Product and Process Design Principles - Seider

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A R E A B U L K R E P O R T ================================================================================================================================= : : : : : M A N P O W E R : TOTAL : : : ITEM : D E S C R I P T I O N :------------------------------------: MATERIAL :------------------: DIRECT : :ORIGIN : SYMBOL :---------: D E S I G N D A T A : COST-USD : MANHOURS:COST-USD: COST-USD: ================================================================================================================================= AREA MISC CONCRETE ITEMS 638. 138 2341. 2979. AREA PIPE TESTING 0. 192 4564. 4564. GRADE UNPAVED AREA 7534. 127 2648. 10182. Area length 50.000 FEET Area width 50.000 FEET AREA INSTRUMENT TESTING 0. 95 2124. 2124. AREA INSTR. RUNS,TRAYS,JBOX. 3086. 60 1266. 4352. AREA EQUIPMENT GROUNDING 185. 11 231. 416. AREA PILED FOUNDATION 8807. 83 1407. 10214. Number of piles 14 AREA ELECTRICAL TESTING 0. 16 344. 344. AREA ROTATING EQP SPARE PARTS 370. 0 0. 370.

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A R E A B U L K R E P O R T ================================================================================================================================= : : : : : M A N P O W E R : TOTAL : : : ITEM : D E S C R I P T I O N :------------------------------------: MATERIAL :------------------: DIRECT : :ORIGIN : SYMBOL :---------: D E S I G N D A T A : COST-USD : MANHOURS:COST-USD: COST-USD: ================================================================================================================================= AREA MISC CONCRETE ITEMS 916. 198 3358. 4274. AREA PIPE TESTING 0. 328 7771. 7771. GRADE UNPAVED AREA 7534. 127 2648. 10182. Area length 50.000 FEET Area width 50.000 FEET AREA INSTRUMENT TESTING 0. 179 4012. 4012. AREA INSTR. RUNS,TRAYS,JBOX. 3471. 68 1450. 4921. AREA EQUIPMENT GROUNDING 369. 23 462. 831. AREA PILED FOUNDATION 13840. 131 2211. 16051. Number of piles 22 AREA ELECTRICAL TESTING 0. 20 430. 430. AREA ROTATING EQP SPARE PARTS 430. 0 0. 430.

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IN-UNITS ENG DEF-STREAMS CONVEN ALL DATABANKS PURE93 / AQUEOUS / SOLIDS / INORGANIC / & NOASPENPCD PROP-SOURCES PURE93 / AQUEOUS / SOLIDS / INORGANIC COMPONENTS C2H6 C2H6 / C3H8 C3H8 / C4H10-1 C4H10-1 / C5H12-1 C5H12-1 / C6H14-1 C6H14-1 FLOWSHEET BLOCK D1 IN=FEED OUT=DIS BOT PROPERTIES RK-SOAVE USER-PROPS DRUSR2 1 2 3 PROP-DATA RKSKIJ-1 IN-UNITS ENG PROP-LIST RKSKIJ BPVAL C2H6 C3H8 -2.2000000E-3 BPVAL C2H6 C4H10-1 6.70000000E-3 BPVAL C2H6 C5H12-1 5.60000000E-3 BPVAL C2H6 C6H14-1 -.0156000000 BPVAL C3H8 C4H10-1 0.0 BPVAL C3H8 C5H12-1 .0233000000 BPVAL C3H8 C6H14-1 -2.2000000E-3 BPVAL C3H8 C2H6 -2.2000000E-3 BPVAL C4H10-1 C3H8 0.0 BPVAL C4H10-1 C5H12-1 .0204000000 BPVAL C4H10-1 C6H14-1 -.0111000000 BPVAL C4H10-1 C2H6 6.70000000E-3 BPVAL C5H12-1 C3H8 .0233000000 BPVAL C5H12-1 C4H10-1 .0204000000 BPVAL C5H12-1 C2H6 5.60000000E-3 STREAM FEED SUBSTREAM MIXED TEMP=225 PRES=250 MOLE-FLOW C2H6 30 / C3H8 200 / C4H10-1 370 / C5H12-1 & 350 / C6H14-1 50

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BLOCK D1 RADFRAC PARAM NSTAGE=14 COL-CONFIG CONDENSER=PARTIAL-V FEEDS FEED 7 PRODUCTS BOT 14 L / DIS 1 V P-SPEC 1 248 COL-SPECS D:F=.226 DP-COL=4 MOLE-RR=6.06 SPEC 1 MOLE-FLOW 191 PHASE=V STAGE=1 COMPS=C3H8 VARY 1 MOLE-RR 3 9 STREAM-REPOR MOLEFLOW

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BOT DIS FEED ------------ STREAM ID BOT DIS FEED FROM : D1 D1 ---- TO : ---- ---- D1 SUBSTREAM: MIXED PHASE: LIQUID VAPOR MIXED COMPONENTS: LBMOL/HR C2H6 3.5935-03 29.9964 30.0000 C3H8 9.0000 191.0000 200.0000 C4H10-1 365.0282 4.9718 370.0000 C5H12-1 349.9682 3.1817-02 350.0000 C6H14-1 50.0000 5.6799-06 50.0000 TOTAL FLOW: LBMOL/HR 774.0000 226.0000 1000.0000 LB/HR 5.1173+04 9615.6886 6.0789+04 CUFT/HR 1757.1876 4228.0955 7798.4407 STATE VARIABLES: TEMP F 260.8017 115.0748 225.0000 PRES PSI 252.0000 248.0000 250.0000 VFRAC 0.0 1.0000 0.2831 LFRAC 1.0000 0.0 0.7169 SFRAC 0.0 0.0 0.0 ENTHALPY: BTU/LBMOL -6.1678+04 -4.4212+04 -5.7856+04 BTU/LB -932.8868 -1039.1178 -951.7619 BTU/HR -4.7738+07 -9.9918+06 -5.7856+07 ENTROPY: BTU/LBMOL-R -105.9894 -66.3064 -96.4772 BTU/LB-R -1.6031 -1.5584 -1.5871 DENSITY: LBMOL/CUFT 0.4405 5.3452-02 0.1282 LB/CUFT 29.1220 2.2742 7.7950 AVG MW 66.1148 42.5473 60.7885

`,/.+66!N8;*!X=*)=*!!BLOCK: D1 MODEL: RADFRAC ------------------------------- INLETS - FEED STAGE 7 OUTLETS - DIS STAGE 1 BOT STAGE 14 PROPERTY OPTION SET: RK-SOAVE STANDARD RKS EQUATION OF STATE

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*** MASS AND ENERGY BALANCE *** IN OUT RELATIVE DIFF. TOTAL BALANCE MOLE(LBMOL/HR) 1000.00 1000.00 -0.113687E-15 MASS(LB/HR ) 60788.5 60788.5 -0.263325E-14 ENTHALPY(BTU/HR ) -0.578562E+08 -0.577303E+08 -0.217615E-02

**** INPUT DATA **** NUMBER OF STAGES 14 ALGORITHM OPTION STANDARD ABSORBER OPTION NO INITIALIZATION OPTION STANDARD HYDRAULIC PARAMETER CALCULATIONS NO INSIDE LOOP CONVERGENCE METHOD BROYDEN DESIGN SPECIFICATION METHOD NESTED MAXIMUM NO. OF OUTSIDE LOOP ITERATIONS 25 MAXIMUM NO. OF INSIDE LOOP ITERATIONS 10 MAXIMUM NUMBER OF FLASH ITERATIONS 50 FLASH TOLERANCE 0.000100000 OUTSIDE LOOP CONVERGENCE TOLERANCE 0.000100000

**** COL-SPECS **** MOLAR VAPOR DIST / TOTAL DIST 1.00000 MOLAR REFLUX RATIO 6.06000 DISTILLATE TO FEED RATIO 0.22600 **** RESULTS ****

*** COMPONENT SPLIT FRACTIONS *** OUTLET STREAMS -------------- DIS BOT COMPONENT: C2H6 .99988 .11978E-03 C3H8 .95500 .45000E-01 C4H10-1 .13437E-01 .98656 C5H12-1 .90906E-04 .99991 C6H14-1 .11360E-06 1.0000

