Power Plant Performance Calculation

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JSWEL Unit No- Test Date: Sl no Description Units Start time Aft 20 mins Aft 40 mins 1 Generator Active Power MW 2 First stage pressure 3 Throttle Pressure 4 MS Temperature @ HDR Bef HPESV 5 HP Exhaust Pressure 6 HP Exhaust Temperature Bef CRH NRV 7 HRH Steam Pressure To IPSV1 8 HRH Temperature @ HDR Bef IPESV 9 Steam Press @ Inlet To LP Turbine 10 LP Turbine Exhaust Temperature 11 Condenser Pressure 12 Cond.Temperature @ Hotwell 13 Condensate flow (sel) 14 Cond Pressure @ Lph-1 Inlet 15 Cond Temp. @ Gsc Outlet 16 LPH-1 Shell Pressure 17 LPH-1 Drain Temperature 18 LPH-2 Shell Pressure 19 LPH-2 Drain Temperature 20 Condensate Temperature @ LPH-2 Outle 21 Condensate pressure at LPH-2 Outlet 22 Condensate pressure at LPH-3 Outlet 23 ECO O/L Temperature 24 LP Extr A3 Pressure Bef Nrv 25 LP Extr A3 Temperature Bef Nrv 26 LPH-3 Drain Temperature 27 Condensate Temperature @ Dearator In 28 Extr A4 Pressure 29 Extr A4 Temperature 30 Fw Flow @ HPH-6 Outlet TPH 31 Fw Pressure @ BFP Disch Hdr 32 Fw Temperature @ BFP Disch Hdr 33 Extr A5 Pressure 34 Extr A5 Temperature 35 HPH-5 Drain Temperature 36 FW Temperature @ HPH-5 Outlet 37 FW Pressure @ HPH-6 Outlet 38 FW Temperature @ HPH-6 Outlet 39 HPH-6 Shell Pressure 40 CRH Temperature @ HPH -6 Inlet Kg/cm 2 Kg/cm 2 0 C Kg/cm 2 0 C Kg/cm 2 0 C Kg/cm 2 0 C Kg/cm 2 0 C T/hr Kg/cm 2 0 C Kg/cm 2 0 C Kg/cm 2 0 C 0 C Kg/cm 2 Kg/cm 2 0 C Kg/cm 2 0 C 0 C 0 C Kg/cm 2 0 C Kg/cm 2 0 C Kg/cm 2 0 C 0 C 0 C Kg/cm 2 0 C Kg/cm 2 0 C

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Power Plant Performance Calculation

Transcript of Power Plant Performance Calculation

Data Survey sheet 1 of 39JSWEL Unit No- Test Date: Test start timeSl noDescription Units Start time Aft 20 mins Aft 40 mins Aft 60 mins1 Generator Active Power MW2 First stage pressure3 Throtte Pressure! MS Te"perature # $D% &ef $P'S() $P '*haust Pressure+ $P '*haust Te"perature &ef ,%$ -%(. $%$ Stea" Pressure To /PS(10 $%$ Te"perature # $D% &ef /P'S(9 Stea" Press # /net To 1P Tur2ine13 1P Tur2ine '*haust Te"perature11 ,on4enser Pressure12 ,on45Te"perature # $otwe13 ,on4ensate fow 6se71! ,on4 Pressure # 1ph81 /net1) ,on4 Te"p5 # Gsc 9utet1+ 1P$81 She Pressure1. 