.5801 570.0000 .

55 469.0000 485.5883 526.0000 .

56 414.0000 438.1696 456.0000 .

57 333.0000 333.1730 334.0000 .

58 528.0000 530.5801 570.0000 .

59 469.0000 485.5883 526.0000 .

60 414.0000 438.1696 456.0000 .

61 333.0000 333.1730 334.0000 .

62 528.0000 530.5801 570.0000 .

63 469.0000 485.5883 526.0000 .

64 414.0000 438.1696 456.0000 .

65 333.0000 333.1730 334.0000 .

---- VAR TrLiq


9 . 0.5148 +INF .

17 . 0.4607 +INF .

18 . 0.5910 +INF .

model.lst Wed May 30 15:17:17 2018 402


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VAR TrLiq


19 . 0.5910 +INF .

20 . 0.5910 +INF .

---- VAR LatHtVapLiq


9 .H2O 25.0000 42.5369 50.0000 .

17.H2O 25.0000 43.8694 50.0000 .

18.H2O 25.0000 40.3543 50.0000 .

19.H2O 25.0000 40.3543 50.0000 .

20.H2O 25.0000 40.3543 50.0000 .

---- VAR Y Binary variable


1 . 1.0000 1.0000 0.0010

5 . . 1.0000 0.0010

55 . . 1.0000 0.0010

58 . 1.0000 1.0000 779.6424

62 . . 1.0000 0.0010

---- VAR YP2 binary variable for 2 phase water streams


1 . . . 0.0010

2 . . 1.0000 0.0010

3 . . 1.0000 0.0010

4 1.0000 1.0000 1.0000 0.0010

5 . . 1.0000 0.0010

6 . . 1.0000 0.0010

7 1.0000 1.0000 1.0000 0.0010

12 . 1.0000 1.0000 0.0010

25 . . . 0.0010

26 . . . 0.0010

31 . . . 0.0010

32 . . 1.0000 0.0010

33 . . 1.0000 0.0010

34 . . . -274.0338

35 . . 1.0000 0.0010

36 . 1.0000 1.0000 0.0010

47 . . . 0.0010

48 . . . 0.0010

49 . . 1.0000 0.0010

50 . . 1.0000 0.0010

51 . . 1.0000 0.0010

55 . . 1.0000 0.0010

model.lst Wed May 30 15:17:17 2018 403


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VAR YP2 binary variable for 2 phase water streams


56 . . 1.0000 0.0010

57 1.0000 1.0000 1.0000 0.0010

58 . . . 0.0010

59 . . 1.0000 -1145.0401

60 . 1.0000 1.0000 0.0010

61 1.0000 1.0000 1.0000 0.0010

62 . . . 0.0010

63 . . 1.0000 0.0010

64 . . 1.0000 0.0010

65 1.0000 1.0000 1.0000 0.0010

---- VAR H Enthalpy of stream


1 -0.0900 -0.0633 . .

2 -0.0900 -0.0646 . .

3 -0.0900 -0.0658 . .

4 -0.0900 -0.0686 . .

5 -0.0900 -0.0646 . .

6 -0.0900 -0.0656 . .

7 -0.0900 -0.0686 . .

8 -0.0900 -0.0787 . .

9 -0.0900 -0.0787 . .

10 -0.0900 -0.0748 . .

11 -0.0900 -0.0776 . .

12 -0.0900 -0.0748 . .

13 -0.0900 -0.0776 . .

14 -0.0900 -0.0776 . .

15 -0.0900 -0.0776 . .

16 -0.0900 -0.0664 . .

17 -0.0900 -0.0794 . .

18 -0.0900 -0.0776 . .

19 -0.0900 -0.0776 . .

20 -0.0900 -0.0776 . .

25 -0.0900 -0.0654 . .

26 -0.0900 -0.0649 . .

31 -0.0900 -0.0649 . EPS

32 -0.0900 -0.0654 . EPS

33 -0.0900 -0.0658 . .

34 -0.0900 -0.0633 . .

35 -0.0900 -0.0646 . .

36 -0.0900 -0.0658 . .

37 -0.0900 -0.0733 . .

38 -0.0900 -0.0762 . .

47 -0.0900 -0.0633 . .

48 -0.0900 -0.0633 . .

49 -0.0900 -0.0654 . EPS

50 -0.0900 -0.0646 . .

model.lst Wed May 30 15:17:17 2018 404


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VAR H Enthalpy of stream


51 -0.0900 -0.0646 . .

52 -0.0900 -0.0748 . .

53 -0.0900 -0.0733 . .

54 -0.0900 -0.0733 . .

55 -0.0900 -0.0646 . .

56 -0.0900 -0.0656 . EPS

57 -0.0900 -0.0686 . .

58 -0.0900 -0.0633 . .

59 -0.0900 -0.0646 . .

60 -0.0900 -0.0674 . .

61 -0.0900 -0.0686 . .

62 -0.0900 -0.0633 . .

63 -0.0900 -0.0650 . .

64 -0.0900 -0.0656 . EPS

65 -0.0900 -0.0686 . .

---- VAR HVap


1 -0.0900 -0.0633 . .

2 -0.0900 -0.0646 . .

3 -0.0900 -0.0658 . .

4 -0.0900 -0.0668 . .

5 -0.0900 -0.0646 . .

6 -0.0900 -0.0656 . .

7 -0.0900 -0.0668 . .

12 -0.0900 -0.0658 . .

25 -0.0900 -0.0654 . .

26 -0.0900 -0.0649 . .

31 -0.0900 -0.0649 . .

32 -0.0900 -0.0654 . .

33 -0.0900 -0.0658 . .

34 -0.0900 -0.0633 . .

35 -0.0900 -0.0646 . .

36 -0.0900 -0.0658 . .

47 -0.0900 -0.0633 . .

48 -0.0900 -0.0633 . .

49 -0.0900 -0.0654 . .

50 -0.0900 -0.0646 . .

51 -0.0900 -0.0646 . EPS

55 -0.0900 -0.0646 . .

56 -0.0900 -0.0656 . .

57 -0.0900 -0.0668 . .

58 -0.0900 -0.0633 . .

59 -0.0900 -0.0646 . .

60 -0.0900 -0.0658 . .

61 -0.0900 -0.0668 . .

62 -0.0900 -0.0633 . .

model.lst Wed May 30 15:17:17 2018 405


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VAR HVap


63 -0.0900 -0.0650 . .

64 -0.0900 -0.0656 . .

65 -0.0900 -0.0668 . .

---- VAR HSatLiq


1 -0.0900 -0.0733 . .

2 -0.0900 -0.0748 . .

3 -0.0900 -0.0762 . .

4 -0.0900 -0.0787 . .

5 -0.0900 -0.0748 . .

6 -0.0900 -0.0762 . .

7 -0.0900 -0.0787 . .

8 -0.0900 -0.0787 . .

10 -0.0900 -0.0748 . .

11 -0.0900 -0.0776 . .

12 -0.0900 -0.0762 . .

13 -0.0900 -0.0776 . .

14 -0.0900 -0.0776 . .

15 -0.0900 -0.0776 . .

25 -0.0900 -0.0748 . .

26 -0.0900 -0.0733 . .

31 -0.0900 -0.0733 . .

32 -0.0900 -0.0748 . .

33 -0.0900 -0.0762 . .

34 -0.0900 -0.0733 . .

35 -0.0900 -0.0748 . .

36 -0.0900 -0.0762 . .

37 -0.0900 -0.0733 . .

38 -0.0900 -0.0762 . .

47 -0.0900 -0.0733 . .

48 -0.0900 -0.0733 . .

49 -0.0900 -0.0748 . .

50 -0.0900 -0.0748 . .

51 -0.0900 -0.0762 . .

52 -0.0900 -0.0748 . .

53 -0.0900 -0.0733 . .

54 -0.0900 -0.0733 . .

55 -0.0900 -0.0748 . .

56 -0.0900 -0.0762 . .

57 -0.0900 -0.0787 . .

58 -0.0900 -0.0733 . .

59 -0.0900 -0.0748 . .

60 -0.0900 -0.0762 . .

61 -0.0900 -0.0787 . .

62 -0.0900 -0.0733 . .

63 -0.0900 -0.0748 . .

model.lst Wed May 30 15:17:17 2018 406


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VAR HSatLiq


64 -0.0900 -0.0762 . .

65 -0.0900 -0.0787 . .

---- VAR HSatVap


16 -0.0900 -0.0664 . .

---- VAR Hc


21.H2 -0.0010 0.0020 0.0110 .

21.O2 -0.0010 0.0020 0.0120 .

21.N2 -0.0010 0.0020 0.0120 .

21.CH4 -0.0220 -0.0179 0.0026 .

21.CO -0.0320 -0.0287 -0.0193 .

21.CO2 -0.1100 -0.1065 -0.0913 .

21.H2O -0.0680 -0.0648 -0.0530 .

22.H2 -0.0010 0.0008 0.0110 .

22.O2 -0.0010 0.0008 0.0120 .

22.N2 -0.0010 0.0008 0.0120 .

22.CH4 -0.0220 -0.0197 0.0026 .

22.CO -0.0320 -0.0299 -0.0193 .

22.CO2 -0.1100 -0.1083 -0.0913 .

22.H2O -0.0680 -0.0663 -0.0530 .

23.H2 -0.0010 0.0016 0.0110 .

23.O2 -0.0010 0.0017 0.0120 .

23.N2 -0.0010 0.0016 0.0120 .

23.CH4 -0.0220 -0.0185 0.0026 .

23.CO -0.0320 -0.0291 -0.0193 .

23.CO2 -0.1100 -0.1071 -0.0913 .

23.H2O -0.0680 -0.0653 -0.0530 .

24.H2 -0.0010 0.0008 0.0110 .

24.O2 -0.0010 0.0008 0.0120 .

24.N2 -0.0010 0.0008 0.0120 .

24.CH4 -0.0220 -0.0197 0.0026 .

24.CO -0.0320 -0.0299 -0.0193 .

24.CO2 -0.1100 -0.1083 -0.0913 .

24.H2O -0.0680 -0.0663 -0.0530 .

27.H2 -0.0010 . 0.0110 .

27.O2 -0.0010 . 0.0120 .

27.N2 -0.0010 . 0.0120 .

27.CH4 -0.0220 -0.0207 0.0026 .

27.CO -0.0320 -0.0307 -0.0193 .

27.CO2 -0.1100 -0.1093 -0.0913 .

27.H2O -0.0680 -0.0672 -0.0530 .

28.H2 -0.0010 . 0.0110 .

model.lst Wed May 30 15:17:17 2018 407


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VAR Hc


28.O2 -0.0010 . 0.0120 .

28.N2 -0.0010 . 0.0120 .

28.CH4 -0.0220 -0.0207 0.0026 .

28.CO -0.0320 -0.0307 -0.0193 .

28.CO2 -0.1100 -0.1093 -0.0913 .

28.H2O -0.0680 -0.0672 -0.0530 .

29.H2 -0.0010 . 0.0110 .

29.O2 -0.0010 . 0.0120 .

29.N2 -0.0010 . 0.0120 .

29.CH4 -0.0220 -0.0207 0.0026 .

29.CO -0.0320 -0.0307 -0.0193 .

29.CO2 -0.1100 -0.1093 -0.0913 .

29.H2O -0.0680 -0.0672 -0.0530 .

30.H2 -0.0010 . 0.0110 .

30.O2 -0.0010 . 0.0120 .

30.N2 -0.0010 . 0.0120 .

30.CH4 -0.0220 -0.0207 0.0026 .

30.CO -0.0320 -0.0307 -0.0193 .