*** SUMMARY OF KEY RESULTS *** TOP STAGE TEMPERATURE F 115.075 BOTTOM STAGE TEMPERATURE F 260.802 TOP STAGE LIQUID FLOW LBMOL/HR 2,006.29 BOTTOM STAGE LIQUID FLOW LBMOL/HR 774.000 TOP STAGE VAPOR FLOW LBMOL/HR 226.000 BOTTOM STAGE VAPOR FLOW LBMOL/HR 1,655.79 MOLAR REFLUX RATIO 8.87737 MOLAR BOILUP RATIO 2.13927 CONDENSER DUTY (W/O SUBCOOL) BTU/HR -0.115854+08 REBOILER DUTY BTU/HR 0.117112+08

**** PROFILES **** **NOTE** REPORTED VALUES FOR STAGE LIQUID AND VAPOR RATES ARE THE FLOWS FROM THE STAGE EXCLUDING ANY SIDE PRODUCT. FOR THE FIRST STAGE, THE REPORTED VAPOR FLOW IS THE VAPOR DISTILLATE FLOW. FOR THE LAST STAGE, THE REPORTED LIQUID FLOW IS THE LIQUID BOTTOMS FLOW.

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ENTHALPY STAGE TEMPERATURE PRESSURE BTU/LBMOL HEAT DUTY F PSI LIQUID VAPOR BTU/HR 1 115.07 248.00 -50783. -44212. -.11585+08 2 125.28 248.31 -51581. -44928. 3 136.57 248.62 -52692. -45507. 5 170.39 249.23 -55843. -47215. 6 190.65 249.54 -57560. -48372. 7 209.38 249.85 -59032. -49521. 8 217.28 250.15 -59293. -50212. 11 235.62 251.08 -59970. -51780. 12 241.42 251.38 -60295. -52207. 13 248.99 251.69 -60816. -52686. 14 260.80 252.00 -61678. -53340. .11711+08 STAGE FLOW RATE FEED RATE PRODUCT RATE LBMOL/HR LBMOL/HR LBMOL/HR LIQUID VAPOR LIQUID VAPOR MIXED LIQUID VAPOR 1 2006. 226.0 226.0000 2 1955. 2232. 3 1864. 2181. 5 1677. 1989. 6 1600. 1903. 283.3846 7 2334. 1542. 716.6153 8 2372. 1560. 11 2453. 1661. 12 2454. 1679. 13 2430. 1680. 14 774.0 1656. 774.0000

**** MASS FLOW PROFILES **** STAGE FLOW RATE FEED RATE PRODUCT RATE LB/HR LB/HR LB/HR LIQUID VAPOR LIQUID VAPOR MIXED LIQUID VAPOR 1 0.8848E+05 9616. 9615.6886 2 0.8897E+05 0.9810E+05 3 0.8829E+05 0.9859E+05 5 0.8877E+05 0.9759E+05 6 0.8996E+05 0.9838E+05 .15740+05 7 0.1382E+06 0.8384E+05 .45048+05 8 0.1425E+06 0.8706E+05 11 0.1523E+06 0.9845E+05 12 0.1544E+06 0.1012E+06 13 0.1558E+06 0.1032E+06 14 0.5117E+05 0.1047E+06 .51173+05 **** MOLE-X-PROFILE **** STAGE C2H6 C3H8 C4H10-1 C5H12-1 C6H14-1 1 0.57253E-01 0.88576 0.56268E-01 0.71663E-03 0.36784E-06 2 0.26424E-01 0.84979 0.12085 0.29316E-02 0.41399E-05 3 0.14274E-01 0.74938 0.22597 0.10340E-01 0.39505E-04 5 0.75715E-02 0.43455 0.48005 0.75943E-01 0.18785E-02 6 0.66748E-02 0.29446 0.53451 0.15547 0.88845E-02 7 0.40998E-02 0.20293 0.52813 0.23898 0.25864E-01 8 0.16827E-02 0.15681 0.56948 0.24609 0.25942E-01 11 0.10271E-03 0.56172E-01 0.63050 0.28601 0.27216E-01 12 0.38791E-04 0.36411E-01 0.61454 0.31913 0.29880E-01 13 0.14072E-04 0.21933E-01 0.56594 0.37366 0.38453E-01 14 0.46428E-05 0.11628E-01 0.47161 0.45216 0.64599E-01

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**** MOLE-Y-PROFILE **** STAGE C2H6 C3H8 C4H10-1 C5H12-1 C6H14-1 1 0.13273 0.84513 0.21999E-01 0.14078E-03 0.25132E-07 2 0.64894E-01 0.88165 0.52798E-01 0.65833E-03 0.33314E-06 3 0.37438E-01 0.84931 0.11061 0.26424E-02 0.37136E-05 5 0.23512E-01 0.62700 0.32189 0.27326E-01 0.27279E-03 6 0.22436E-01 0.48332 0.42565 0.66941E-01 0.16554E-02 7 0.14670E-01 0.37152 0.48748 0.12031 0.60259E-02 8 0.61322E-02 0.29788 0.55617 0.13318 0.66399E-02 11 0.38744E-03 0.11540 0.69553 0.18013 0.85532E-02 12 0.14792E-03 0.76709E-01 0.70375 0.20941 0.99812E-02 13 0.54526E-04 0.47830E-01 0.68040 0.25783 0.13882E-01 14 0.18479E-04 0.26750E-01 0.61003 0.33697 0.26231E-01

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================================================================================================================================= : : : DESIGN : C O N S T R U C T I O N : MISC. AND : : PERCENT : :NO.: I T E M : ENG'G AND :-------------------------------------------------: ALL *: AMOUNT : OF : : : :PROCUREMENT: MATERIAL : MANHOURS : MANPOWER : INDIRECTS :SUBCONTRACTS : : CONTRACT : : : : K-USD : K-USD : : K-USD : K-USD : K-USD : K-USD : TOTAL : ================================================================================================================================= 1 PURCHASED EQUIPMENT - 289.2 - - - - 289.2 18.4 2 EQUIPMENT SETTING - - 265. 5.6 - - 5.6 0.4 3 PIPING - 93.2 2599. 59.7 - - 152.9 9.8 4 CIVIL - 15.4 710. 12.0 - - 27.5 1.8 5 STEEL - 7.0 218. 3.9 - - 10.9 0.7 6 INSTRUMENTATION - 89.6 1455. 33.3 - - 122.9 7.8 7 ELECTRICAL - 17.5 380. 7.9 - - 25.5 1.6 8 INSULATION - 34.7 1242. 24.3 - - 58.9 3.8 9 PAINT - 2.5 343. 5.4 - - 7.9 0.5 10 OTHER 350.7 56.3 - 0.0 321.3 - 728.3 46.5 -------------------- ------- --------- --------- -------- -------- -------- ------------ ----- 11 SUBTOTAL, DIRECT 350.7 605.4 7210. 152.1 321.3 - 1429.6 91.2 12 SUBCONTRACTS - - - - 0.0 0.0 0.0 13 G AND A OVERHEADS 0.0 18.2 4.6 9.6 0.0 32.4 2.1 14 CONTRACT FEE 33.0 21.8 16.5 34.8 0.0 106.0 6.8 -------------------- ------- --------- -------- -------- -------- ------------ ----- 15 BASE TOTAL 383.7 645.4 173.2 365.7 0.0 1568.0 100.0 16 ESCALATION 0.0 0.0 0.0 0.0 0.0 0.0 0.0 17 CONTINGENCIES 69.1 116.2 31.2 65.8 0.0 282.2 18.0 18 SPECIAL CHARGES - - - - 0.0 0.0 0.0 -------------------- ------- --------- -------- -------- -------- ------------ ----- 19 TOTAL 452.7 761.6 204.3 431.6 0.0 1850.2 118.0 ================================================================================================================================= * NO SUBCONTRACTS