1P$81 Drain Te"perature10 1P$82 She Pressure19 1P$82 Drain Te"perature23 ,on4ensate Te"perature # 1P$82 9utet21 ,on4ensate pressure at 1P$82 9utet22 ,on4ensate pressure at 1P$83 9utet23 ',9 9:1 Te"perature 2! 1P '*tr A3 Pressure &ef -rv2) 1P '*tr A3 Te"perature &ef -rv2+ 1P$83 Drain Te"perature2. ,on4ensate Te"perature # Dearator /net20 '*tr A! Pressure29 '*tr A! Te"perature33 Fw Fow # $P$8+ 9utetTP$31 Fw Pressure # &FP Disch $4r 32 Fw Te"perature # &FP Disch $4r33 '*tr A) Pressure3! '*tr A) Te"perature3) $P$8) Drain Te"perature3+ FW Te"perature # $P$8) 9utet3. FW Pressure # $P$8+ 9utet30 FW Te"perature # $P$8+ 9utet39 $P$8+ She Pressure!3 ,%$ Te"perature # $P$ 8+ /net;g:c"2;g:c"23 ,;g:c"23 ,;g:c"23 ,;g:c"23 ,;g:c"23 ,T:hr;g:c"23 ,;g:c"23 ,;g:c"23 ,3 ,;g:c"2;g:c"23 ,;g:c"23 ,3 ,3 ,;g:c"23 ,;g:c"23 ,;g:c"23 ,3 ,3 ,;g:c"23 ,;g:c"23 ,Data Survey sheet 2 of 39JSWEL Unit No- Test Date: Test start timeSl noDescription Units Start time Aft 20 mins Aft 40 mins Aft 60 mins!1 $P$8+ Drain Te"perature!2 ,W Te"p # ,on4enser /net $4r!3 ,W Te"p # ,on4enser 9utet $4r!! Tota Stea" fow TP$!) AP%DS Fow TP$!+ %$ spray .3 A"2ient te"p84ry 2u23 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,3 ,Data Survey sheet 3 of 39JSWEL Unit No- Test Date: Test start timeSl noDescription Units Start time Aft 20 mins Aft 40 mins Aft 60 mins.1 A"2ient te"p8wet 2u23 ,TU!"#NE $EAT !ATE CALCULAT#%NDAT' 8P1A-T STAT?S 8STE& N%' &A!A(ETE! UN#T1 F''D WAT'% F19W6D'-S/T@ AS P'% DATA S$''T7 TP$ 30.53!32 D'-S/T@ 9F F''D WAT'% AT F19W '1'M'-T 02)5303 D'-S/T@ ,9%%',T/9- FA,T9% 8 1! ,9%%',T'D F''D WAT'% F19W TP$ 30.53!3) S@ST'M 1'A;AG'S TP$ 3+ %$ SP%A@ A?A-T/T@ TP$ 3. AP%DS F19W TP$ 30 MA/- ST'AM F19W T$%9?G$ T?%&/-' TP$ 30.53!39 $P T?%&/-' F/%ST STAG' P%'SS?%' ATA 123533313 /P T?%&/-' /-1'T P%'SS?%' ATA 315.011 D'-S/T@ 9F ST'AM AT F/%ST STAG' 353293)12 /-T'%M'D/AT' G1A-D 1'A;AG'TP$ 95).!!13 $P T?%&/-' 'B$A?ST P%'SS?%' ATA 3)5311! D'-S/T@ 9F ST'AM AT $P T?%&/-' 'B$A?ST 353.0!1) $P T?%&/-' 'B$A?ST G1A-D 1'A;AG'TP$ 05022.1+ 'B%A,T/9- ST'AM F19W T$%9?G$ $P $'AT'% 8+ TP$ 395))31. ST'AM F19W T$%9?G$ %'$'AT'%TP$ 329539+10 $'AT %AT';,A1:;W$% 19.)5.)19 ,9%%',T/9- FA,T9% F9% $'AT %AT' 8 15333323 ,9%%',T'D $'AT %AT' ;,A1:;W$% 19.)5.)21 ?