30.CO2 -0.1100 -0.1093 -0.0913 .

30.H2O -0.0680 -0.0672 -0.0530 .

39.H2 -0.0010 . 0.0110 .

39.O2 -0.0010 . 0.0120 .

39.N2 -0.0010 . 0.0120 .

39.CH4 -0.0220 -0.0207 0.0026 .

39.CO -0.0320 -0.0307 -0.0193 .

39.CO2 -0.1100 -0.1093 -0.0913 .

39.H2O -0.0680 -0.0672 -0.0530 .

40.H2 -0.0010 0.0026 0.0110 .

40.O2 -0.0010 0.0028 0.0120 .

40.N2 -0.0010 0.0027 0.0120 .

40.CH4 -0.0220 -0.0167 0.0026 .

40.CO -0.0320 -0.0280 -0.0193 .

40.CO2 -0.1100 -0.1054 -0.0913 .

40.H2O -0.0680 -0.0640 -0.0530 .

41.H2 -0.0010 . 0.0110 .

41.O2 -0.0010 . 0.0120 .

41.N2 -0.0010 . 0.0120 .

41.CH4 -0.0220 -0.0207 0.0026 .

41.CO -0.0320 -0.0307 -0.0193 .

41.CO2 -0.1100 -0.1093 -0.0913 .

41.H2O -0.0680 -0.0672 -0.0530 .

42.H2 -0.0010 0.0101 0.0110 .

42.O2 -0.0010 0.0113 0.0120 .

42.N2 -0.0010 0.0107 0.0120 .

42.CH4 -0.0220 0.0013 0.0026 .

42.CO -0.0320 -0.0199 -0.0193 .

42.CO2 -0.1100 -0.0922 -0.0913 .

42.H2O -0.0680 -0.0538 -0.0530 .

43.H2 -0.0010 0.0038 0.0110 .

model.lst Wed May 30 15:17:17 2018 408


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VAR Hc


43.O2 -0.0010 0.0040 0.0120 .

43.N2 -0.0010 0.0038 0.0120 .

43.CH4 -0.0220 -0.0145 0.0026 .

43.CO -0.0320 -0.0268 -0.0193 .

43.CO2 -0.1100 -0.1036 -0.0913 .

43.H2O -0.0680 -0.0626 -0.0530 .

44.H2 -0.0010 . 0.0110 .

44.O2 -0.0010 . 0.0120 .

44.N2 -0.0010 . 0.0120 .

44.CH4 -0.0220 -0.0207 0.0026 .

44.CO -0.0320 -0.0307 -0.0193 .

44.CO2 -0.1100 -0.1093 -0.0913 .

44.H2O -0.0680 -0.0672 -0.0530 .

45.H2 -0.0010 0.0049 0.0110 .

45.O2 -0.0010 0.0054 0.0120 .

45.N2 -0.0010 0.0051 0.0120 .

45.CH4 -0.0220 -0.0119 0.0026 .

45.CO -0.0320 -0.0256 -0.0193 .

45.CO2 -0.1100 -0.1015 -0.0913 .

45.H2O -0.0680 -0.0610 -0.0530 .

46.H2 -0.0010 0.0008 0.0110 .

46.O2 -0.0010 0.0008 0.0120 .

46.N2 -0.0010 0.0008 0.0120 .

46.CH4 -0.0220 -0.0197 0.0026 .

46.CO -0.0320 -0.0299 -0.0193 .

46.CO2 -0.1100 -0.1083 -0.0913 .

46.H2O -0.0680 -0.0663 -0.0530 .

---- VAR InHPPHPStmTurb Inlet HP Pressure for expander of HP Steam turbine


1 45.0000 45.0000 80.0000 .

2 45.0000 45.0000 80.0000 .

3 45.0000 45.0000 80.0000 .

---- VAR InHPTHPStmTurb Inlet HP Temperature for expander of HP Steam turbine


1 528.0000 695.2674 795.0000 .

2 528.0000 695.2674 795.0000 .

3 528.0000 695.2674 795.0000 .

model.lst Wed May 30 15:17:17 2018 409


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---- VAR OutMPPHPStmTurb Outlet MP Pressure for expander of HP Steam turbine


1 15.0000 20.0000 40.0000 .

2 15.0000 20.0000 40.0000 .

3 15.0000 20.0000 40.0000 .

---- VAR OutLPPHPStmTurb Outlet LP Pressure for expander of HP Steam turbine


1 4.0000 7.0000 10.0000 .

2 4.0000 7.0000 10.0000 .

3 4.0000 7.0000 10.0000 .

---- VAR OutMPTHPStmTurb Outlet MP Temperature for expander of HP Steam turbine


1 273.0000 568.5495 701.0000 .

2 273.0000 568.5495 701.0000 .

3 273.0000 568.5495 701.0000 .

---- VAR OutLPTHPStmTurb Outlet LP Temperature for expander of HP Steam turbine


1 273.0000 438.1696 581.0000 .

2 273.0000 438.1696 581.0000 .

3 273.0000 438.1696 581.0000 .

---- VAR MPWorkHPStmTurb MP expnasion work of HP Steam turbine


1 . . +INF .

2 . 3.9336 +INF .

3 . . +INF .

---- VAR LPWorkHPStmTurb LP expnasion work of HP Steam turbine


1 . . +INF .

2 . 2.6424 +INF .

3 . . +INF .

model.lst Wed May 30 15:17:17 2018 410


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---- VAR VPWorkHPStmTurb VP expnasion work of HP Steam turbine


1 . . +INF .

2 . . +INF .

3 . . +INF .

---- VAR TotWorkHPStmTurb Total work of HP Steam turbine


1 . . +INF .

2 . 6.5760 +INF .

3 . . +INF .

---- VAR Dum1HPStmTurb


1 . 438.1696 +INF .

2 . 438.1696 +INF .

3 . . +INF EPS



1 . . +INF 1.5419

2 . . +INF EPS

3 . 438.1696 +INF .



1 . 460.0000 +INF .

2 . 460.0000 +INF .

3 . . +INF EPS



1 . . +INF .

2 . . +INF .

3 . 460.0000 +INF .

model.lst Wed May 30 15:17:17 2018 411


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1 . 438.1696 +INF .

2 . 438.1696 +INF .

3 . . +INF .



1 . . +INF .

2 . . +INF .

3 . 460.0000 +INF .



1 . 568.5495 +INF .

2 . 568.5495 +INF .

3 . . +INF .



1 . . +INF EPS

2 . . +INF .

3 . 568.5495 +INF .



1 . 530.0000 +INF .

2 . 530.0000 +INF .

3 . . +INF .



1 . . +INF .

2 . . +INF 1.1122

3 . 530.0000 +INF .

model.lst Wed May 30 15:17:17 2018 412


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1 . 568.5495 +INF .

2 . 568.5495 +INF .

3 . . +INF EPS



1 . . +INF .

2 . . +INF .

3 . 530.0000 +INF .

---- VAR YModeHPStmTurb


1.MPBkPr . 1.0000 1.0000 0.0010

1.MPExt . . 1.0000 0.0010

1.LPBkPr . . 1.0000 0.0010

1.LPExt . . 1.0000 0.0010

1.VPCond . . 1.0000 0.0010

2.MPBkPr . . 1.0000 EPS

2.MPExt . 1.0000 1.0000 EPS

2.LPBkPr . 1.0000 1.0000 EPS

2.LPExt . . 1.0000 EPS

2.VPCond . . 1.0000 -2.811754E+7

3.MPBkPr . . 1.0000 -2.014906E+6

3.MPExt . . 1.0000 -2.014906E+6

3.LPBkPr . . 1.0000 EPS

3.LPExt . . 1.0000 EPS

3.VPCond . . 1.0000 -2.811754E+7

---- VAR YLP


1 . 1.0000 1.0000 895.8567

2 . 1.0000 1.0000 EPS

3 . . 1.0000 EPS

---- VAR InMPPMPStmTurb Inlet MP Pressure for expander of MP Steam turbine


1 15.0000 20.0000 40.0000 .

2 15.0000 20.0000 40.0000 .

model.lst Wed May 30 15:17:17 2018 413


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---- VAR InMPTMPStmTurb Inlet MP Temperature for expander of MP Steam turbine


1 469.0000 568.5495 701.0000 .

2 469.0000 568.5495 701.0000 .

---- VAR OutLPPMPStmTurb Outlet LP Pressure for expander of MP Steam turbine


1 4.0000 7.0000 10.0000 .

2 4.0000 7.0000 10.0000 .

---- VAR OutLPTMPStmTurb Outlet LP Temperature for expander of HP Steam turbine


1 273.0000 438.1696 581.0000 .

2 273.0000 438.1696 581.0000 .

---- VAR LPWorkMPStmTurb LP expnasion work of MP Steam turbine


1 . . +INF .

2 . . +INF .

---- VAR VPWorkMPStmTurb VP expnasion work of HP Steam turbine


1 . . +INF .

2 . . +INF .

---- VAR TotWorkMPStmTurb Total work of HP Steam turbine


1 . . +INF .

2 . . +INF .

---- VAR Dum11MPStmTurb


1 . . +INF .

2 . . +INF .

model.lst Wed May 30 15:17:17 2018 414


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1 . 438.1696 +INF .

2 . 438.1696 +INF .



1 . . +INF .

2 . . +INF .



1 . 460.0000 +INF .

2 . 460.0000 +INF .



1 . . +INF .

2 . . +INF EPS



1 . 460.0000 +INF .

2 . 460.0000 +INF .

---- VAR YModeMPStmTurb


1.LPBkPr . . 1.0000 0.0010

1.LPExt . . 1.0000 0.0010

1.VPCond . . 1.0000 -2.963009E+7

2.LPBkPr . . 1.0000 EPS

2.LPExt . . 1.0000 EPS

2.VPCond . . 1.0000 -2.963009E+7

---- VAR HtLdVacCondTurb


1 . . +INF .

model.lst Wed May 30 15:17:17 2018 415


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---- VAR MassFCW . . +INF .

---- VAR WorkPumpV˜ . . +INF .

---- VAR WorkPump


VP . . +INF .

MP . . +INF .

HP . . +INF .

HRSG . 0.0820 +INF .

---- VAR Dum1BlrCmbtr


MP .H2 . . +INF .

MP .O2 . . +INF .

MP .N2 . . +INF .

MP .CH4 . . +INF .

MP .CO . . +INF .

MP .CO2 . . +INF .

MP .H2O . . +INF .

HP .H2 . . +INF .

HP .O2 . . +INF .

HP .N2 . . +INF .

HP .CH4 . . +INF .

HP .CO . . +INF .

HP .CO2 . . +INF .

HP .H2O . . +INF .

GT .H2 . 658.9660 +INF .

GT .O2 . 2243.1732 +INF .

GT .N2 . 8438.6040 +INF .

GT .CH4 . 119.8120 +INF .

GT .CO . 359.4360 +INF .

GT .CO2 . 59.9060 +INF .

GT .H2O . . +INF .

GTSF.H2 . 106.3981 +INF .

GTSF.O2 . 1494.3482 +INF .

GTSF.N2 . 8438.6040 +INF .

GTSF.CH4 . 19.3451 +INF .

GTSF.CO . 58.0353 +INF .

GTSF.CO2 . 548.8266 +INF .

GTSF.H2O . 898.5901 +INF .

model.lst Wed May 30 15:17:17 2018 416


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---- VAR QBlr Heat exchanged


MP . . +INF .

HP . . +INF .

HRSG . 52.6620 +INF .

---- VAR POpr operating pressure of header


MP 20.0000 20.0000 20.0000 15.1072

HP 45.0000 45.0000 45.0000 2.3771

LP 7.0000 7.0000 7.0000 -8.8115

---- VAR TOpr operating temperature of header


MP 469.0000 568.5495 701.0000 .