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=========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. HT - 3 HORIZ DRUM D1-cond acc Shell material A 515 19000 CODE OF ACCOUNT: 114 Liquid volume 2350.23 GALLONS TAG NO.: D1-cond acc Vessel diameter 5.000 FEET Vessel tangent to tangent length 16.00 FEET Design temperature 250.00 DEG F Design gauge pressure 258.30 PSIG Application CONT Base material thickness 0.625 INCHES Total weight 9600 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 19000. 1.0000 : 593. 0.0312 29 : 0.031 : PIPING : 14291. 0.7522 : 8952. 0.4712 391 : 0.626 : CIVIL : 1587. 0.0835 : 2031. 0.1069 120 : 1.280 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 21954. 1.1555 : 3823. 0.2012 164 : 0.174 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 0. 0.0000 : 0. 0.0000 0 : 0.000 : PAINT : 801. 0.0421 : 1399. 0.0736 89 : 1.748 : ------------------------------------------------------------------------- SUBTOTAL : 57633. 3.0333 : 16799. 0.8842 793 : 0.291 : TOTAL MATERIAL AND MANPOWER COST =USD 74400. INST'L COST/PE RATIO = 3.916 ========================================================================================================================== =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. CP - 4 CENTRIF D1-reflux pump Casing material CS 5200 CODE OF ACCOUNT: 161 Liquid flow rate 401.99 GPM TAG NO.: D1-reflux pu Fluid head 50.00 FEET Design temperature 250.00 DEG F Speed 3600.00 RPM Driver power 5.000 HP Design gauge pressure 258.30 PSIG Driver type MOTOR Seal type SNGL Total weight 530 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 5200. 1.0000 : 383. 0.0737 19 : 0.074 : PIPING : 9746. 1.8743 : 4684. 0.9007 204 : 0.481 : CIVIL : 170. 0.0327 : 523. 0.1005 31 : 3.077 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 6262. 1.2042 : 1747. 0.3359 76 : 0.279 : ELECTRICAL : 596. 0.1147 : 898. 0.1727 42 : 1.506 : INSULATION : 2557. 0.4918 : 1928. 0.3708 98 : 0.754 : PAINT : 144. 0.0276 : 350. 0.0673 22 : 2.437 : ------------------------------------------------------------------------- SUBTOTAL : 24675. 4.7452 : 10512. 2.0216 492 : 0.426 : TOTAL MATERIAL AND MANPOWER COST =USD 35200. INST'L COST/PE RATIO = 6.769 ========================================================================================================================== Equipment mapped from 'D1'. QUOTE EQP- 5 D1-overhead split Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: D1-overhead ==========================================================================================================================

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. QUOTE EQP- 6 D1-bottoms split Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: D1-bottoms s ========================================================================================================================== Equipment mapped from 'D1'. RB - 7 KETTLE D1-reb Tube material A 214 52600 CODE OF ACCOUNT: 262 Heat transfer area 3579.55 SF TAG NO.: D1-reb Shell material A285C TEMA type BKT Shell design gauge pressure 262.00 PSIG Shell design temperature 310.80 DEG F Shell diameter 54.00 INCHES Shell length 25.00 FEET Tube port diameter 36.00 INCHES Tube design gauge pressure 60.30 PSIG Tube design temperature 331.00 DEG F Tube outside diameter 1.000 INCHES Tube length extended 20.00 FEET Total weight 34300 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 52600. 1.0000 : 1152. 0.0219 52 : 0.022 : PIPING : 13678. 0.2600 : 11432. 0.2173 495 : 0.836 : CIVIL : 1436. 0.0273 : 1881. 0.0358 111 : 1.310 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 13153. 0.2501 : 4707. 0.0895 205 : 0.358 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 8253. 0.1569 : 5679. 0.1080 291 : 0.688 : PAINT : 292. 0.0056 : 736. 0.0140 47 : 2.519 : ------------------------------------------------------------------------- SUBTOTAL : 89412. 1.6999 : 25587. 0.4864 1201 : 0.286 : TOTAL MATERIAL AND MANPOWER COST =USD 115000. INST'L COST/PE RATIO = 2.186 ========================================================================================================================== =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. TW - 10 TRAYED D1-tower Shell material A 515 64100 CODE OF ACCOUNT: 111 Number of trays 15 TAG NO.: D1-tower Vessel diameter 5.000 FEET Vessel tangent to tangent height 42.00 FEET Design temperature 310.80 DEG F Design gauge pressure 262.30 PSIG Application DISTIL Tray type SIEVE Tray spacing 24.00 INCHES Tray material A285C Tray thickness 0.188 INCHES Base material thickness 0.625 INCHES Total weight 31500 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 64100. 1.0000 : 1877. 0.0293 92 : 0.029 : PIPING : 20847. 0.3252 : 14937. 0.2330 651 : 0.716 : CIVIL : 1572. 0.0245 : 2153. 0.0336 127 : 1.370 : STRUCTURAL STEEL : 7021. 0.1095 : 3924. 0.0612 218 : 0.559 : INSTRUMENTATION : 36315. 0.5665 : 16719. 0.2608 729 : 0.460 : ELECTRICAL : 1678. 0.0262 : 909. 0.0142 45 : 0.542 : INSULATION : 10270. 0.1602 : 8250. 0.1287 423 : 0.803 : PAINT : 643. 0.0100 : 1376. 0.0215 88 : 2.141 : ------------------------------------------------------------------------- SUBTOTAL : 142445. 2.2222 : 50145. 0.7823 2373 : 0.352 : TOTAL MATERIAL AND MANPOWER COST =USD 192600. INST'L COST/PE RATIO = 3.005 ==========================================================================================================================

Page 955: Product and Process Design Principles - Seider

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. HE - 13 FLOAT HEAD D1-cond Tube material A 214 139400 CODE OF ACCOUNT: 261 Number of shells 2 TAG NO.: D1-cond Area per shell 5551.00 SF Shell material A285C TEMA type BES Shell design gauge pressure 258.61 PSIG Shell design temperature 250.00 DEG F Shell diameter 46.00 INCHES Shell length 23.00 FEET Tube design gauge pressure 60.30 PSIG Tube design temperature 250.00 DEG F Tube outside diameter 1.000 INCHES Tube length extended 20.00 FEET Total weight 89200 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 139400. 1.0000 : 1601. 0.0115 73 : 0.011 : PIPING : 34630. 0.2484 : 15175. 0.1089 665 : 0.438 : CIVIL : 1237. 0.0089 : 1693. 0.0121 100 : 1.369 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 8835. 0.0634 : 2876. 0.0206 125 : 0.326 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 13585. 0.0975 : 8413. 0.0604 430 : 0.619 : PAINT : 636. 0.0046 : 1512. 0.0108 96 : 2.377 : ------------------------------------------------------------------------- SUBTOTAL : 198323. 1.4227 : 31270. 0.2243 1489 : 0.158 : TOTAL MATERIAL AND MANPOWER COST =USD 229600. INST'L COST/PE RATIO = 1.647 ==========================================================================================================================

Page 956: Product and Process Design Principles - Seider

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A R E A B U L K R E P O R T ================================================================================================================================= : : : : : M A N P O W E R : TOTAL : : : ITEM : D E S C R I P T I O N :------------------------------------: MATERIAL :------------------: DIRECT : :ORIGIN : SYMBOL :---------: D E S I G N D A T A : COST-USD : MANHOURS:COST-USD: COST-USD: ================================================================================================================================= AREA MISC CONCRETE ITEMS 638. 138 2341. 2979. AREA PIPE TESTING 0. 192 4564. 4564. GRADE UNPAVED AREA 7534. 127 2648. 10182. Area length 50.000 FEET Area width 50.000 FEET AREA INSTRUMENT TESTING 0. 95 2124. 2124. AREA INSTR. RUNS,TRAYS,JBOX. 3086. 60 1266. 4352. AREA EQUIPMENT GROUNDING 185. 11 231. 416. AREA PILED FOUNDATION 8807. 83 1407. 10214. Number of piles 14 AREA ELECTRICAL TESTING 0. 16 344. 344. AREA ROTATING EQP SPARE PARTS 370. 0 0. 370.