-/T $'AT %AT';,A1:;W$% 222!5+922 D'S/G-'D $'AT %AT' ;,A1:;W$% 210353223 D/FF'%'-,' /- $'AT %AT' ;,A1:;W$% !!5+.AT 133> 19AD C 3> MA;' ?P;G:M3;G:M3;G:M3Data Survey sheet ) of 39JSWEL Unit No- ) Test Date:Test Time:Sl noDescription Units1 Generator Active Power MW2 First stage pressure3 Throtte Pressure! MS Te"perature # $D% &ef $P'S() $P '*haust Pressure+ $P '*haust Te"perature &ef ,%$ -%(. $%$ Stea" Pressure To /PS(10 $%$ Te"perature # $D% &ef /P'S(9 Stea" Press # /net To 1P Tur2ine13 1P Tur2ine '*haust Te"perature11 ,on4enser Pressure12 ,on45Te"perature # $otwe13 ,on4ensate fow 6se71! GS hea4er pressure1) GS hea4er te"p1+ GS, 4rain te"p1. ,on4ensate pressure at GS, inet10 ,on4 Pressure # 1ph81 /net19 ,on4 Te"p5 # Gsc 9utet23 1P$81 She Pressure21 1P$81 Drain Te"perature22 1P$82 She Pressure23 1P$82 Drain Te"perature2! ,on4ensate Te"perature # 1P$82 9utet2) ,on4ensate pressure at 1P$82 9utet2+ ,on4ensate pressure at 1P$83 9utet2. ',9 9:1 Te"perature 20 1P '*tr A3 Pressure &ef -rv29 1P '*tr A3 Te"perature &ef -rv33 1P$83 Drain Te"perature31 ,on4ensate Te"perature # Dearator /net32 '*tr A! Pressure33 '*tr A! Te"perature3! Fw Fow # $P$8+ 9utetTP$3) Fw Pressure # &FP Disch $4r 3+ Fw Te"perature # &FP Disch $4r;g:c"2;g:c"23 ,;g:c"23 ,;g:c"23 ,;g:c"23 ,;g:c"23 ,T:hr""wc3 ,3 ,;g:c"2;g:c"23 ,;g:c"23 ,;g:c"23 ,3 ,;g:c"2;g:c"23 ,;g:c"23 ,3 ,3 ,;g:c"23 ,;g:c"23 ,Data Survey sheet + of 39JSWEL Unit No- ) Test Date:Test Time:Sl noDescription Units3. '*tr A) Pressure30 '*tr A) Te"perature39 $P$8) Drain Te"perature!3 FW Te"perature # $P$8) 9utet!1 FW Pressure # $P$8+ 9utet!2 FW Te"perature # $P$8+ 9utet!3 $P$8+ She Pressure!! ,%$ Te"perature # $P$ 8+ /net!) $P$8+ Drain Te"perature!+ ,W Te"p # ,on4enser /net $4r!. ,W Te"p # ,on4enser 9utet $4r!0 Tota Stea" fow TP$!9 AP%DS Fow TP$)3 %$ spray +) car2on >++ -itrogen >+. 9*ygen >+0 Moisture in coa >+9 Ash in coa >.3 Suphur in coa >.1 ,oa caorific vaue 6G,(7 =ca:=g.2 un2urnt in fy ash >.3 un2urnt in &otto" ash >.! A"2ient te"p84ry 2u2.) A"2ient te"p8wet 2u23 ,3 ,Test S*mmarJSWEL Unit No- ) Test +*ration-4 $!STest Date: 2,'0)'0-Test Time: -:00 A($P ,yin4er 'fficiency> 'rrD)11/P ,yin4er 'fficiency > 'rrD)111P ,yin4er 'fficiency > 'rrD)11(acuu" 'fficiency > 'rrD)119vera 'fficiency of Tur2ine > 'rrD)11TG $eat rate correcte4 ;ca:;Wh 'rrD)11?nit $eat rate 2y Direct Metho4 ;ca:;Wh 23.150?nit $eat rate 2y cacuation ;ca:;Wh 'rrD)11Air ea=age into con4enser ;g:hr 051&oier 'fficiency > 'rrD)11AP$8A 1ea=age > 125+AP$8& 1ea=age > 2352'fficiency of $P$8+ > 9)59'fficiency of $P$8) > .352'*traction stea" Fow to $P$8+ T:hr 'rrD)11'*traction stea" Fow to $P$8) T:hr 