HP 528.0000 695.2674 795.0000 .

LP 414.0000 438.1696 581.0000 .

---- VAR TSatOpr Heat exchanged


MP 469.0000 485.5883 526.0000 .

HP 528.0000 530.5801 570.0000 .

LP 414.0000 438.1696 456.0000 .

---- VAR WasteH


MP . 1.7316 +INF .

HP . 0.9973 +INF .

LP . . +INF 44.1207

---- VAR MassFCW1


MP . 20.6929 +INF .

HP . 11.9184 +INF .

LP . . +INF .


---- VAR WorkFan . . +INF .

model.lst Wed May 30 15:17:17 2018 417


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---- VAR InPGTCmpr Inlet Pressure for compressor


1 0.9900 1.0133 1.1000 .

---- VAR OutPGTCmpr Outlet Pressure for compressor


1 0.9900 20.0000 20.0000 .

---- VAR InTGTCmpr Inlet Temperature for compressor


1 298.0000 298.1500 299.0000 .

---- VAR OutTGTCmpr Outlet Temperature for compressor


1 298.0000 624.9257 704.0000 .

---- VAR WorkGTCmpr Ideal compressor work


1 . 28.9124 +INF .

---- VAR InPGTExpdr Inlet Pressure for expander


1 0.9900 20.0000 20.0000 .

---- VAR OutPGTExpdr Outlet Pressure for expander


1 1.3000 1.3000 20.0000 105.7366

---- VAR InTGTExpdr Inlet Temperature for expander


1 298.0000 1500.0000 1510.0000 .

model.lst Wed May 30 15:17:17 2018 418


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---- VAR OutTGTExpdr Outlet Temperature for expander


1 298.0000 761.2915 1510.0000 .

---- VAR WorkGTExpdr Ideal expander work


1 . 82.4184 +INF .


---- VAR WorkGT . 53.5060 +INF .

---- VAR MDE


1 . 10.0000 +INF .

2 . 20.0000 +INF .

---- VAR WHPTE


1 . . +INF .

2 . 6.5760 +INF .

3 . . +INF .

---- VAR MDC


1 . . +INF .

2 . . +INF .

---- VAR WHPTM


1.1 . . +INF .

1.2 . . +INF .

2.1 . . +INF EPS

2.2 . . +INF .

3.1 . . +INF .

3.2 . . +INF .

model.lst Wed May 30 15:17:17 2018 419


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---- VAR WMPTM


1.1 . . +INF .

1.2 . . +INF EPS

2.1 . . +INF .

2.2 . . +INF .

---- VAR YMD


1 . . 1.0000 EPS

2 . . 1.0000 EPS

---- VAR YWHPTE


1 . . 1.0000 -42152.1434

2 . 1.0000 1.0000 EPS

3 . . 1.0000 EPS

---- VAR YWHPTM


1.1 . . 1.0000 -5269.0179

1.2 . . 1.0000 -5269.0179

2.1 . . 1.0000 EPS

2.2 . . 1.0000 EPS

3.1 . . 1.0000 EPS

3.2 . . 1.0000 EPS

---- VAR YWMPTM


1.1 . . 1.0000 EPS

1.2 . . 1.0000 EPS

2.1 . . 1.0000 EPS

2.2 . . 1.0000 EPS


---- VAR Z -INF 5226.2818 +INF .

**** REPORT SUMMARY : 0 NONOPT

0 INFEASIBLE

0 UNBOUNDED

0 ERRORS

model.lst Wed May 30 15:17:17 2018 420


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**** Saved point /var/www/html/interfaces/cgi-bin/steam/TEST4a_p.gdx

model.lst Wed May 30 15:17:17 2018 421


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**** SOLVER STATUS FILE LISTED BELOW

=0Dicopt 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

=1

------------------------------------------------------------------

Dicopt 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

------------------------------------------------------------------

Aldo Vecchietti and Ignacio E. Grossmann

Engineering Design Research Center

Carnegie Mellon University

Pittsburgh, Pennsylvania 15213

------------------------------------------------------------------

=2

=1

=CReading parameter(s) from "/var/www/html/interfaces/cgi-bin/steam/dicopt.opt"

=C>> *maxcycles 40

=C>> infeasder 1

=C>>

=C>> * binary corresponding to infeasible NLP subproblems are rejected

=C>> *continue 0

=C>>

=C>> * iteration limit for NLPS

=C>>

=C>> *stop 0

=CFinished reading from "/var/www/html/interfaces/cgi-bin/steam/dicopt.opt"

=2

=CCONOPT 3 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

=0CONOPT 3 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)

2 BRANCH * MAJERR MINERR JACERR (DEFAULT)

3 OPTIMIZE (DEFAULT)

4 BRANCH * * * * * * MAJERR (DEFAULT)

5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)

7 MAJERR MESSAGE MAJOR ERROR - TERMINATE (DEFAULT)

8 EXIT (DEFAULT)

9 MINERR MESSAGE MINOR ERROR - TERMINATE (DEFAULT)

10 EXIT (DEFAULT)

11 JACERR MESSAGE FUNCTION OR DERIVATIVE ERROR (DEFAULT)

12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT

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*** Line 0 SET LFEERR = 0

*** Line 0 SET LFITER = 20000

*** Line 0 SET RVTIME = 1000.000000

*** Line 2 BRANCH with Lbranch = 1

*** Line 3 OPTIMIZE

Search for a first feasible solution

Iter Phase Ninf Infeasibility RGmax NSB Step InItr MX OK

0 0 1.0213924645E+01 (Input point)

After locating simple pre- and post-pivots



Pre-triangular equations: 539

Post-triangular equations: 31

Definitional equations: 134

1 0 1.0000019381E+01 (After pre-processing)

2 0 9.3750004725E-01 (After scaling)

3 0 0 4.4503407035E-01 5.3E-01 T T

4 0 0 1.5196722045E-03 1.0E+00 F T

5 0 0 2.2221878761E-04 1.0E+00 F T

6 0 0 3.2494834414E-05 1.0E+00 F T

7 0 0 4.7518897056E-06 1.0E+00 F T

8 0 0 6.9509577263E-07 1.0E+00 F T

9 0 0 1.0187910929E-07 1.0E+00 F T

10 0 0 1.5134254711E-08 1.0E+00 F T

11 0 0 2.4497279691E-09 1.0E+00 F T

** Feasible solution. Value of objective = 37218.7118893

Search for an optimal solution.

Iter Phase Ninf Objective RGmax NSB Step InItr MX OK

12 3 2.0179731488E+04 1.1E+04 1 9.7E-01 1 T T

13 3 1.4102214102E+04 6.7E+03 7 4.6E-01 6 F F

14 3 1.1445558923E+04 6.2E+03 6 4.5E-01 1 F F

15 3 9.9077106426E+03 6.2E+03 6 3.9E-05 T T

16 3 8.2031970103E+03 6.4E+03 5 4.1E-05 T T

17 3 7.7590156909E+03 9.1E+02 4 5.2E-04 T T

18 3 7.7590156909E+03 4.0E+03 4 0.0E+00 T T

19 3 7.7590156909E+03 2.0E+03 4 0.0E+00 T T

20 3 7.6089977301E+03 3.9E+03 4 1.1E-05 T T

21 3 7.4929058949E+03 1.4E+03 5 3.7E-05 F F

22 3 7.3186729999E+03 1.6E+02 5 5.1E-03 T T

23 3 7.2439750594E+03 1.5E+03 5 1.0E+00 3 T T

24 3 6.5295363654E+03 1.8E+03 11 3.4E-01 8 F F

25 3 5.4217520631E+03 1.9E+03 13 1.0E+00 3 T T

model.lst Wed May 30 15:17:17 2018 423


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26 3 5.1288339663E+03 2.2E+02 12 1.0E+00 6 T T

27 3 5.1250543332E+03 1.0E+01 22 1.0E+00 20 T T

28 3 5.1250521847E+03 1.0E-03 22 1.0E+00 22 T T

29 3 5.1250521847E+03 0.0E+00 22

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2

Work length = 491779 double words = 3.75 Mbytes

Estimate = 491779 double words = 3.75 Mbytes

Max used = 223676 double words = 1.71 Mbytes

Timing for Function Evaluations:

Statistics for FDEval-Fnc Calls: 46550. Time: 0.037 T/C: 7.9484E-07

Statistics for FDEval-Drv Calls: 5586. Time: 0.006 T/C: 1.0741E-06

Statistics for 2DDirLag Calls: 0. Time: 0.000 T/C: 0.0000E+00

Statistics for 2DLagr Calls: 0. Time: 0.000 T/C: 0.0000E+00

=1

=0IBM ILOG CPLEX 24.4.1 r50296 Released Dec 20, 2014 LEG x86 64bit/Linux

=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------

CONTROL FILE STATISTICS

--------------------------------------------------------------

Rows : 1276, columns : 2051, nonzeroes : 5122

model.lst Wed May 30 15:17:17 2018 424


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Free Rows : 0

Iteration limit : 19971

Resource limit : 9.999170e+02

Objective variable : 1309

Objective sense : minimize

Advanced basis : yes

Binary variables : 76

Integer variables : 0

SOS1 variables : 0

SOS2 variables : 0

SemiCont variables : 0

SemiInt variables : 0

OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

model.lst Wed May 30 15:17:17 2018 425


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computeserver

covers 0

craind 1

crossoveralg default

cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0

eachcutlim 2100000000

epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0

intsollim 2100000000

itlim 19971

lbheur 0

model.lst Wed May 30 15:17:17 2018 426


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liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0

polishafternode 2100000000

polishafterintsol 2100000000

polishaftertime 1e+75

polishafterdettime 1e+75

populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

model.lst Wed May 30 15:17:17 2018 427


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preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0

rampupdettimelimit 1e+75

rampupduration 0

rampuptimelimit 1e+75

randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1

siftitlim 2100000000

simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75

solnpoolcapacity 2100000000

solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

model.lst Wed May 30 15:17:17 2018 428


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submipnodelim 500

symmetry -1

threads 1

tilim 999.917

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.983

tuningdettilim 1e+07

usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx

usergdxsol bchsol.gdx

usergdxname bchout.gdx

usergdxnameinc bchout_i.gdx

usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10

userheurinterval 100

userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0

usercgmaxcols 2147483647

usercgadvind 1

usercgsolopt 0

usercgdumplp bchcgdump.lp

userpricingcall

usersolvenodelp

varsel 0

waitforenter 0

workdir /var/www/html/interfaces/cgi-bin/steam/225a/

workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

model.lst Wed May 30 15:17:17 2018 429


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----------------------------------------------------

=1


=2

=1


=2

Tried aggregator 3 times.

MIP Presolve eliminated 778 rows and 1456 columns.

MIP Presolve modified 271 coefficients.

Aggregator did 236 substitutions.

Reduced MIP has 262 rows, 359 columns, and 857 nonzeros.

Reduced MIP has 49 binaries, 0 generals, 0 SOSs, and 0 indicators.

Presolve time = 0.01 sec. (2.67 ticks)

Found incumbent of value 3.6924998e+09 after 0.01 sec. (3.42 ticks)

Probing fixed 0 vars, tightened 13 bounds.

Probing time = 0.00 sec. (0.11 ticks)

Tried aggregator 1 time.













Clique table members: 42.

MIP emphasis: balance optimality and feasibility.

MIP search method: dynamic search.

Parallel mode: none, using 1 thread.


LP Presolve eliminated 2 rows and 0 columns.