Page 957: Product and Process Design Principles - Seider

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1><@:<L=PI>@$9P?H$?H>$0>F:PB>@$8K;<$`Z>>$1()R08$J:BD>@a$$

!C O N T R A C T S U M M A R Y

PRIME CONTRACTOR (CONTRACT NO. 1)

================================================================================================================================= : : : DESIGN : C O N S T R U C T I O N : MISC. AND : : PERCENT : :NO.: I T E M : ENG'G AND :-------------------------------------------------: ALL *: AMOUNT : OF : : : :PROCUREMENT: MATERIAL : MANHOURS : MANPOWER : INDIRECTS :SUBCONTRACTS : : CONTRACT : : : : K-USD : K-USD : : K-USD : K-USD : K-USD : K-USD : TOTAL : ================================================================================================================================= 1 PURCHASED EQUIPMENT - 296.9 - - - - 296.9 17.9 2 EQUIPMENT SETTING - - 287. 6.1 - - 6.1 0.4 3 PIPING - 107.8 2865. 65.9 - - 173.7 10.5 4 CIVIL - 15.6 744. 12.6 - - 28.2 1.7 5 STEEL - 7.0 218. 3.9 - - 10.9 0.7 6 INSTRUMENTATION - 95.9 1536. 35.1 - - 131.0 7.9 7 ELECTRICAL - 18.2 426. 8.9 - - 27.1 1.6 8 INSULATION - 38.5 1355. 26.5 - - 65.0 3.9 9 PAINT - 2.7 374. 5.9 - - 8.6 0.5 10 OTHER 371.0 59.7 - 0.0 333.4 - 764.1 46.1 -------------------- ------- --------- --------- -------- -------- -------- ------------ ----- 11 SUBTOTAL, DIRECT 371.0 642.3 7805. 164.9 333.4 - 1511.6 91.3 12 SUBCONTRACTS - - - - 0.0 0.0 0.0 13 G AND A OVERHEADS 0.0 19.3 4.9 10.0 0.0 34.2 2.1 14 CONTRACT FEE 34.5 22.5 17.7 35.7 0.0 110.4 6.7 -------------------- ------- --------- -------- -------- -------- ------------ ----- 15 BASE TOTAL 405.5 684.0 187.5 379.2 0.0 1656.2 100.0 16 ESCALATION 0.0 0.0 0.0 0.0 0.0 0.0 0.0 17 CONTINGENCIES 73.0 123.1 33.7 68.3 0.0 298.1 18.0 18 SPECIAL CHARGES - - - - 0.0 0.0 0.0 -------------------- ------- --------- -------- -------- -------- ------------ ----- 19 TOTAL 478.5 807.2 221.2 447.4 0.0 1954.3 118.0 ================================================================================================================================= * NO SUBCONTRACTS!

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Page 958: Product and Process Design Principles - Seider

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== CP - 8 CENTRIF reboiler pump Casing material CS 7000 CODE OF ACCOUNT: 161 Liquid flow rate 756.52 GPM Fluid head 20.00 FEET Design temperature 298.99 DEG F Speed 3600.00 RPM Driver power 3.000 HP Design gauge pressure 262.00 PSIG Driver type MOTOR Seal type SNGL Total weight 630 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 7000. 1.0000 : 463. 0.0662 23 : 0.066 : PIPING : 14619. 2.0884 : 5699. 0.8141 248 : 0.390 : CIVIL : 160. 0.0229 : 504. 0.0720 30 : 3.146 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 6277. 0.8967 : 1747. 0.2495 76 : 0.278 : ELECTRICAL : 596. 0.0852 : 898. 0.1283 42 : 1.506 : INSULATION : 3826. 0.5465 : 2219. 0.3170 113 : 0.580 : PAINT : 201. 0.0287 : 487. 0.0695 31 : 2.420 : ------------------------------------------------------------------------- SUBTOTAL : 32680. 4.6685 : 12016. 1.7166 563 : 0.368 : TOTAL MATERIAL AND MANPOWER COST =USD 44700. INST'L COST/PE RATIO = 6.386 ==========================================================================================================================

!!!!!!!!!!!!!!!!!!!!!!!!!!!!

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A R E A B U L K R E P O R T ================================================================================================================================= : : : : : M A N P O W E R : TOTAL : : : ITEM : D E S C R I P T I O N :------------------------------------: MATERIAL :------------------: DIRECT : :ORIGIN : SYMBOL :---------: D E S I G N D A T A : COST-USD : MANHOURS:COST-USD: COST-USD: ================================================================================================================================= AREA MISC CONCRETE ITEMS 657. 142 2413. 3070. AREA PIPE TESTING 0. 211 5002. 5002. GRADE UNPAVED AREA 7534. 127 2648. 10182. Area length 50.000 FEET Area width 50.000 FEET AREA INSTRUMENT TESTING 0. 100 2242. 2242. AREA INSTR. RUNS,TRAYS,JBOX. 3086. 60 1266. 4352. AREA EQUIPMENT GROUNDING 222. 14 277. 499. AREA PILED FOUNDATION 8807. 83 1407. 10214. Number of piles 14 AREA ELECTRICAL TESTING 0. 17 376. 376. AREA ROTATING EQP SPARE PARTS 860. 0 0. 860.

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Page 960: Product and Process Design Principles - Seider

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Page 961: Product and Process Design Principles - Seider

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!C O N T R A C T S U M M A R Y

PRIME CONTRACTOR (CONTRACT NO. 1)

================================================================================================================================= : : : DESIGN : C O N S T R U C T I O N : MISC. AND : : PERCENT : :NO.: I T E M : ENG'G AND :-------------------------------------------------: ALL *: AMOUNT : OF : : : :PROCUREMENT: MATERIAL : MANHOURS : MANPOWER : INDIRECTS :SUBCONTRACTS : : CONTRACT : : : : K-USD : K-USD : : K-USD : K-USD : K-USD : K-USD : TOTAL : ================================================================================================================================= 1 PURCHASED EQUIPMENT - 159.5 - - - - 159.5 8.4 2 EQUIPMENT SETTING - - 390. 8.3 - - 8.3 0.4 3 PIPING - 76.9 4404. 101.6 - - 178.6 9.4 4 CIVIL - 23.1 1086. 18.4 - - 41.5 2.2 5 STEEL - 12.6 333. 6.0 - - 18.6 1.0 6 INSTRUMENTATION - 147.7 2704. 61.9 - - 209.6 11.1 7 ELECTRICAL - 20.0 485. 10.1 - - 30.1 1.6 8 INSULATION - 44.3 1924. 37.7 - - 82.0 4.3 9 PAINT - 2.3 346. 5.4 - - 7.7 0.4 10 OTHER 513.1 49.9 - 0.0 425.9 - 988.9 52.1 -------------------- ------- --------- --------- -------- -------- -------- ------------ ----- 11 SUBTOTAL, DIRECT 513.1 536.2 11672. 249.5 425.9 - 1724.8 91.0 12 SUBCONTRACTS - - - - 0.0 0.0 0.0 13 G AND A OVERHEADS 0.0 16.1 7.5 12.8 0.0 36.4 1.9 14 CONTRACT FEE 45.2 20.4 25.7 43.9 0.0 135.2 7.1 -------------------- ------- --------- -------- -------- -------- ------------ ----- 15 BASE TOTAL 558.3 572.8 282.7 482.6 0.0 1896.3 100.0 16 ESCALATION 0.0 0.0 0.0 0.0 0.0 0.0 0.0 17 CONTINGENCIES 100.5 103.1 50.9 86.9 0.0 341.3 18.0 18 SPECIAL CHARGES - - - - 0.0 0.0 0.0 -------------------- ------- --------- -------- -------- -------- ------------ ----- 19 TOTAL 658.7 675.9 333.6 569.4 0.0 2237.6 118.0 ================================================================================================================================= * NO SUBCONTRACTS

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Page 962: Product and Process Design Principles - Seider