'rrD)11'*traction stea" Fow to Deaerator T:hr 'rrD)11'*traction stea" Fow to 1P$83 T:hr 'rrD)11'*traction stea" Fow to 1P$81C2 T:hr 'rrD)11TTD$P$8+ 'rrD)11D,A $P$8+ 351TTD $P$8) 'rrD)11D,A $P$8) 25!TTD 1P$83 'rrD)11D,A 1P$83 !5.TTD 1P$82 'rrD)11D,A 1P$81 )50oCoCoCoCoCoCoCoCTG $'AT %AT'Page 9 of 39JSWEL Unit No- 1 8:00 AMTest Date: 29.01.08SL.NO PARAMETER UNIT kcalk!"1 #$ t%&'ine (l )&* +SC 12,.,82 #$ t%&'ine (l te-). ./9.08/ 1i&st sta2e )&. +SC 119..03 C4# )&. At T%&'ine e5"a%st +SC /..33. C4# te-). At T%&'ine e5"a%st /,1.98, #4# )&. at ($ t%&'ine (l +SC /2.380 #4# te-). at ($ t%&'ine (l .30.908 #4# )&. 6e7o&e inte&ce)t 8l8 +SC /2.389 ($ T%&'ine ol $&. 9Dea. E5t.: +SC ..2910 ($ T%&'ine ol Te-). 9Dea. E5t.: /03./011 L$ e5"a%st )&. +SC -0.89 13.3312 E5t&n. Stea- )&. At #$#-, +SC /3.,11/ E5t&n. Stea- te-). At #$#-, /.9..,13 #$# -, ;&ain te-). 18...,1. 1W te-). 'e7o&e #$#-, 182.321, 1W te-). a7te& #$#-, 2/2.2010 1W )&. at 7lo! ele-ent +SC 139..918 1W 7lo!- D$ t)" 300.30 -0.91.819 A$4DS 1L,o"2usti2es in 2otto" ash ;g:;g of coaTota co"2usti2es? ;g:;g of coa,v ofcar2on ;E:;g?n2urnt car2on oss ;E:;g2'$eat loss +*e to +r fl*e 0as,ar2on 2urnt per ;g of fue ;g:;g >>,9 at A$ outet ,9 pp" >>Wt of 4ry gases ;g:;g of coaA$ gas outet te"pcar2on to hy4rogen ration c:hA$ sec air inet te"p A$ pri"ary air inet te"pSec air fow T:hrPri air fow T:hr%eference air te"p ,fDf?f,&D"?&,(,1?,,292 at A$ outet 92,92 at A$ outet ,92-2 at A$ outet -2WGFtG3,/nstantaneous sp heat ot fue gas at tG 3, 6fig . of ASM' PT, !517 ;E:;g3,tSA3,TPA3,ASAAPAt%A3,/nstantaneous Sp heat of fue gas at t%A 3,6fro" fig . of ASM' PT, !517 ;E:;g3,Mean Sp5 $eat of 4ry fue gas$eat lost +*e to +r fl*e 0as;E:;g;E:;g$eat ost 4ue to fue "oisture ;E:;g4'$eat lost +*e to /*rnin0 of 1+ro0en$eat ost 4ue to 2urning of hy4rogen ;E:;g2'$eat lost +*e to moist*re in air;E:;gA"2ient te"p84ry 2u2A"2ient te"p8wet 2u2;g:;g of airWt of -itrogen in 4ry gas ;g:;g of coaWt of 4ry air ;g:;g of coa$eat ost 4ue to "oisture in air =G:=gTe"p of 2otto" ash a2ove a"2ientSp5 $eat of 2otto" ash ;E:;g$eat ost 4ue sensi2e heat of 2otto" ash ;E:;gTe"p of fy ash Sp5heat of fy ash ;E:;g$eat ost 4ue to sensi2e heat of fy ash ;E:;g,PGF;E:;g3,1GF;E:;g3,3'$eat lost +*e to f*el moist*re 5 Partia pr H1psi6a7H353.33;g:c"2'nthapy of vapour at partia pr an4 te"p tGhtG'nthapy of saturate4 i;E:;g,oa fow T:hr;w;w;g ;w8hr:;g$eat cre4it & ;E:;gE..