Reduced LP has 222 rows, 305 columns, and 763 nonzeros.


Initializing dual steep norms . . .

Iteration log . . .

Iteration: 1 Dual objective = 0.005000



Removing shift (4).


Iteration log . . .


Root relaxation solution time = 0.00 sec. (1.44 ticks)

model.lst Wed May 30 15:17:17 2018 430


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Nodes Cuts/

Node Left Objective IInf Best Integer Best Bound ItCnt Gap

* 0+ 0 3.69250e+09 0.0050 100.00%


0 0 5125.0534 12 3.69250e+09 5125.0534 134 100.00%

* 0+ 0 5221.9019 5125.0534 1.85%

Found incumbent of value 5221.901874 after 0.02 sec. (7.11 ticks)

0 0 5125.0544 13 5221.9019 Cuts: 26 161 1.85%

0 0 5125.0560 6 5221.9019 Cuts: 13 166 1.85%

* 0+ 0 5145.5266 5125.0560 0.40%


0 0 5125.0560 6 5145.5266 Cuts: 9 168 0.40%

0 2 5125.0560 6 5145.5266 5125.0560 168 0.40%

Elapsed time = 0.05 sec. (17.70 ticks, tree = 0.00 MB, solutions = 2)

* 10+ 5 5134.3720 5125.0560 0.18%


* 20+ 7 5131.5980 5125.0560 0.13%


* 24 7 integral 0 5131.5152 5125.0560 276 0.13%


Clique cuts applied: 1

Implied bound cuts applied: 10

Flow cuts applied: 3

Mixed integer rounding cuts applied: 8

Gomory fractional cuts applied: 3

Root node processing (before b&c):

Real time = 0.05 sec. (17.79 ticks)

Sequential b&c:


------------

Total (root+branch&cut) = 0.06 sec. (26.70 ticks)

=1



=2

=1


=2







Iteration log . . .



=1


model.lst Wed May 30 15:17:17 2018 431


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=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=C--- DICOPT: Setting up next NLP



=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT


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*** Line 0 SET RVTIME = 999.8430000


*** Line 3 OPTIMIZE



0 0 1.3119314335E+03 (Input point)








2 0 4.4553263227E+00 (After scaling)

3 0 1 4.4553263227E+00 0.0E+00 T T

4 0 1 4.4553263227E+00 0.0E+00 T T

5 0 1 4.4553263227E+00 0.0E+00 T T

6 0 2 3.0887583238E-01 1.0E+00 F T

7 0 2 2.5241155214E-01 1.0E+00 F T

8 0 2 2.4987719926E-01 1.0E+00 F T

9 0 2 2.4975624520E-01 1.0E+00 F T

10 0 2 2.4975213649E-01 1.0E+00 F T

11 0 2 2.4975189007E-01 1.0E+00 F T

12 1 1 2.4975188317E-01 0.0E+00 0

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2




model.lst Wed May 30 15:17:17 2018 433


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=C

=C--- WARNING : infeasder option is on,

=C--- problem will keep running even when infeasible NLPs are given

=C

=C--- GMO Resort Time 0ms

=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

model.lst Wed May 30 15:17:17 2018 434


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Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

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dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 19517

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

model.lst Wed May 30 15:17:17 2018 436


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mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

model.lst Wed May 30 15:17:17 2018 437


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relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 999.833

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.967


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




model.lst Wed May 30 15:17:17 2018 438


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usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2














model.lst Wed May 30 15:17:17 2018 439


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Iteration log . . .



Perturbation started.



Removing perturbation.


Iteration log . . .



Nodes Cuts/


* 0+ 0 3.69250e+09 0.0050 100.00%


0 0 5125.0534 11 3.69250e+09 5125.0534 172 100.00%

* 0+ 0 5255.6821 5125.0534 2.49%


0 0 5132.0082 11 5255.6821 Cuts: 39 203 2.35%

* 0+ 0 5208.0398 5132.0082 1.46%


0 0 5133.7991 13 5208.0398 Cuts: 20 219 1.43%

* 0+ 0 5165.4580 5133.7991 0.61%


0 0 5134.7900 7 5165.4580 Cuts: 18 237 0.59%

0 0 5134.7900 7 5165.4580 MIRcuts: 4 241 0.59%

* 0+ 0 5159.4104 5134.7900 0.48%


0 0 5134.7900 9 5159.4104 MIRcuts: 6 245 0.48%

model.lst Wed May 30 15:17:17 2018 440


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0 2 5134.7900 9 5159.4104 5134.7900 245 0.48%


* 20+ 2 5154.5503 5134.8703 0.38%

Impl Bds: 4









Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .



=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

model.lst Wed May 30 15:17:17 2018 441


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=1


=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 999.7410000


*** Line 3 OPTIMIZE



0 0 1.3127228389E+03 (Input point)




model.lst Wed May 30 15:17:17 2018 442


05/30/18 15:17:15 Page 391







2 0 5.9734649492E+00 (After scaling)

3 0 1 5.9734649492E+00 0.0E+00 T T

4 0 1 5.9734649492E+00 0.0E+00 T T

5 0 1 5.9734649492E+00 0.0E+00 T T

6 0 1 5.9734649492E+00 0.0E+00 T T

7 0 1 5.9734649492E+00 0.0E+00 T T

8 0 1 5.9734649492E+00 0.0E+00 T T

9 0 2 5.9734649492E+00 0.0E+00 T T

10 0 2 5.9734649492E+00 0.0E+00 T T

11 0 2 2.4364183832E-01 1.0E+00 F T

12 0 2 1.7718963017E-01 1.0E+00 F T

13 0 2 1.3454419717E-01 1.0E+00 F T

14 0 2 2.0802102976E-02 1.0E+00 F T

15 0 2 5.1512439224E-03 1.0E+00 F T

16 0 2 3.4239223827E-03 1.0E+00 F T

17 0 2 3.2017526505E-03 1.0E+00 F T

18 0 2 3.1654582639E-03 1.0E+00 F T

19 0 2 3.1602701306E-03 1.0E+00 F T


20 0 2 3.1593977239E-03 1.0E+00 F T

21 0 2 3.1592722855E-03 1.0E+00 F T

22 0 2 3.1592511610E-03 1.0E+00 F T

23 1 1 1.4245557174E-03 1.6E+02 2 5.5E-01 2 F F

24 1 1 4.0071016971E-08 1.0E+03 3 1.0E+00 1 T T

25 1 1 3.8124624711E-08 1.6E-08 0 0.0E+00 F T

26 1 1 3.8124624711E-08 2.5E-08 0

=1


The feasibility tolerance (Rtnwmi) is 4.00000E-10

It may be relaxed with option:

Rtnwmi=x.xx

=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




model.lst Wed May 30 15:17:17 2018 443


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=2






Statistics for FDEval-Drv Calls: 2960. Time: 0.000 T/C: 0.0000E+00



=C



=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

model.lst Wed May 30 15:17:17 2018 444


05/30/18 15:17:15 Page 393



Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

model.lst Wed May 30 15:17:17 2018 445


05/30/18 15:17:15 Page 394



dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 18692

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

model.lst Wed May 30 15:17:17 2018 446


05/30/18 15:17:15 Page 395



miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

model.lst Wed May 30 15:17:17 2018 447


05/30/18 15:17:15 Page 396



readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 999.708

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.942


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

model.lst Wed May 30 15:17:17 2018 448


05/30/18 15:17:15 Page 397



usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2









model.lst Wed May 30 15:17:17 2018 449


05/30/18 15:17:15 Page 398























Iteration log . . .




Removing shift (5).


Iteration log . . .



Nodes Cuts/


* 0+ 0 3.69250e+09 0.0050 100.00%


0 0 5125.0534 12 3.69250e+09 5125.0534 153 100.00%

* 0+ 0 5264.7605 5125.0534 2.65%


0 0 5132.0082 13 5264.7605 Cuts: 35 185 2.52%

* 0+ 0 5232.5799 5132.0082 1.92%


0 0 5133.7994 13 5232.5799 Cuts: 20 197 1.89%

* 0+ 0 5189.9981 5133.7994 1.08%


0 0 5134.7900 13 5189.9981 Cuts: 14 210 1.06%

0 0 5134.7900 10 5189.9981 Cuts: 13 216 1.06%

* 0+ 0 5159.2518 5134.7900 0.47%


0 2 5134.7198 8 5159.2518 5134.7900 216 0.47%


* 10+ 8 5154.7145 5134.7900 0.39%

model.lst Wed May 30 15:17:17 2018 450


05/30/18 15:17:15 Page 399




* 30+ 2 5154.4806 5154.4262 0.00%

Impl Bds: 9









Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .



=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1

model.lst Wed May 30 15:17:17 2018 451


05/30/18 15:17:15 Page 400




=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 999.6190000


*** Line 3 OPTIMIZE



0 0 1.1758227076E+03 (Input point)





model.lst Wed May 30 15:17:17 2018 452


05/30/18 15:17:15 Page 401






2 0 3.8189104500E+00 (After scaling)

3 0 1 3.8189104500E+00 0.0E+00 T T

4 0 1 3.8189104500E+00 0.0E+00 T T

5 0 1 2.7528147252E-02 1.0E+00 F T

6 0 1 7.1762193162E-04 1.0E+00 F T

7 0 1 7.8663746842E-05 1.0E+00 F T

8 0 1 7.7256326145E-06 1.0E+00 F T

9 0 1 7.6980780730E-07 1.0E+00 F T

10 0 1 7.7634726939E-08 1.0E+00 F T

11 0 1 8.1122827119E-09 1.0E+00 F T




12 3 5.2263151312E+03 1.4E+01 1 6.6E-01 1 T T

13 3 5.2263150832E+03 0.0E+00 1 0.0E+00 0 F T

14 3 5.2263150832E+03 0.0E+00 1

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2









model.lst Wed May 30 15:17:17 2018 453


05/30/18 15:17:15 Page 402




=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

model.lst Wed May 30 15:17:17 2018 454


05/30/18 15:17:15 Page 403



barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

model.lst Wed May 30 15:17:17 2018 455


05/30/18 15:17:15 Page 404



.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 18111

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

model.lst Wed May 30 15:17:17 2018 456


05/30/18 15:17:15 Page 405



objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


model.lst Wed May 30 15:17:17 2018 457


05/30/18 15:17:15 Page 406



simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 999.601

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.92


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0

model.lst Wed May 30 15:17:17 2018 458


05/30/18 15:17:15 Page 407




usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2


























model.lst Wed May 30 15:17:17 2018 459


05/30/18 15:17:15 Page 408











Iteration log . . .




Removing shift (7).

Markowitz threshold set to 0.3



Iteration log . . .



Nodes Cuts/


* 0+ 0 1.27420e+10 0.0050 100.00%


0 0 5141.5610 15 1.27420e+10 5141.5610 181 100.00%

* 0+ 0 11970.4197 5141.5610 57.05%


0 0 5156.7833 19 11970.4197 Cuts: 33 228 56.92%

* 0+ 0 5308.7944 5156.7833 2.86%


0 0 5157.2653 17 5308.7944 Cuts: 33 247 2.85%

0 0 5157.2656 17 5308.7944 Cuts: 11 267 2.85%

0 0 5157.2658 16 5308.7944 Cuts: 7 282 2.85%

0 2 5157.2658 16 5308.7944 5157.2658 282 2.85%


* 10+ 4 5308.5643 5157.2658 2.85%


* 14 5 integral 0 5279.4148 5157.2658 501 2.31%


* 14 4 integral 0 5279.4148 5157.2658 501 2.31%


* 21 0 integral 0 5278.8360 5278.8360 544 0.00%

Impl Bds: 1







model.lst Wed May 30 15:17:17 2018 460


05/30/18 15:17:15 Page 409





Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .






=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2


model.lst Wed May 30 15:17:17 2018 461


05/30/18 15:17:15 Page 410





=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 999.4920000


*** Line 3 OPTIMIZE



0 0 1.1732414606E+03 (Input point)








2 0 3.7104792921E+00 (After scaling)

3 0 1 3.7104792921E+00 0.0E+00 T T

4 0 1 3.7104792921E+00 0.0E+00 T T

5 0 1 3.7104792921E+00 0.0E+00 T T

model.lst Wed May 30 15:17:17 2018 462


05/30/18 15:17:15 Page 411



6 0 2 3.7104792921E+00 0.0E+00 T T

7 0 3 3.7104792921E+00 0.0E+00 T T

8 0 4 2.4401716492E+00 5.9E-01 T T

9 0 4 2.2998026354E+00 1.0E+00 F T

10 0 4 2.2998026354E+00 0.0E+00 F F

11 0 4 1.4640732189E+00 4.8E-01 T T

12 0 4 1.4640732189E+00 0.0E+00 T T

13 0 4 1.4640732189E+00 0.0E+00 T T

14 0 4 1.4640732189E+00 0.0E+00 T T

15 0 4 1.4640732189E+00 0.0E+00 T T

16 0 4 1.4640732189E+00 0.0E+00 T T

17 0 4 1.4640732189E+00 0.0E+00 T T

18 0 4 1.4640732189E+00 0.0E+00 T T

19 0 4 1.4640732189E+00 0.0E+00 F F


20 0 5 1.4640732189E+00 0.0E+00 F F

21 0 6 1.4624773399E+00 1.0E+00 F T

22 0 6 1.4624753670E+00 1.0E+00 F T

23 1 3 4.5918100879E-02 5.0E-01 5 1.0E+00 3 T T

24 1 3 5.8060672699E-06 1.0E+03 4 1.0E+00 4 T T

25 1 1 1.1851766821E-06 1.0E+00 3 1.0E+00 2 T T

26 1 1 1.1851766821E-06 0.0E+00 3

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2









model.lst Wed May 30 15:17:17 2018 463


05/30/18 15:17:15 Page 412



=C



=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

model.lst Wed May 30 15:17:17 2018 464


05/30/18 15:17:15 Page 413



aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

model.lst Wed May 30 15:17:17 2018 465


05/30/18 15:17:15 Page 414



eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 17400

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

model.lst Wed May 30 15:17:17 2018 466


05/30/18 15:17:15 Page 415



nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

model.lst Wed May 30 15:17:17 2018 467


05/30/18 15:17:15 Page 416



secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 999.466

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.893


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

model.lst Wed May 30 15:17:17 2018 468


05/30/18 15:17:15 Page 417



userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2






















model.lst Wed May 30 15:17:17 2018 469


05/30/18 15:17:15 Page 418















Iteration log . . .





Removing shift (8).




Iteration log . . .



Nodes Cuts/


* 0+ 0 1.27421e+10 0.0050 100.00%


0 0 5141.5968 14 1.27421e+10 5141.5968 207 100.00%

* 0+ 0 11991.2176 5141.5968 57.12%


0 0 5156.7835 17 11991.2176 Cuts: 32 278 57.00%

* 0+ 0 5316.0579 5156.7835 3.00%


0 0 5157.2653 16 5316.0579 Cuts: 33 303 2.99%

0 0 5157.2658 16 5316.0579 Cuts: 13 331 2.99%

0 0 5157.2658 15 5316.0579 Cuts: 5 336 2.99%

0 2 5157.2658 15 5316.0579 5157.2658 336 2.99%


* 19 5 integral 0 5283.8775 5187.0627 651 1.83%


* 20 4 integral 0 5283.8396 5187.0627 655 1.83%







model.lst Wed May 30 15:17:17 2018 470


05/30/18 15:17:15 Page 419





Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .




=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2




model.lst Wed May 30 15:17:17 2018 471


05/30/18 15:17:15 Page 420



=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 999.3370000


*** Line 3 OPTIMIZE



0 0 1.1586658085E+03 (Input point)








2 0 3.6948730227E+00 (After scaling)

3 0 1 3.6948730227E+00 0.0E+00 T T

4 0 1 3.6948730227E+00 0.0E+00 T T

5 0 1 3.6948730227E+00 0.0E+00 T T

6 0 1 3.6948730227E+00 0.0E+00 T T

7 0 1 3.6948730227E+00 0.0E+00 T T

model.lst Wed May 30 15:17:17 2018 472


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8 0 1 3.6948730227E+00 0.0E+00 T T

9 0 1 3.6948730227E+00 0.0E+00 T T

10 0 1 3.6948730227E+00 0.0E+00 T T

11 0 1 3.6948730227E+00 0.0E+00 T T

12 0 1 3.6948730227E+00 0.0E+00 T T

13 0 1 3.6948730227E+00 0.0E+00 T T

14 0 1 3.6948730227E+00 0.0E+00 T T

15 0 1 3.6948730227E+00 0.0E+00 T T

16 0 1 3.6948730227E+00 0.0E+00 T T

17 0 1 3.6948730227E+00 0.0E+00 T T

18 0 1 3.6948730227E+00 0.0E+00 T T

19 0 1 3.6948730227E+00 0.0E+00 T T


20 0 1 3.6948730227E+00 0.0E+00 T T

21 0 1 3.6948730227E+00 0.0E+00 T T

22 0 1 3.6948730227E+00 0.0E+00 T T

23 0 1 3.6948730227E+00 0.0E+00 T T

24 0 1 3.6948730227E+00 0.0E+00 T T

25 0 1 3.6948730227E+00 0.0E+00 T T

26 0 1 3.6948730227E+00 0.0E+00 T T

27 0 2 3.6948730227E+00 0.0E+00 T T

28 0 2 3.6518373200E+00 4.3E-02 T T

29 0 2 3.6518373200E+00 0.0E+00 T T

30 0 3 3.6518373200E+00 0.0E+00 T T

31 0 4 1.5258927997E+00 8.1E-01 T T

32 0 4 1.5258927997E+00 0.0E+00 T T

33 0 4 1.5258927997E+00 0.0E+00 F F

34 0 4 1.4672747249E+00 0.0E+00 T T

35 0 4 1.4281810905E+00 9.0E-02 T T

36 0 4 1.3711854567E+00 1.3E-01 T T

37 0 4 1.2914613308E+00 2.5E-01 T T

38 0 4 1.2131371564E+00 1.0E+00 F T

39 0 4 1.2131371564E+00 0.0E+00 F F


40 0 4 6.8203037219E-01 9.3E-02 T T

41 0 4 6.8203037219E-01 0.0E+00 T T

42 0 4 6.8203037219E-01 0.0E+00 T T

43 0 4 6.8203037219E-01 0.0E+00 T T

44 0 4 6.7175487084E-01 3.8E-01 T T

45 0 4 6.7175487084E-01 0.0E+00 T T

46 0 4 6.7175487084E-01 0.0E+00 T T

47 0 4 6.7175487084E-01 0.0E+00 F F

48 0 5 6.5444446077E-01 1.0E+00 F T

49 0 5 6.5407060267E-01 1.0E+00 F T

50 0 5 6.5404942811E-01 1.0E+00 F T

51 0 5 6.5404823002E-01 1.0E+00 F T

52 0 5 6.5404816224E-01 1.0E+00 F T

53 1 1 2.1322517918E-02 8.7E-02 2 1.0E+00 2 T T

54 1 1 2.1322517918E-02 0.0E+00 0

=1

model.lst Wed May 30 15:17:17 2018 473


05/30/18 15:17:15 Page 422




=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2









=C



=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0

model.lst Wed May 30 15:17:17 2018 474


05/30/18 15:17:15 Page 423










SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

model.lst Wed May 30 15:17:17 2018 475


05/30/18 15:17:15 Page 424



covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 16336

lbheur 0

liftprojcuts 0

model.lst Wed May 30 15:17:17 2018 476


05/30/18 15:17:15 Page 425



lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

model.lst Wed May 30 15:17:17 2018 477


05/30/18 15:17:15 Page 426



pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

model.lst Wed May 30 15:17:17 2018 478


05/30/18 15:17:15 Page 427



symmetry -1

threads 1

tilim 999.315

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.863


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

model.lst Wed May 30 15:17:17 2018 479


05/30/18 15:17:15 Page 428



=1


=2

=1


=2


































Iteration log . . .







Removing shift (11).




model.lst Wed May 30 15:17:17 2018 480


05/30/18 15:17:15 Page 429



Iteration log . . .



Nodes Cuts/


* 0+ 0 1.27502e+10 0.0050 100.00%


0 0 5161.2829 13 1.27502e+10 5161.2829 225 100.00%

* 0+ 0 12043.8077 5161.2829 57.15%


0 0 5171.7954 16 12043.8077 Cuts: 34 269 57.06%

* 0+ 0 5457.2128 5171.7954 5.23%


0 0 5171.7958 12 5457.2128 Cuts: 32 286 5.23%

0 0 5171.7960 15 5457.2128 Cuts: 14 321 5.23%

0 0 5171.7964 13 5457.2128 Cuts: 47 342 5.23%

* 0+ 0 5456.9257 5171.7964 5.23%


* 0+ 0 5311.8251 5171.7964 2.64%


0 2 5171.7964 13 5311.8251 5171.7964 342 2.64%


* 15 9 integral 0 5305.2015 5171.7964 570 2.51%


* 16 8 integral 0 5305.1622 5171.7964 575 2.51%


* 16 8 integral 0 5305.1622 5171.7964 575 2.51%









Sequential b&c:


------------


=1



=2

=1


=2




model.lst Wed May 30 15:17:17 2018 481


05/30/18 15:17:15 Page 430






Iteration log . . .




=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)

model.lst Wed May 30 15:17:17 2018 482


05/30/18 15:17:15 Page 431




10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 999.1670000


*** Line 3 OPTIMIZE



0 0 1.1586679127E+03 (Input point)








2 0 3.6969708641E+00 (After scaling)

3 0 2 2.4670118117E-02 1.0E+00 F T

4 0 2 2.1598548599E-02 1.0E+00 F T

5 0 2 2.1345326094E-02 1.0E+00 F T

6 0 2 2.1345326094E-02 0.0E+00 T T

7 0 2 2.1345326094E-02 0.0E+00 T T

8 0 2 2.1324359783E-02 1.0E+00 F T

9 0 2 2.1322667909E-02 1.0E+00 F T

10 0 2 2.1322530147E-02 1.0E+00 F T

11 1 1 2.1322517918E-02 0.0E+00 0

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1

model.lst Wed May 30 15:17:17 2018 483


05/30/18 15:17:15 Page 432






=2









=C



=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



model.lst Wed May 30 15:17:17 2018 484


05/30/18 15:17:15 Page 433



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

model.lst Wed May 30 15:17:17 2018 485


05/30/18 15:17:15 Page 434



divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 15239

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

model.lst Wed May 30 15:17:17 2018 486


05/30/18 15:17:15 Page 435



mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


model.lst Wed May 30 15:17:17 2018 487


05/30/18 15:17:15 Page 436



rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 999.156

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.831


usercutcall

model.lst Wed May 30 15:17:17 2018 488


05/30/18 15:17:15 Page 437



usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2





model.lst Wed May 30 15:17:17 2018 489


05/30/18 15:17:15 Page 438
































Iteration log . . .





Removing shift (8).


Iteration log . . .