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'A1'. TW - 2 TRAYED A1-tower Shell material A 515 16000 CODE OF ACCOUNT: 111 Number of trays 15 TAG NO.: A1-tower Vessel diameter 1.500 FEET Vessel tangent to tangent height 42.00 FEET Design temperature 320.00 DEG F Design gauge pressure 60.30 PSIG Application DISTIL Tray type SIEVE Tray spacing 24.00 INCHES Tray material A285C Tray thickness 0.188 INCHES Base material thickness 0.500 INCHES Total weight 6400 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 16000. 1.0000 : 512. 0.0320 25 : 0.032 : PIPING : 8486. 0.5304 : 14966. 0.9354 647 : 1.764 : CIVIL : 909. 0.0568 : 1434. 0.0896 84 : 1.578 : STRUCTURAL STEEL : 4590. 0.2869 : 2162. 0.1351 120 : 0.471 : INSTRUMENTATION : 31542. 1.9714 : 16719. 1.0449 729 : 0.530 : ELECTRICAL : 1152. 0.0720 : 696. 0.0435 34 : 0.604 : INSULATION : 4921. 0.3075 : 4701. 0.2938 240 : 0.955 : PAINT : 380. 0.0238 : 860. 0.0538 55 : 2.264 : ------------------------------------------------------------------------- SUBTOTAL : 67980. 4.2488 : 42051. 2.6282 1934 : 0.619 : TOTAL MATERIAL AND MANPOWER COST =USD 110000. INST'L COST/PE RATIO = 6.875 ========================================================================================================================= =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. TW - 3 TRAYED D1-tower Shell material A 515 53500 CODE OF ACCOUNT: 111 Number of trays 30 TAG NO.: D1-tower Vessel diameter 3.000 FEET Vessel tangent to tangent height 72.00 FEET Design temperature 353.02 DEG F Design gauge pressure 35.30 PSIG Application DISTIL Tray type SIEVE Tray spacing 24.00 INCHES Tray material A285C Tray thickness 0.188 INCHES Average wall thickness 0.417 INCHES Total weight 21400 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 53500. 1.0000 : 1727. 0.0323 84 : 0.032 : PIPING : 13675. 0.2556 : 17933. 0.3352 778 : 1.311 : CIVIL : 1136. 0.0212 : 1685. 0.0315 99 : 1.484 : STRUCTURAL STEEL : 7974. 0.1491 : 3845. 0.0719 213 : 0.482 : INSTRUMENTATION : 35223. 0.6584 : 16909. 0.3161 737 : 0.480 : ELECTRICAL : 2230. 0.0417 : 1193. 0.0223 59 : 0.535 : INSULATION : 11094. 0.2074 : 9098. 0.1701 466 : 0.820 : PAINT : 620. 0.0116 : 1350. 0.0252 86 : 2.178 : ------------------------------------------------------------------------- SUBTOTAL : 125452. 2.3449 : 53740. 1.0045 2522 : 0.428 : TOTAL MATERIAL AND MANPOWER COST =USD 179200. INST'L COST/PE RATIO = 3.350 ==========================================================================================================================

Page 963: Product and Process Design Principles - Seider

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. HE - 4 FIXED T S D1-cond Tube material A 214 12200 CODE OF ACCOUNT: 261 Heat transfer area 154.71 SF TAG NO.: D1-cond Shell material A285C TEMA type BEM Shell design gauge pressure 35.30 PSIG Shell design temperature 255.39 DEG F Shell diameter 8.000 INCHES Shell length 20.00 FEET Tube design gauge pressure 60.30 PSIG Tube design temperature 255.39 DEG F Tube outside diameter 1.000 INCHES Tube length extended 20.00 FEET Total weight 1800 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 12200. 1.0000 : 841. 0.0689 38 : 0.069 : PIPING : 9609. 0.7876 : 8169. 0.6696 358 : 0.850 : CIVIL : 669. 0.0549 : 1120. 0.0918 66 : 1.673 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 7741. 0.6345 : 2859. 0.2344 125 : 0.369 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 3692. 0.3026 : 2988. 0.2449 152 : 0.809 : PAINT : 213. 0.0175 : 516. 0.0423 33 : 2.419 : ------------------------------------------------------------------------- SUBTOTAL : 34124. 2.7971 : 16492. 1.3518 772 : 0.483 : TOTAL MATERIAL AND MANPOWER COST =USD 50600. INST'L COST/PE RATIO = 4.148 ========================================================================================================================= ========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. HT - 5 HORIZ DRUM D1-cond acc Shell material A 515 7500 CODE OF ACCOUNT: 114 Liquid volume 237.96 GALLONS TAG NO.: D1-cond acc Vessel diameter 3.000 FEET Vessel tangent to tangent length 4.500 FEET Design temperature 254.98 DEG F Design gauge pressure 35.30 PSIG Application CONT Base material thickness 0.313 INCHES Total weight 1500 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 7500. 1.0000 : 511. 0.0681 25 : 0.068 : PIPING : 5991. 0.7988 : 8621. 1.1495 373 : 1.439 : CIVIL : 995. 0.1326 : 1453. 0.1937 86 : 1.461 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 16896. 2.2527 : 3624. 0.4832 156 : 0.215 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 2474. 0.3298 : 2678. 0.3571 136 : 1.083 : PAINT : 142. 0.0189 : 376. 0.0501 24 : 2.642 : ------------------------------------------------------------------------- SUBTOTAL : 33997. 4.5329 : 17263. 2.3017 800 : 0.508 : TOTAL MATERIAL AND MANPOWER COST =USD 51300. INST'L COST/PE RATIO = 6.840 ==========================================================================================================================

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. CP - 6 CENTRIF D1-reflux pump Casing material CS 3300 CODE OF ACCOUNT: 161 Liquid flow rate 37.44 GPM TAG NO.: D1-reflux pu Fluid head 70.00 FEET Design temperature 254.98 DEG F Speed 3600.00 RPM Driver power 1.000 HP Design gauge pressure 35.30 PSIG Driver type MOTOR Seal type SNGL Total weight 200 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 3300. 1.0000 : 205. 0.0621 10 : 0.062 : PIPING : 3202. 0.9704 : 4783. 1.4493 206 : 1.494 : CIVIL : 141. 0.0429 : 468. 0.1417 27 : 3.306 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 4916. 1.4896 : 1747. 0.5293 76 : 0.355 : ELECTRICAL : 596. 0.1807 : 898. 0.2721 42 : 1.506 : INSULATION : 1685. 0.5106 : 1734. 0.5256 88 : 1.029 : PAINT : 79. 0.0241 : 218. 0.0661 14 : 2.746 : ------------------------------------------------------------------------- SUBTOTAL : 13920. 4.2181 : 10052. 3.0462 463 : 0.722 : TOTAL MATERIAL AND MANPOWER COST =USD 24000. INST'L COST/PE RATIO = 7.273 ========================================================================================================================== Equipment mapped from 'D1'. QUOTE EQP- 7 D1-overhead split Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: D1-overhead ========================================================================================================================== ========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'D1'. QUOTE EQP- 8 D1-bottoms split Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: D1-bottoms s ========================================================================================================================== Equipment mapped from 'D1'. RB - 9 U TUBE D1-reb Tube material A 214 23500 CODE OF ACCOUNT: 262 Heat transfer area 921.20 SF TAG NO.: D1-reb Shell material A285C TEMA type BKU Shell design gauge pressure 35.30 PSIG Shell design temperature 353.02 DEG F Shell diameter 39.00 INCHES Shell length 13.00 FEET Tube port diameter 26.00 INCHES Tube design gauge pressure 110.30 PSIG Tube design temperature 377.80 DEG F Tube outside diameter 1.000 INCHES Tube length extended 20.00 FEET Total weight 9100 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 23500. 1.0000 : 713. 0.0303 32 : 0.030 : PIPING : 8327. 0.3543 : 9585. 0.4079 416 : 1.151 : CIVIL : 1067. 0.0454 : 1526. 0.0649 90 : 1.431 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 12322. 0.5243 : 4641. 0.1975 203 : 0.377 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 5213. 0.2218 : 4266. 0.1815 218 : 0.818 : PAINT : 189. 0.0081 : 480. 0.0204 31 : 2.536 : ------------------------------------------------------------------------- SUBTOTAL : 50618. 2.1540 : 21210. 0.9026 990 : 0.419 : TOTAL MATERIAL AND MANPOWER COST =USD 71800. INST'L COST/PE RATIO = 3.055