#C#ENC7 8Test con+ition9,o"2usti2es heat oss ;E:;g$eat ost 4ue to heat in 4ry fue gas ;E:;g$eat ost 4ue "oisture in as fire4 fue ;E:;g;E:;g$eat ost 4ue to "oisture in air ;E:;g;E:;g$eat ost 4ue to sensi2e heat in fy ash ;E:;g;E:;g$eat cre4it & ;E:;gTota heat oss 1 ;E:;g'fficiency >$eat lost in percenta0e?n2urnt car2on oss >$eat ost 4ue to heat in 4ry fue gas >$eat ost 4ue to "oisture in as fire4 fue >>$eat ost 4ue to "oisture in air >>$eat ost 4ue to sensi2e heat of fy ash >>$eat cre4it >Tota heat oss >$eat ost 4ue surface ra4iation C convection 6as per pri4ection71,'$eat cre+itsMi powerP"i;w8hr:;g of fue ;w;gHPoct":,fo:13331?,1GF1"f$eat ost 4ue to "oisture fro" 2urning to hy4rogen1$1"A $eat ost 4ue to sensi2e heat of 2otto" ash12ash1fash$eat ost 4ue to surface %a4iation C con4uction1't$eat ost 4ue to "oisture fro" 2urning to hy4rogen$eat ost 4ue to sensi2e heat of 2otto" ash$eat ost 4ue to surface %a4iation C con4uctionEfficienc8Test con+ition9 >!ea+in0s135.1935333532135!313533353335322)+2051+!+!53+35+3)5)0125133533353302533125)012)521125+1153132.5)13.5333305+313)593295.035991533123!5)0'rrD)11'rrD)11'rrD)11'rrD)11'rrD)112)533235+3353395+3125!.Err:2))13)3533153))2',212!533350!-'32352!+15)1)3503!)35333533093150.E..#C#ENC7 8Test con+ition9!+!53+123!5)0'rrD)11'rrD)11'rrD)1112592053)+15)13150.Err:2))Err:2)):J;:< DES#1Fue input ,oa fow tph )3503 234)'46 2)44'00,ore* fow =n"3:hr 3,oa G,( =ca:=g +12253),ore* ,( =ca:n"3FW FW Fow tph !335!3FW te"p at 'co i: 232523FW pr at 'co i: ksc 1!95)9'nthapy of FW at eco i: =G:=g 'rrD)11 Err:2)) 432',-%$ $%$ Fow 'rrD)11'nthapy of $%$ stea" at /PT /:1 'rrD)11 Err:2)) 2)4)')2'nthapy of ,%$ stea" AT $PT 9:1 'rrD)11 Err:2)) )-44'62MS 1ine osses Err:2)) )'2%$ 1ine osses Err:2)) )'2Tota &oier heat input 234)'46 2)44'00"oiler losses DES#E?traction steam flo> to Deaerator,on4ensate fow through 1P$83 3!259! T:hr'nthapy of con4ensate at Deaerator inet 'rrD)11 ;E:=g'*tn A! pressure +23539+) ;pa6a7Deaerator water te"p 1))52'*tn A! te"p 33!533'nthapy of fee4 water at Deaerator outet 'rrD)11 ;E:=g'*traction stea" fow to $P $eater8+ 'rrD)11 T:hr'*traction stea" fow to $P $eater8) 'rrD)11 T:hr'nthapy of $P$8) 4rain 'rrD)11 ;E:=g'nthapy of stea" to 4eaerator 'rrD)11 ;E:=g'*tn fow to Deaerator Err:2)) T:hrSaturation te"p of stea" at operating pressure 'rrD)11TTD of Deaerator Err:2))E?traction steam flo> to