Nodes Cuts/


* 0+ 0 1.27504e+10 0.0050 100.00%


0 0 5171.2620 12 1.27504e+10 5171.2620 220 100.00%

* 0+ 0 5574.1209 5171.2620 7.23%


0 0 5179.0450 16 5574.1209 Cuts: 36 249 7.09%

* 0+ 0 5493.8594 5179.0450 5.73%


model.lst Wed May 30 15:17:17 2018 490


05/30/18 15:17:15 Page 439



0 0 5179.0455 11 5493.8594 Cuts: 36 267 5.73%

0 0 5179.0455 15 5493.8594 Cuts: 12 291 5.73%

0 0 5179.0460 13 5493.8594 Cuts: 30 306 5.73%

* 0+ 0 5493.5722 5179.0460 5.73%


* 0+ 0 5334.3641 5179.0460 2.91%


* 0+ 0 5334.3631 5179.0460 2.91%


0 2 5179.0460 13 5334.3631 5179.0460 306 2.91%


* 16 10 integral 0 5326.5240 5179.0470 565 2.77%


* 17 9 integral 0 5326.4847 5179.0470 569 2.77%









Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .




=1



=2

=1


=2

model.lst Wed May 30 15:17:17 2018 491


05/30/18 15:17:15 Page 440



=1


=2

=1


=2

=1


=2

=1


=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 998.9940000


model.lst Wed May 30 15:17:17 2018 492


05/30/18 15:17:15 Page 441



*** Line 3 OPTIMIZE



0 0 1.1585052445E+03 (Input point)








2 0 3.6541429960E+00 (After scaling)

3 0 2 2.4669887248E-02 1.0E+00 F T

4 0 2 2.1598319056E-02 1.0E+00 F T

5 0 2 2.1345096560E-02 1.0E+00 F T

6 0 2 2.1324357565E-02 1.0E+00 F T

7 0 2 2.1322667872E-02 1.0E+00 F T

8 0 2 2.1322530151E-02 1.0E+00 F T

9 1 1 2.1322517918E-02 0.0E+00 0

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2









model.lst Wed May 30 15:17:17 2018 493


05/30/18 15:17:15 Page 442



=C



=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

model.lst Wed May 30 15:17:17 2018 494


05/30/18 15:17:15 Page 443



aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

model.lst Wed May 30 15:17:17 2018 495


05/30/18 15:17:15 Page 444



eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 13879

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

model.lst Wed May 30 15:17:17 2018 496


05/30/18 15:17:15 Page 445



nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

model.lst Wed May 30 15:17:17 2018 497


05/30/18 15:17:15 Page 446



secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 998.984

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.797


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

model.lst Wed May 30 15:17:17 2018 498


05/30/18 15:17:15 Page 447



userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2






















model.lst Wed May 30 15:17:17 2018 499


05/30/18 15:17:15 Page 448















Iteration log . . .





Removing shift (6).


Iteration log . . .



Nodes Cuts/


* 0+ 0 1.27505e+10 0.0050 100.00%


0 0 5177.9606 13 1.27505e+10 5177.9606 212 100.00%

* 0+ 0 5610.6884 5177.9606 7.71%


0 0 5186.2414 15 5610.6884 Cuts: 38 242 7.56%

* 0+ 0 5530.5060 5186.2414 6.22%


0 0 5186.2420 12 5530.5060 Cuts: 32 257 6.22%

0 0 5186.2420 18 5530.5060 Cuts: 9 266 6.22%

* 0+ 0 5354.1323 5186.2420 3.14%


0 0 5186.2424 16 5354.1323 Cuts: 36 280 3.14%

0 2 5186.2424 16 5354.1323 5186.2424 280 3.14%


* 16 8 integral 0 5347.8476 5186.2424 512 3.02%


* 17 7 integral 0 5347.8082 5186.2424 516 3.02%


* 60+ 0 5347.8072 5347.8062 0.00%

Impl Bds: 7




model.lst Wed May 30 15:17:17 2018 500


05/30/18 15:17:15 Page 449








Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .




=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

model.lst Wed May 30 15:17:17 2018 501


05/30/18 15:17:15 Page 450






=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 998.8160000


*** Line 3 OPTIMIZE



0 0 1.1584363721E+03 (Input point)








2 0 3.6541429960E+00 (After scaling)

3 0 2 2.4669887248E-02 1.0E+00 F T

4 0 2 2.1598319056E-02 1.0E+00 F T

model.lst Wed May 30 15:17:17 2018 502


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5 0 2 2.1345096560E-02 1.0E+00 F T

6 0 2 2.1324357565E-02 1.0E+00 F T

7 0 2 2.1322667872E-02 1.0E+00 F T

8 0 2 2.1322530151E-02 1.0E+00 F T

9 1 1 2.1322517918E-02 0.0E+00 0

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2









=C



=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

model.lst Wed May 30 15:17:17 2018 503


05/30/18 15:17:15 Page 452



--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

model.lst Wed May 30 15:17:17 2018 504


05/30/18 15:17:15 Page 453



bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

model.lst Wed May 30 15:17:17 2018 505


05/30/18 15:17:15 Page 454



iis 0

implbd 0

interactive 0


itlim 12604

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





model.lst Wed May 30 15:17:17 2018 506


05/30/18 15:17:15 Page 455



populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

model.lst Wed May 30 15:17:17 2018 507


05/30/18 15:17:15 Page 456



solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 998.805

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.761


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

model.lst Wed May 30 15:17:17 2018 508


05/30/18 15:17:15 Page 457



writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2


































Iteration log . . .





model.lst Wed May 30 15:17:17 2018 509


05/30/18 15:17:15 Page 458






Iteration log . . .



Nodes Cuts/


* 0+ 0 1.27507e+10 0.0050 100.00%


0 0 5184.4572 14 1.27507e+10 5184.4572 193 100.00%

* 0+ 0 5647.2560 5184.4572 8.20%


0 0 5193.4380 16 5647.2560 Cuts: 36 218 8.04%

* 0+ 0 5567.1526 5193.4380 6.71%


0 0 5193.4386 16 5567.1526 Cuts: 36 237 6.71%

0 0 5193.4389 16 5567.1526 Cuts: 13 246 6.71%

* 0+ 0 5360.1934 5193.4389 3.11%


0 2 5193.4389 16 5360.1934 5193.4389 246 3.11%


* 18 10 integral 0 5357.7338 5193.4389 445 3.07%


* 19 9 integral 0 5357.6945 5193.4389 449 3.07%


* 26 11 integral 0 5357.6935 5193.4532 521 3.07%

MIRcuts: 1









Sequential b&c:


------------


=1



=2

=1


=2


model.lst Wed May 30 15:17:17 2018 510


05/30/18 15:17:15 Page 459








Iteration log . . .






=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




model.lst Wed May 30 15:17:17 2018 511


05/30/18 15:17:15 Page 460



5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 998.5460000


*** Line 3 OPTIMIZE



0 0 1.2611842553E+03 (Input point)








2 0 5.6963078900E+00 (After scaling)

3 0 1 5.6963078900E+00 0.0E+00 T T

4 0 1 5.6963078900E+00 0.0E+00 T T

5 0 1 5.6963078900E+00 0.0E+00 T T

6 0 1 5.6963078900E+00 0.0E+00 T T

7 0 1 5.6963078900E+00 0.0E+00 T T

8 0 1 5.6963078900E+00 0.0E+00 T T

9 0 1 5.6963078900E+00 0.0E+00 T T

10 0 1 5.6963078900E+00 0.0E+00 T T

11 0 1 5.6963078900E+00 0.0E+00 T T

12 0 1 5.6963078900E+00 0.0E+00 T T

13 0 1 5.6963078900E+00 0.0E+00 F F

14 0 2 5.6626962976E+00 8.1E-04 T T

15 0 3 5.6626962976E+00 0.0E+00 T T

16 0 4 5.6626962976E+00 0.0E+00 T T

17 0 5 5.6626962976E+00 0.0E+00 T T

18 0 6 5.6626962976E+00 0.0E+00 T T

19 0 7 5.6626962976E+00 0.0E+00 T T

model.lst Wed May 30 15:17:17 2018 512


05/30/18 15:17:15 Page 461




20 0 8 5.6626962976E+00 0.0E+00 T T

21 0 9 5.6626962976E+00 0.0E+00 T T

22 0 10 5.6626962976E+00 0.0E+00 T T

23 0 11 5.6626962976E+00 0.0E+00 T T

24 0 12 5.6626962976E+00 0.0E+00 T T

25 0 13 5.6626962976E+00 0.0E+00 T T

26 0 14 5.6626962976E+00 0.0E+00 T T

27 0 15 5.6626962976E+00 0.0E+00 T T

28 0 16 5.6626962976E+00 0.0E+00 T T

29 0 17 5.6626962976E+00 0.0E+00 T T

30 0 18 5.6626962976E+00 0.0E+00 T T

31 0 19 5.6626962976E+00 0.0E+00 T T

32 0 20 5.6626962976E+00 0.0E+00 T T

33 0 21 5.6626962976E+00 0.0E+00 T T

34 0 22 5.6626962976E+00 0.0E+00 T T

35 0 22 5.5837499574E+00 1.5E-01 T T

36 0 22 5.4478955155E+00 3.3E-01 T T

37 0 22 5.4478955155E+00 0.0E+00 T T

38 0 22 5.4478955155E+00 0.0E+00 T T

39 0 22 5.4478955155E+00 0.0E+00 T T


40 0 22 5.3733321769E+00 1.7E-01 T T

41 0 22 5.2202619974E+00 1.0E+00 F T

42 0 22 5.0744643008E+00 1.0E+00 F T

43 0 22 5.0293201996E+00 1.0E+00 F T

44 0 22 5.0181346470E+00 1.0E+00 F T

45 0 22 5.0146273879E+00 1.0E+00 F T

46 0 22 5.0138139266E+00 1.0E+00 F T

47 0 22 5.0135377137E+00 1.0E+00 F T

48 0 22 5.0134794027E+00 1.0E+00 F T

49 0 22 5.0134573561E+00 1.0E+00 F T

50 0 22 5.0134532711E+00 1.0E+00 F T

51 0 22 5.0134514802E+00 1.0E+00 F T

52 0 22 5.0134512051E+00 1.0E+00 F T

53 1 19 1.9297999762E+00 3.4E+01 19 1.0E+00 3 T T

54 1 4 1.2215976553E-01 1.0E+00 16 1.0E+00 8 T T




55 3 5.2904729439E+03 1.3E+03 1 1.0E+00 1 T T

56 3 5.2560533405E+03 1.1E+02 2 5.7E-01 3 F F

57 3 5.2330709946E+03 1.1E+02 2 6.9E-01 2 T T

58 3 5.2262817816E+03 1.1E+02 1 1.0E+00 1 T T

59 3 5.2262817832E+03 0.0E+00 1 0.0E+00 0 F T

60 3 5.2262817832E+03 0.0E+00 1

=1

model.lst Wed May 30 15:17:17 2018 513


05/30/18 15:17:15 Page 462




=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2










=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0





model.lst Wed May 30 15:17:17 2018 514


05/30/18 15:17:15 Page 463






SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

model.lst Wed May 30 15:17:17 2018 515


05/30/18 15:17:15 Page 464



cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 10782

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

model.lst Wed May 30 15:17:17 2018 516


05/30/18 15:17:15 Page 465



memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

model.lst Wed May 30 15:17:17 2018 517


05/30/18 15:17:15 Page 466



probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 998.492

trelim 1e+75

model.lst Wed May 30 15:17:17 2018 518


05/30/18 15:17:15 Page 467



tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.698


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

model.lst Wed May 30 15:17:17 2018 519


05/30/18 15:17:15 Page 468



=1


=2





























Iteration log . . .