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'F1'. VT - 10 CYLINDER F1 Shell material A 515 7100 CODE OF ACCOUNT: 113 Liquid volume 264.40 GALLONS TAG NO.: F1 Vessel diameter 3.000 FEET Vessel tangent to tangent height 5.000 FEET Design temperature 320.00 DEG F Design gauge pressure 35.30 PSIG Application CONT Base material thickness 0.313 INCHES Total weight 1400 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 7100. 1.0000 : 512. 0.0721 25 : 0.072 : PIPING : 7383. 1.0398 : 8809. 1.2406 381 : 1.193 : CIVIL : 659. 0.0929 : 1103. 0.1554 65 : 1.673 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 17931. 2.5255 : 3739. 0.5266 161 : 0.209 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 3291. 0.4635 : 3060. 0.4309 156 : 0.930 : PAINT : 172. 0.0242 : 448. 0.0631 29 : 2.605 : ------------------------------------------------------------------------- SUBTOTAL : 36536. 5.1459 : 17670. 2.4887 817 : 0.484 : TOTAL MATERIAL AND MANPOWER COST =USD 54200. INST'L COST/PE RATIO = 7.634 ========================================================================================================================== =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'H1'. HE - 11 JACKETED H1 Material CS 16100 CODE OF ACCOUNT: 263 Heat transfer area 160.11 SF TAG NO.: H1 Tube length 20.00 FEET Number of tubes per shell 1 Design gauge pressure 60.30 PSIG Temperature 331.00 DEG F Number of sections 8 Total weight 7280 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 16100. 1.0000 : 2195. 0.1363 100 : 0.136 : PIPING : 9192. 0.5709 : 8144. 0.5059 357 : 0.886 : CIVIL : 1937. 0.1203 : 2415. 0.1500 143 : 1.247 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 5647. 0.3507 : 1635. 0.1016 69 : 0.290 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 5778. 0.3589 : 4314. 0.2680 220 : 0.747 : PAINT : 213. 0.0132 : 516. 0.0320 33 : 2.419 : ------------------------------------------------------------------------- SUBTOTAL : 38867. 2.4141 : 19219. 1.1937 922 : 0.494 : TOTAL MATERIAL AND MANPOWER COST =USD 58100. INST'L COST/PE RATIO = 3.609 ==========================================================================================================================

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C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'H2'. HE - 12 FLOAT HEAD H2 Tube material A 214 12400 CODE OF ACCOUNT: 261 Heat transfer area 195.80 SF TAG NO.: H2 Shell material A285C TEMA type BES Shell design gauge pressure 35.30 PSIG Shell design temperature 353.02 DEG F Shell diameter 10.00 INCHES Shell length 22.00 FEET Tube design gauge pressure 60.30 PSIG Tube design temperature 353.02 DEG F Tube outside diameter 1.000 INCHES Tube length extended 20.00 FEET Total weight 2500 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 12400. 1.0000 : 874. 0.0705 40 : 0.070 : PIPING : 9626. 0.7763 : 8205. 0.6617 360 : 0.852 : CIVIL : 679. 0.0547 : 1132. 0.0913 67 : 1.669 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 7742. 0.6243 : 2868. 0.2313 125 : 0.370 : ELECTRICAL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSULATION : 5130. 0.4137 : 3490. 0.2814 177 : 0.680 : PAINT : 215. 0.0173 : 519. 0.0418 33 : 2.417 : ------------------------------------------------------------------------- SUBTOTAL : 35791. 2.8863 : 17087. 1.3780 802 : 0.477 : TOTAL MATERIAL AND MANPOWER COST =USD 52900. INST'L COST/PE RATIO = 4.266 ========================================================================================================================== ========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'M1'. QUOTE EQP- 14 M1 Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: M1 ========================================================================================================================== Equipment mapped from 'S1'. QUOTE EQP- 15 S1 Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: S1 ========================================================================================================================== Equipment mapped from 'P1'. CP - 18 CENTRIF P1 Casing material CS 2800 CODE OF ACCOUNT: 161 Liquid flow rate 22.73 GPM TAG NO.: P1 Fluid head 62.10 FEET Design temperature 250.00 DEG F Speed 3600.00 RPM Driver power 1.500 HP Fluid viscosity 0.583 CPOISE Design gauge pressure 60.30 PSIG Driver type MOTOR Seal type SNGL Total weight 210 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 2800. 1.0000 : 205. 0.0732 10 : 0.073 : PIPING : 1441. 0.5146 : 4641. 1.6576 200 : 3.221 : CIVIL : 148. 0.0529 : 481. 0.1717 28 : 3.246 : STRUCTURAL STEEL : 0. 0.0000 : 0. 0.0000 0 : 0.000 : INSTRUMENTATION : 4228. 1.5102 : 1747. 0.6239 76 : 0.413 : ELECTRICAL : 596. 0.2129 : 898. 0.3207 42 : 1.506 : INSULATION : 999. 0.3569 : 1391. 0.4967 71 : 1.392 : PAINT : 48. 0.0171 : 139. 0.0495 9 : 2.903 : ------------------------------------------------------------------------- SUBTOTAL : 10261. 3.6645 : 9501. 3.3933 436 : 0.926 : TOTAL MATERIAL AND MANPOWER COST =USD 19800. INST'L COST/PE RATIO = 7.071

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==========================================================================================================================

C O M P O N E N T L I S T =========================================================================================================================== : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A --------------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : =========================================================================================================================== Equipment mapped from 'T1'. QUOTE EQP- 19 T1 Number of identical items 1 0 CODE OF ACCOUNT: 100 TAG NO.: T1 ==========================================================================================================================

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A R E A B U L K R E P O R T ================================================================================================================================= : : : : : M A N P O W E R : TOTAL : : : ITEM : D E S C R I P T I O N :------------------------------------: MATERIAL :------------------: DIRECT : :ORIGIN : SYMBOL :---------: D E S I G N D A T A : COST-USD : MANHOURS:COST-USD: COST-USD: ================================================================================================================================= AREA MISC CONCRETE ITEMS 916. 198 3358. 4274. AREA PIPE TESTING 0. 328 7771. 7771. GRADE UNPAVED AREA 7534. 127 2648. 10182. Area length 50.000 FEET Area width 50.000 FEET AREA INSTRUMENT TESTING 0. 179 4012. 4012. AREA INSTR. RUNS,TRAYS,JBOX. 3471. 68 1450. 4921. AREA EQUIPMENT GROUNDING 369. 23 462. 831. AREA PILED FOUNDATION 13840. 131 2211. 16051. Number of piles 22 AREA ELECTRICAL TESTING 0. 20 430. 430. AREA ROTATING EQP SPARE PARTS 430. 0 0. 430.

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Page 1051: Product and Process Design Principles - Seider

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Page 1052: Product and Process Design Principles - Seider

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/9!,656'#'&6,!9/,Z!

VARIABLES Qs, Qcw, R1, R2, R3, R4, Z ; EQUATIONS OBJ,T1,T2,T3,T4,T5,B1,B2,B3,B4,B5,B6; OBJ .. Z =E= Qs; T1.. Qs-R1+30 =E= 0; T2.. R1-R2+2.5 =E= 0; T3.. R2-R3-82.5 =E= 0; T4.. R3-R4+75 =E= 0; T5.. R4-Qcw-15 =E= 0; B1.. R1 =G= 0; B2.. R2 =G= 0; B3.. R3 =G= 0; B4.. R4 =G= 0; B5.. Qs =G= 0; B6.. Qcw =G= 0; MODEL CASCADE /ALL/; SOLVE CASCADE USING LP MINIMIZING Z;

S O L V E S U M M A R Y MODEL CASCADE OBJECTIVE Z TYPE LP DIRECTION MINIMIZE SOLVER MINOS5 FROM LINE 38 **** SOLVER STATUS 1 NORMAL COMPLETION **** MODEL STATUS 1 OPTIMAL **** OBJECTIVE VALUE 50.0000!