Iteration log . . .



Nodes Cuts/


* 0+ 0 1.88546e+10 0.0050 100.00%


0 0 5184.4597 15 1.88546e+10 5184.4597 210 100.00%

model.lst Wed May 30 15:17:17 2018 520


05/30/18 15:17:15 Page 469



* 0+ 0 5647.2583 5184.4597 8.20%


0 0 5193.4413 16 5647.2583 Cuts: 39 238 8.04%

* 0+ 0 5604.6055 5193.4413 7.34%


0 0 5193.4419 18 5604.6055 Cuts: 38 257 7.34%

* 0+ 0 5604.6045 5193.4419 7.34%


0 0 5193.4389 15 5604.6045 Cuts: 17 266 7.34%

* 0+ 0 5445.2893 5193.4419 4.63%


0 0 5193.4389 14 5445.2893 Cuts: 6 269 4.63%

* 0+ 0 5369.1736 5193.4419 3.27%


0 2 5193.4389 14 5369.1736 5193.4419 269 3.27%


* 16 5 integral 0 5369.1323 5209.7709 443 2.97%


* 30+ 3 5360.1950 5233.1169 2.37%

Impl Bds: 1


* 36 6 integral 0 5360.1545 5233.1169 566 2.37%


* 42 5 integral 0 5360.1535 5260.9133 642 1.85%

Impl Bds: 1


* 59 2 integral 0 5357.6960 5357.6765 776 0.00%

MIRcuts: 2









Sequential b&c:


------------


=1



=2

=1


=2





model.lst Wed May 30 15:17:17 2018 521


05/30/18 15:17:15 Page 470





Iteration log . . .





=1



=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)

model.lst Wed May 30 15:17:17 2018 522


05/30/18 15:17:15 Page 471




10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 998.2870000


*** Line 3 OPTIMIZE



0 0 1.2611842007E+03 (Input point)








2 0 5.6963070068E+00 (After scaling)

3 0 6 5.6963070068E+00 0.0E+00 T T

4 0 6 5.6963070068E+00 0.0E+00 T T

5 0 6 5.6963070068E+00 0.0E+00 T T

6 0 6 5.6963070068E+00 0.0E+00 T T

7 0 6 5.6963070068E+00 0.0E+00 F F

8 0 7 5.6555144704E+00 8.1E-04 T T

9 0 8 5.6555144704E+00 0.0E+00 T T

10 0 9 5.6555144704E+00 0.0E+00 T T

11 0 10 5.6555144704E+00 0.0E+00 T T

12 0 11 5.6555144704E+00 0.0E+00 T T

13 0 12 5.6555144704E+00 0.0E+00 T T

14 0 13 5.6555144704E+00 0.0E+00 T T

15 0 14 5.6555144704E+00 0.0E+00 T T

16 0 15 5.6555144704E+00 0.0E+00 T T

17 0 16 5.6555144704E+00 0.0E+00 T T

18 0 17 5.6555144704E+00 0.0E+00 T T

19 0 18 5.6555144704E+00 0.0E+00 T T


20 0 19 5.6555144704E+00 0.0E+00 T T

21 0 20 5.6555144704E+00 0.0E+00 T T

22 0 21 5.6555144704E+00 0.0E+00 T T

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23 0 22 5.6555144704E+00 0.0E+00 T T

24 0 22 5.6483502551E+00 6.1E-03 T T

25 0 22 5.6483502551E+00 0.0E+00 T T

26 0 22 5.6483502551E+00 0.0E+00 F F

27 0 22 5.6483502551E+00 0.0E+00 F F

28 0 23 5.6483502551E+00 0.0E+00 F F

29 0 24 5.6483502551E+00 0.0E+00 F F

30 0 25 5.6483502551E+00 0.0E+00 F F

31 0 26 5.6483502551E+00 0.0E+00 F F

32 0 27 5.6483502551E+00 0.0E+00 F F

33 0 28 5.6483502551E+00 0.0E+00 F F

34 0 29 5.6483502551E+00 0.0E+00 F F

35 0 30 5.6483502551E+00 0.0E+00 F F

36 0 31 5.6483502551E+00 0.0E+00 F F

37 0 32 5.6483502551E+00 0.0E+00 F F

38 0 33 5.6483502551E+00 0.0E+00 F F

39 0 34 5.6483502551E+00 0.0E+00 F F


40 0 35 5.6483502551E+00 0.0E+00 F F

41 0 36 5.6483502551E+00 0.0E+00 F F

42 0 37 5.6483502551E+00 0.0E+00 F F

43 0 38 5.6483502551E+00 0.0E+00 F F

44 0 39 5.6483502551E+00 0.0E+00 F F

45 0 40 5.6483502551E+00 0.0E+00 F F

46 0 41 5.6483502551E+00 0.0E+00 F F

47 0 42 5.6483502551E+00 0.0E+00 F F

48 0 43 5.6483502551E+00 0.0E+00 F F

49 0 44 5.6483502551E+00 0.0E+00 F F

50 0 45 5.6483502551E+00 0.0E+00 F F

51 0 46 5.6483502551E+00 0.0E+00 F F

52 0 47 5.6483502551E+00 0.0E+00 F F

53 0 48 5.6483502551E+00 0.0E+00 F F

54 0 49 5.6483502551E+00 0.0E+00 F F

55 0 50 5.6483502551E+00 0.0E+00 F F

56 0 51 5.6483502551E+00 0.0E+00 F F

57 0 52 5.6483502551E+00 0.0E+00 F F

58 0 53 5.6483502551E+00 0.0E+00 F F

59 0 54 5.6483502551E+00 0.0E+00 F F


60 0 55 5.6483502551E+00 0.0E+00 F F

61 0 56 5.6483502551E+00 0.0E+00 F F

62 0 57 5.6483502551E+00 0.0E+00 F F

63 0 58 5.6483502551E+00 0.0E+00 F F

64 0 59 5.6483502551E+00 0.0E+00 F F

65 0 60 5.6483502551E+00 0.0E+00 F F

66 0 61 5.6483502551E+00 0.0E+00 T T

67 0 62 5.6483502551E+00 0.0E+00 T T

68 0 62 5.6230261061E+00 3.9E-01 T T

69 0 62 5.6230261061E+00 0.0E+00 F F

70 0 62 5.6230261061E+00 0.0E+00 F F

71 0 63 5.6230261061E+00 0.0E+00 F F

model.lst Wed May 30 15:17:17 2018 524


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72 0 64 5.6230261061E+00 0.0E+00 F F

73 0 65 5.6230261061E+00 0.0E+00 F F

74 0 66 5.6230261061E+00 0.0E+00 F F

75 0 67 5.6230261061E+00 0.0E+00 F F

76 0 68 5.6230261061E+00 0.0E+00 F F

77 0 69 5.6230261061E+00 0.0E+00 F F

78 0 70 5.6230261061E+00 0.0E+00 F F

79 0 71 5.6230261061E+00 0.0E+00 F F


80 0 72 5.6230261061E+00 0.0E+00 F F

81 0 73 5.6230261061E+00 0.0E+00 F F

82 0 74 5.6230261061E+00 0.0E+00 F F

83 0 75 5.6230261061E+00 0.0E+00 F F

84 0 76 5.6222614892E+00 1.0E+00 F T

85 1 72 4.5608138792E+00 3.3E+01 69 1.0E+00 3 T T

86 1 64 3.3503607047E+00 3.3E+01 66 1.0E+00 8 T T

87 1 47 3.0428146585E+00 1.0E+00 58 1.0E+00 15 T T

88 1 23 2.2688124282E+00 1.0E+00 41 1.0E+00 18 T T

89 1 6 6.3284087792E-02 1.0E+00 22 1.0E+00 15 T T

90 1 1 3.2279708571E-02 2.5E-01 6 1.0E+00 5 T T

91 1 1 3.2279708571E-02 0.0E+00 6

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2









=C

model.lst Wed May 30 15:17:17 2018 525


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=C


=1


=1


=2

=1


=2

=1

Cplex 12.6.1.0

=2

--------------------------------------------------------------


--------------------------------------------------------------


Free Rows : 0








SOS1 variables : 0

SOS2 variables : 0



OPTCA : 0.000000e+00 , OPTCR : 0.000000e+00

Priorities : no

Cheat : n.a.

Cutoff : n.a.

Node limit : 10000

Option Values:

----------------------------------------------------

usebasis 1

cutoff 0

tryint 0

domlim 0

advind 2

aggcutlim 3

aggfill 10

model.lst Wed May 30 15:17:17 2018 526


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aggind -1

auxrootthreads 0

baralg 0

barcolnz 0

barcrossalg 0

bardisplay 1

barepcomp 1e-08

bargrowth 1e+12

baritlim 2100000000

barmaxcor -1

barobjrng 1e+20

barorder 0

barqcpepcomp 1e-07

barstartalg 1

bbinterval 7

bndstrenind -1

brdir 0

bttol 0.9999

calcqcpduals 1

cliques 0

clocktype 0

clonelog 0

coeredind -1

computeserver

covers 0

craind 1


cutlo -1e+75

cutpass 0

cuts 0

cutsfactor 4

cutup 1e+75

depind -1

dettilim 1e+75

disjcuts 0

divetype 0

divfltup 1e+299

divfltlo -1e+299

.divflt 0

dpriind 0

dtprefix bnd

dtterm 1

dumpcuts 0

dumptree 0

dumplp 0


epagap 0

epgap 0

epint 1e-05

epmrk 0.01

epopt 1e-06

epper 1e-06

eprelax 1e-06

model.lst Wed May 30 15:17:17 2018 527


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eprhs 1e-06

feasopt 0

feasoptmode 0

.feaspref 1

fixoptfile

flowcovers 0

flowpaths 0

flushfiles 0

fpheur 0

fraccand 200

fraccuts 0

fracpass 0

gubcovers 0

heurfreq 0

iafile

iatriggerfile

iatriggertime 60

iis 0

implbd 0

interactive 0


itlim 9755

lbheur 0

liftprojcuts 0

lpalg default

lpmethod 0

ltol 0

mcfcuts 0

memoryemphasis 0

localimplied 0

mipdisplay 4

mipemphasis 0

mipkappastats -1

mipinterval 0

mipordind 1

mipordtype 0

mipsearch 0

mipstart 0

miptrace

miptracenode 100

miptracetime 1

miqcpstrat 0

mircuts 0

mpslongnum 1

mtol 0

names 1

netdisplay 2

netepopt 1e-06

neteprhs 1e-06

netfind 2

netitlim 2100000000

netppriind 0

nodefileind 1

model.lst Wed May 30 15:17:17 2018 528


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nodelim 10000

nodesel 1

numericalemphasis 0

objdif 0

objllim -1e+75

objrng

objulim 1e+75

parallelmode 1

perind 0

perlim 0

polishtime 0

polishafterepagap 0

polishafterepgap 0





populatelim 20

ppriind 0

predual 0

preind 1

prelinear 1

prepass -1

preslvnd 0

pricelim 0

printoptions 0

probe 0

probetime 1e+75

probedettime 1e+75

probread

qpmakepsdind 1

qpmethod 0

qtolin -1

quality 0


rampupduration 0


randomseed 0

readflt

readparams

reduce 3

reinv 0

relaxfixedinfeas 0

relaxpreind -1

relobjdif 0

repairtries 0

repeatpresolve -1

rerun yes

rhsrng

rinsheur 0

rngrestart

scaind 0

secret

model.lst Wed May 30 15:17:17 2018 529


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siftalg 0

siftdisplay 1


simdisplay 1

singlim 10

solnpool

solnpoolmerge

solnpoolnumsym 10

solnpoolagap 1e+75


solnpoolgap 1e+75

solnpoolintensity 0

solnpoolpop 1

solnpoolpopdel

solnpoolpoprepeat

solnpoolprefix soln

solnpoolreplace 0

solutiontarget 0

solvefinal 1

startalg 0

strongcandlim 10

strongitlim 0

subalg 0

submipnodelim 500

symmetry -1

threads 1

tilim 998.235

trelim 1e+75

tuning

tuningdisplay 1

tuningmeasure 1

tuningrepeat 1

tuningtilim 199.647


usercutcall

usercutfirst 10

usercutfreq 10

usercutinterval 100

usercutmult 2

usercutnewint 1

usergdxin bchin.gdx




usergdxprefix

userheurcall

userheurfirst 10

userheurfreq 10


userheurmult 2

userheurnewint 1

userheurobjfirst 0

userincbcall

model.lst Wed May 30 15:17:17 2018 530


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userincbicall

userjobid

userkeep 0


usercgadvind 1

usercgsolopt 0


userpricingcall

usersolvenodelp

varsel 0

waitforenter 0


workmem 128

writebas

writeflt

writelp

writemps

writemst

writeord

writeparam

writepre

writesav

zerohalfcuts 0

----------------------------------------------------

=1


=2

=1


=2























model.lst Wed May 30 15:17:17 2018 531


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Iteration log . . .