Page 1053: Product and Process Design Principles - Seider

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Page 1054: Product and Process Design Principles - Seider

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9/,!*'+!:/<+2!(8<!<+.2(,+6!*'+!+P=(*;/86!*/!H+!;8.2=<+<!;8!*'+!:/<+2D!!T/,!8/?;.+!bK]0!=6+,6F!;*!

;6!,+./::+8<!*'(*!(22!+P=(*;/86!H+!;8.2=<+<D!!!U+8.+F!*'+!:/<+2!<+.2(,(*;/8!6*(*+:+8*!;6Z!

MODEL MODEL_NAME /ALL/;!

$

-:B[>$-?L?>;>=?"$7'+!6/2?+!6*(*+:+8*!<+9;8+6!*'+Z!

&D!! ]/<+2!*/!H+!/)*;:;C+<!A<+9;8+<!),+?;/=621!;8!*'+!:/<+2!<+.2(,(*;/8!6*(*+:+8*BD!

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!SOLVE MODEL_NAME USING PROBLEM_TYPE MINIMIZING OBJEC_FUNC_VARIABLE;!

!

7'+! 5+1! 4/,<6! t0XaqSY! (8<! tN0E3bY! :=6*! H+! ),+6+8*! ;8! *'+! 6*(*+:+8*F! (6! 4+22! (6! +;*'+,!

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Page 1055: Product and Process Design Principles - Seider

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2;8+(,!./86*,(;8*6!(8<!(!2;8+(,!/HV+.*;?+!9=8.*;/8!())+(,D!!7'+!/HV+.*;?+!9=8.*;/8!?(,;(H2+F!Z,! ;6!

:;8;:;C+<F!(8<!./86+P=+8*21F!*'+!6/2?+!6*(*+:+8*!;6Z!!

SOLVE CASCADE USING LP MINIMIZING Z;!

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7'+,+!(,+!6+?+,(2!/)*;:;C(*;/8!9/,:=2(*;/86!*'(*!.(8!H+!6/2?+<F!*'+!:/6*!./::/8!H+;8@Z!

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J:@;KBL?P:=$ 65M-$-A=?Lh$a;8+(,!),/@,(:! a`!];>+<!;8*+@+,!2;8+(,!),/@,(:! ]E`!3/82;8+(,!),/@,(:! 3a`!

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1:NK;>=?L?P:="$$E*!;6!;:)/,*(8*!*/!(<<!</.=:+8*(*;/8!*/!*'+!;8)=*!9;2+!*/!6;:)2;91!<+H=@@;8@!(6!

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Page 1056: Product and Process Design Principles - Seider

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())2;+<!=6;8@!*'+!6*(*+:+8*!

POSITIVE VARIABLES w,x;!

!

K2*+,8(*;?+21F! 9/,! ,+(2$?(2=+<! ?(,;(H2+6F! *';6! .(8! H+! (../:)2;6'+<! H1! <+9;8;8@! +P=(*;/86! *'(*!

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65M-$-A=?Lh! 0L=Q>$:=$,L@PLFB>!FREE A<+9(=2*B $V!*/!V!POSITIVE R!*/!WV!NEGATIVE $V!*/!R!BINARY R!/,!&!/821!INTEGER RF!&F!�F!&RR!

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<+9;8+!*'+!H;8(,1!?(,;(H2+F!:F!*';6!;6!(../:)2;6'+<!=6;8@!*'+!6*(*+:+8*Z!

BINARY VARIABLE y;

,L@PLFB>$1PZ<BLA"$K9*+,!./:)=*;8@!(!6/2=*;/8F!bK]0!<;6)2(16!*'+!?(,;(H2+!?(2=+6!;8!*'+!/=*)=*!

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7/! (../:)2;6'! *';6F! (!DISPLAY! 6*(*+:+8*! ;6! (<<+<! 9/22/4;8@! *'+!MODEL! 6*(*+:+8*D! !\';2+! (!

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DISPLAY R1.L,R2.L,R3.L,R4.L,Qcw.L,Qs.L !0=H6+P=+8*21F!*'+6+!(,+!<;6)2(1+<!;8!*'+!/=*)=*F!(6!6'/48!;8!T;@=,+!OD!!(h<L=D>D$ +=<K?$ JPB>$ C:@$ (hL;<B>$ .#"T"$K8! ;:),/?+<! ;8)=*! 9;2+! 9/,! S>(:)2+! &RDQF! 8(:+<!

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Page 1057: Product and Process Design Principles - Seider

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&:K=DZ$L=D$+=P?PLB$):=DP?P:=Z"$\'+8! *'+!H/=8<6!=6;8@!?(,;(H2+! ,+$<+.2(,(*;/8!6*(*+:+8*6!(,+!

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x.lo = 10.0;!

(8<!*/!6+*!(8!=))+,!H/=8<!9/,!/F!=6+Z!

x.up = 100.0;!

K8!;8;*;(2!6*(,*;8@!)/;8*!9/,!*'+!6/2?+,!;6!6=))2;+<!H1!*'+!=6+,!4;*'!*'+!;'?';!AtD2YB!+>*+86;/8Z!!

x.1 = 50.0;

L/=8<;8@!(8<!;8;*;(2;C(*;/8!6*(*+:+8*6!())+(,!(9*+,!*'+!?(,;(H2+!<+.2(,(*;/8!6*(*+:+8*6F!H=*!),;/,!

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VARIABLE R1.L = 80.000 VARIABLE R2.L = 82.500 VARIABLE R3.L = 0.000 VARIABLE R4.L = 75.000 VARIABLE QCW.L = 60.000 VARIABLE QS.L = 50.000

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* This is the input file for Example 10.4

* The GAMS file formulates an LP to be solved for minimum utilities * Declare the variables * Note that Z (used for the objective function) * 1. must be declared * 2. should not be made positive VARIABLES Qs, Qcw, R1, R2, R3, R4 Z minimum utilities ; * Remember the semi-colons !!! * Declare non-negative variables POSITIVE VARIABLE Qs, Qcw, R1, R2, R3, R4; * If desired, specify additional bounds on variables * or initial values could be specified here. * Now declare the equations in the problem! EQUATIONS COST this defines the objective function T1,T2,T3,T4,T5 ; * and define the equations just declared COST .. Z =E= Qs; T1.. Qs-R1+30 =E= 0; T2.. R1-R2+2.5 =E= 0; T3.. R2-R3-82.5 =E= 0; T4.. R3-R4+75 =E= 0; T5.. R4-Qcw-15 =E= 0; * Nearly done! Place all of the above in the model CASCADE MODEL CASCADE /ALL/; * and solve it using an LP solver SOLVE CASCADE USING LP MINIMIZING Z; * Let’s display these variables at the solution * at the end of the output file DISPLAY R1.L,R2.L,R3.L,R4.L,Qcw.L,Qs.L !

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!* Define variables VARIABLES Ah1c1, Ah1c2, F1, F2, F3, F4, F5, F6, F7, F8, T3, T4, T56, T78, DELh1c1, DELh1c2, Z heat exchanger cost ; * Declare total variables strictly non-negative POSITIVE VARIABLES Ah1c1, Ah1c2,F1, F2, F3, F4, F5, F6, F7, F8 ; * For NLPs, providing initial conditions and bounds can improve the solver's * likelihood of finding feasible solutions, as well as avoiding numerical * difficulties DELh1c1.L = 20 ; DELh1c1.LO = 10 ; DELh1c1.UP = 100 ; DELh1c2.L = 20 ; DELh1c2.LO = 10 ; DELh1c2.UP = 100 ; Ah1c1.L = 100.0 ; Ah1c2.L = 100.0 ; T3.L = 440 ; T3.LO = 330 ; T3.UP = 440 ; T4.L = 440 ; T4.LO = 330 ; T4.UP = 440 ; T56.L = 330 ; T56.LO = 330 ; T56.UP = 440 ; T78.L = 330 ; T78.LO = 330 ; T78.UP = 440 ; * Specify equations. EQUATIONS OBJ defines the objective function, MBALSPL1,MBALSPL2,MBALSPL3, MBALMIX1, MBALMIX2, EBALMIX1, EBALMIX2, EBALEX1, EBALEX2, FEAS1, FEAS2, FEAS3, FEAS4, AREA1, AREA2, DELTAC1, DELTAC2; OBJ.. Z =E= 1300*(Ah1c1**0.6)+1300*(Ah1c2**0.6); MBALSPL1.. F1+F2 =E= 22; MBALSPL2.. F3-F5-F6 =E= 0; MBALSPL3.. F4-F7-F8 =E= 0; MBALMIX1.. F3-F1-F8 =E= 0; MBALMIX2.. F4-F2-F6 =E= 0; EBALMIX1.. 440*F1+T78*F8-T3*F3 =E= 0; EBALMIX2.. 440*F2+T56*F6-T4*F4 =E= 0; EBALEX1.. F3*(T3-T56) =E= 1620; EBALEX2.. F4*(T4-T78) =E= 360; FEAS1.. T3-430 =G= 10; FEAS2.. T56-349 =G= 10; FEAS3.. T4-368 =G= 10; FEAS4.. T78-320 =G= 10; AREA1.. Ah1c1*DELh1c1 =E= 1620; AREA2.. Ah1c2*DELh1c2 =E= 720; *Chen LMTD approximation DELTAC1.. DELh1c1=E=((T3-430)*(T56-349)*(1/2)*((T3-430)+(T56-349)))**0.333; DELTAC2.. DELh1c2=E=((T4-368)*(T78-320)*(1/2)*((T4-368)*(T78-320)))**0.333; MODEL COST /ALL/; SOLVE COST USING NLP MINIMIZING Z; DISPLAY Z.L, Ah1c1.L, Ah1c2.L, DELh1c1.L, DELh1c2.L, T3.L,T4.L, T56.L, T78.L; DISPLAY F1.L, F2.L, F3.L, F4.L, F5.L, F6.L, F7.L, F8.L;

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!* Define cold, hot and interval sets SETS HOT hot streams / H1, H2, S / COLD cold streams / C1, C2, W / INT interval / 1,2,3,4,5 /; TABLE U(HOT,COLD) upper bound on heat transfer between streams C1 C2 W H1 588.93 588.93 250.14 H2 762.00 747.84 250.14 S 0.00 127.68 0.00 ; * Define a table having more than 2 dimensions * Remember defaults are taken as 0.0!! TABLE QH(HOT,INT) Hot side heat transferred 1 2 3 4 5 S 127.68 H1 298.86 290.07 H2 938.95 232.10 ; TABLE QC(COLD,INT) Cold side heat transferred 1 2 3 4 5 C1 76.20 259.08 426.72 C2 127.68 541.12 206.72 W 125.07 125.07 ; VARIABLES Q(HOT,COLD,INT), R(HOT,INT), Y(HOT,COLD) Z minimum no of matches ; * Declare variables non-negative POSITIVE VARIABLES Q(HOT,COLD,INT), R(HOT,INT); * and those which are binary BINARY VARIABLES Y(HOT,COLD) EQUATIONS OBJ defines the objective function S, H2a, H2b, H2c, H2d, H1a, H1b, H1c CSIDE(COLD,INT), QMATCH(HOT,COLD); OBJ.. Z =E= SUM(HOT,SUM(COLD,Y(HOT,COLD))); S.. R("S","1")+Q("S","C2","1") =E= QH("S","1"); H2a.. R("H2","2")+Q("H2","C1","2")+Q("H2","C2","2") =E= QH("H2","2"); H2b.. R("H2","3")-R("H2","2")+Q("H2","C1","3")+Q("H2","C2","3") =E= QH("H2","3"); H2c.. R("H2","4")-R("H2","3")+Q("H2","C1","4")+Q("H2","W","4") =E= QH("H2","4"); H2d.. -R("H2","4")+Q("H2","W","5") =E= QH("H2","5"); H1a.. R("H1","3")+Q("H1","C1","3")+Q("H1","C2","3") =E= QH("H1","3"); H1b.. R("H1","4")-R("H1","3")+Q("H1","C1","4")+Q("H1","W","4") =E= QH("H1","4"); H1c.. -R("H1","4")+Q("H1","W","5") =E= QH("H1","5"); CSIDE(COLD,INT).. SUM(HOT,Q(HOT,COLD,INT)) =E= QC(COLD,INT); QMATCH(HOT,COLD).. SUM(INT,Q(HOT,COLD,INT)) =L= U(HOT,COLD)*Y(HOT,COLD); MODEL MATCH /ALL/; SOLVE MATCH USING MIP MINIMIZING Z; DISPLAY R.L,Q.L,Z.L !

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TABLE U(HOT,COLD) upper bound on heat transfer between streams

C1 C2 W H1 588.93 588.93 250.14 H2 762.00 747.84 250.14 S 0.00 127.68 0.00 ;!

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1 VARIABLES 2 Qcw, R1, R2, R3, R4, Z ; 3 4 EQUATIONS 5 OBJ,T1,T2,T3,T4,T5,B1,B2,B3,B4,B5,B6; 6 7 OBJ .. Z =E= Qs; **** $140 8 T1.. Qs-R1+30 =E= 0; 9 T2.. R1-R2+2.5 =E= 0; 10 T3.. R2-R3-82.5 =E= 0; 11 T4.. R3-R4+75 =E= 0; 12 T5.. R4-Qcw-15 =E= 0; 13 14 B1.. R1 =G= 0 15 B2.. R2 =G= 0; **** $409 16 B3.. R3 =G= 0; 17 B4.. R4 =G= 0; 18 B5.. Qs =G= 0; 19 B6.. Qcw =G= 0; 20 21 MODEL CASCADE /ALL/; 22 SOLVE CASCADE USING LP MINIMIZING Z; **** $257 140 Unknown symbol 257 Solve statement not checked because of previous errors 409 Unrecognizable item - skip to find a new statement looking for a ';' or a key word to get started again **** 3 ERROR(S) 0 WARNING(S)

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Page 1068: Product and Process Design Principles - Seider

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Page 1069: Product and Process Design Principles - Seider

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C O M P O N E N T L I S T ======================================================================================================================= : : : : : PURCHASED: :ORIGIN : ITEM TYPE : I T E M :--------------------- D E S I G N D A T A ----------------: EQUIPMENT: : : : D E S C R I P T I O N : : COST USD : ======================================================================================================================= Equipment mapped from 'D1'. TW - 10 TRAYED D1-tower Shell material A 515 64100 CODE OF ACCOUNT: 111 Number of trays 15 TAG NO.: D1-tower Vessel diameter 5.000 FEET Vessel tangent to tangent height 42.00 FEET Design temperature 310.80 DEG F Design gauge pressure 262.30 PSIG Application DISTIL Tray type SIEVE Tray spacing 24.00 INCHES Tray material A285C Tray thickness 0.188 INCHES Base material thickness 0.625 INCHES Total weight 31500 LBS I T E M :--- M A T E R I A L ---:********* M A N P O W E R *********:--- L/M ---: : FRACTION : FRACTION : RATIO : : USD OF PE : USD OF PE MANHOURS : USD/USD : EQUIPMENT&SETTING: 64100. 1.0000 : 1877. 0.0293 92 : 0.029 : PIPING : 20847. 0.3252 : 14937. 0.2330 651 : 0.716 : CIVIL : 1572. 0.0245 : 2153. 0.0336 127 : 1.370 : STRUCTURAL STEEL : 7021. 0.1095 : 3924. 0.0612 218 : 0.559 : INSTRUMENTATION : 36315. 0.5665 : 16719. 0.2608 729 : 0.460 : ELECTRICAL : 1678. 0.0262 : 909. 0.0142 45 : 0.542 : INSULATION : 10270. 0.1602 : 8250. 0.1287 423 : 0.803 : PAINT : 643. 0.0100 : 1376. 0.0215 88 : 2.141 : ------------------------------------------------------------------------- SUBTOTAL : 142445. 2.2222 : 50145. 0.7823 2373 : 0.352 : TOTAL MATERIAL AND MANPOWER COST =USD 192600. INST'L COST/PE RATIO = 3.005 ======================================================================================================================

$$

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