Removing shift (11).

Iteration: 216 Scaled dual infeas = 0.000000




Iteration log . . .



Nodes Cuts/


* 0+ 0 1.88547e+10 0.0050 100.00%


0 0 5184.4607 12 1.88547e+10 5184.4607 220 100.00%

* 0+ 0 5688.3318 5184.4607 8.86%


0 0 5193.4423 15 5688.3318 Cuts: 36 242 8.70%

* 0+ 0 5584.3610 5193.4423 7.00%


0 0 5193.4429 15 5584.3610 Cuts: 36 260 7.00%

0 0 5193.4432 16 5584.3610 Cuts: 13 269 7.00%

* 0+ 0 5401.2695 5193.4432 3.85%


0 2 5193.4432 16 5401.2695 5193.4432 269 3.85%


* 10+ 8 5379.4546 5193.4432 3.46%


* 16 10 integral 0 5379.4368 5193.4432 529 3.46%


* 30 14 integral 0 5378.4103 5256.6674 669 2.26%


* 31 13 integral 0 5377.1900 5256.6674 670 2.24%


* 31 13 integral 0 5377.1900 5256.6674 670 2.24%


* 40 16 integral 0 5377.1890 5260.9143 770 2.16%

Impl Bds: 1


* 40 16 integral 0 5377.1890 5260.9143 770 2.16%


model.lst Wed May 30 15:17:17 2018 532


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* 60 8 integral 0 5364.1935 5362.3017 874 0.04%

MIRcuts: 1


* 74 2 integral 0 5363.5723 5363.5528 913 0.00%

Impl Bds: 1


* 74 2 integral 0 5363.5723 5363.5528 913 0.00%









Sequential b&c:


------------


=1



=2

=1


=2







Iteration log . . .








=1



=2

=1


=2

=1


model.lst Wed May 30 15:17:17 2018 533


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=2

=1


=2

=1


=2

=1


=2

=1


=2




=1



Bagsvaerdvej 246 A


=2

1 INPUT (DEFAULT)




5 OUTPUT (DEFAULT)

6 EXIT (DEFAULT)


8 EXIT (DEFAULT)


10 EXIT (DEFAULT)


12 OUTPUT (DEFAULT)

13 EXIT (DEFAULT)

*** Line 1 INPUT



*** Line 0 SET RVTIME = 998.0260000


*** Line 3 OPTIMIZE

model.lst Wed May 30 15:17:17 2018 534


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0 0 1.3143275962E+03 (Input point)








2 0 4.0709446466E+00 (After scaling)

3 0 3 4.0709446466E+00 0.0E+00 T T

4 0 3 4.0709446466E+00 0.0E+00 T T

5 0 3 4.0709446466E+00 0.0E+00 T T

6 0 3 4.0709446466E+00 0.0E+00 T T

7 0 3 4.0709446466E+00 0.0E+00 F F

8 0 4 4.0709446466E+00 0.0E+00 F F

9 0 5 4.0709446466E+00 0.0E+00 F F

10 0 6 4.0709446466E+00 0.0E+00 F F

11 0 7 4.0709446466E+00 0.0E+00 F F

12 0 8 4.0709446466E+00 0.0E+00 F F

13 0 9 4.0709446466E+00 0.0E+00 F F

14 0 10 4.0709446466E+00 0.0E+00 F F

15 0 11 4.0709446466E+00 0.0E+00 F F

16 0 12 4.0709446466E+00 0.0E+00 F F

17 0 13 4.0709446466E+00 0.0E+00 F F

18 0 14 4.0709446466E+00 0.0E+00 F F

19 0 15 4.0709446466E+00 0.0E+00 F F


20 0 16 4.0709446466E+00 0.0E+00 F F

21 0 17 4.0709446466E+00 0.0E+00 F F

22 0 18 4.0709446466E+00 0.0E+00 F F

23 0 19 4.0709446466E+00 0.0E+00 F F

24 0 20 4.0709446466E+00 0.0E+00 F F

25 0 21 4.0709446466E+00 0.0E+00 F F

26 0 22 4.0709446466E+00 0.0E+00 F F

27 0 23 4.0709446466E+00 0.0E+00 F F

28 0 24 4.0709446466E+00 0.0E+00 F F

29 0 25 4.0709446466E+00 0.0E+00 F F

30 0 26 4.0709446466E+00 0.0E+00 F F

31 0 27 4.0709446466E+00 0.0E+00 F F

32 0 28 4.0709446466E+00 0.0E+00 T T

33 0 29 4.0709446466E+00 0.0E+00 T T

34 0 30 4.0709446466E+00 0.0E+00 F F

35 0 31 4.0709446466E+00 0.0E+00 F F

36 0 32 4.0709446466E+00 0.0E+00 F F

37 0 33 4.0709446466E+00 0.0E+00 F F

38 0 34 4.0709446466E+00 0.0E+00 F F

39 0 35 4.0709446466E+00 0.0E+00 F F

model.lst Wed May 30 15:17:17 2018 535


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40 0 36 4.0709446466E+00 0.0E+00 T T

41 0 36 4.0709446466E+00 0.0E+00 T T

42 0 36 4.0709446466E+00 0.0E+00 T T

43 0 37 4.0579821197E+00 9.5E-04 T T

44 0 37 3.3754056098E+00 6.5E-01 T T

45 0 37 3.3754056098E+00 0.0E+00 T T

46 0 37 3.2878230017E+00 1.0E+00 F T

47 0 37 3.2832203886E+00 1.0E+00 F T

48 0 37 3.2832203886E+00 0.0E+00 F F

49 0 37 3.2832203886E+00 0.0E+00 F F

50 0 38 3.2831408876E+00 1.0E+00 F T

51 1 33 1.6174458547E+00 1.0E+00 11 1.0E+00 3 T T

52 1 21 1.0812792370E+00 1.0E+00 34 1.0E+00 10 T T

53 1 4 5.3838752749E-02 1.0E+00 19 1.0E+00 10 T T




54 3 5.2358692350E+03 5.8E+02 2 5.8E-01 3 F F

55 3 5.2322956229E+03 5.6E+02 2 1.0E+00 1 T T

56 3 5.2262817832E+03 1.8E+01 1 5.9E-01 1 T T

57 3 5.2262817832E+03 0.0E+00 0

=1


=2


*** Line 5 OUTPUT

*** Line 6 EXIT

=1




=2







model.lst Wed May 30 15:17:17 2018 536


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=1

=C--- DICOPT: Stopped on NLP worsening

=C

=C The search was stopped because the objective function

=C of the NLP subproblems started to deteriorate.

=C

=C--- DICOPT: Best integer solution found: 5226.281783

=2

DICOPT Log File

------------------------------------------------------------------

Major Major Objective CPU time Itera- Evaluation Solver

Step Iter Function (Sec) tions Errors

NLP 1 5125.05218 0.08 29 0 conopt

MIP 1 5131.51524 0.07 442 0 cplex

NLP 2 *Infeas* 0.01 12 0 conopt

MIP 2 5154.55031 0.09 799 0 cplex


MIP 3 5154.55137 0.09 567 0 cplex

NLP 4 5226.31508< 0.02 14 0 conopt

MIP 4 5278.83598 0.11 685 0 cplex


MIP 5 5283.83965 0.13 1010 0 cplex


MIP 6 5305.16216 0.15 1086 0 cplex


MIP 7 5326.48468 0.16 1351 0 cplex


MIP 8 5347.80720 0.17 1266 0 cplex


MIP 9 5357.69350 0.26 1762 0 cplex

NLP 10 5226.28178< 0.05 60 0 conopt

MIP 10 5357.69604 0.21 936 0 cplex


MIP 11 5363.57233 0.21 1108 0 cplex

NLP 12 5226.28178 0.06 57 0 conopt

------------------------------------------------------------------

Total solver times : NLP = 0.39 MIP = 1.64

Perc. of total : NLP = 19.01 MIP = 80.99

------------------------------------------------------------------

=4

=2

-------------------------------------------------------------

Values of discrete variables at the end of major iterations

-------------------------------------------------------------

Total no. of variables : 1309

Total no. of binary variables : 76

Total no. of integer variables : 0

Seq. no. of binary variables in the list of variables

model.lst Wed May 30 15:17:17 2018 537


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822 823 824 825 826

827 828 829 830 831

832 833 834 835 836

837 838 839 840 841

842 843 844 845 846

847 848 849 850 851

852 853 854 855 856

857 858 1162 1163 1164

1165 1166 1167 1168 1169

1170 1171 1172 1173 1174

1175 1176 1177 1178 1179

1206 1207 1208 1209 1210

1211 1294 1295 1296 1297

1298 1299 1300 1301 1302

1303 1304 1305 1306 1307

1308

Values of binary variables : Iteration no.: 1

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.150 1.000 0.000

0.000 1.000 0.867 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.044 0.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.570 0.821 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.909 0.823 0.000 0.991

0.000 0.000 1.000 0.009 0.000

0.000 0.000 0.991 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

1.000 0.000 1.000 0.000 0.000

0.000 1.000 0.000 1.000 1.000

0.000 0.000 1.000 0.000 0.000

model.lst Wed May 30 15:17:17 2018 538


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0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


0.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

1.000 1.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


0.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2

model.lst Wed May 30 15:17:17 2018 539


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0.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

1.000 1.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 1.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 1.000

0.000 0.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

model.lst Wed May 30 15:17:17 2018 540


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0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 1.000

0.000 0.000 0.000 1.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 1.000

0.000 0.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 0.000 0.000 1.000

0.000 0.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 1.000 0.000

model.lst Wed May 30 15:17:17 2018 541


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0.000 0.000 0.000 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 1.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000

=2


1.000 0.000 0.000 1.000 0.000

model.lst Wed May 30 15:17:17 2018 542


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0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 0.000 0.000

1.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 1.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 1.000 1.000 0.000 0.000

0.000 0.000 0.000 1.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 1.000 1.000 0.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000 1.000

0.000

**** SOLVER STATUS FILE LISTED ABOVE

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E x e c u t i o n

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**** REPORT FILE SUMMARY

RES1 /var/www/html/interfaces/steam/output.html

EXECUTION TIME = 0.025 SECONDS 3 MB 24.4.1 r50296 LEX-LEG

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**** FILE SUMMARY

Input /var/www/html/interfaces/cgi-bin/steam/model.gms

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