- Đường cong ASTM D
of Design Cũng như các trường hợp trên các specification đặt vào Pro/II đều ưu tiên đảm bảo cân bằng vật chất của các dịng trên cơ sở các thơng số hoạt động của tháp phải nằm trong giớ
cân bằng vật chất của các dịng trên cơ sở các thơng số hoạt động của tháp phải nằm trong giới hạn cho phép.
Tập tin input:
$ Generated by PRO/II Keyword Generation System <version 8.0> $ Generated on: Thu Jan 17 10:40:35 2008
TITLE PROJECT=DAU THAY THE, PROBLEM=DAU MIXED
PRINT STREAM=ALL, RATE=WT, FRACTION=WT, PERCENT=WT, TBP, KVT1=38, & KVT2=50
DIMENSION METRIC, PRES=KG/CMG, DUTY=KW, STDTEMP=0, STDPRES=0 OUTDIMENSION ADD, METRIC, PRES=KG/CMG, DUTY=KW, STDTEMP=0, & STDPRES=-2.20145E-8, PBASIS=1.03323
SEQUENCE SIMSCI
CALCULATION TRIALS=25, RVPBASIS=APIN, TVP=37.778, RECYCLE=ALL COMPONENT DATA
LIBID 1,H2/2,NH3/3,H2S/4,H2O/5,METHANE/6,ETHANE/7,PROPANE/ & 8,IBUTANE/9,BUTANE/10,22PR/11,IPENTANE/12,PENTANE/ & 13,CYPNTANE/14,22MB/15,23MB/16,2MP/17,3MP/18,HEXANE, & BANK=PROCESS,SIMSCI
CUTPOINTS TBPCUTS=95.6,158,1/200,1/1050,17/1450,4, BLEND=NGUYEN THERMODYNAMIC DATA
METHOD SYSTEM=GS, TRANSPORT=PETR, REFPROPS=SIMSCI, KVIS(LV)=SIMS, & CLOU(LV)=SIMS, POUR(LV)=INDEX, FLPO=NELS, SULF(WT)=SUM, & CETA=API, AROM(TOTA,LV)=SUM, NAPH(LV)=SUM, &
PARA(TOTAL,LV)=SUM, PARA(ISO,LV)=SUM, OLEF(MONO,LV)=SUM, & VANA(WT)=SUM, NICK(WT)=SUM, FRZP(LV)=INDEX, RON(C,LV)=SIMS, & MON(C,LV)=SIMS, SMOK(LV)=SUM, SET=GS01, DEFAULT
WATER DECANT=OFF
KVIS GAMMA=-3.5, REFINDEX=71.5, REFVALUE=1, NCFILL=SIMSCI, & NCBLEND=EXCL
CLOU GAMMA=0.05, REFINDEX=10000, REFVALUE=60, NCFILL=NOFILL, & NCBLEND=EXCL
POUR GAMMA=0.08, REFINDEX=10000, REFVALUE=60, NCFILL=API, & NCBLEND=EXCL
SULF(PCT) NCFILL=NOFILL, NCBLEND=MISS AROM(TOTA,PCT) NCFILL=NOFILL, NCBLEND=MISS NAPH(PCT) NCFILL=SIMSCI, NCBLEND=MISS PARA(TOTAL,PCT) NCFILL=SIMSCI, NCBLEND=MISS PARA(ISO,PCT) NCFILL=SIMSCI, NCBLEND=MISS OLEF(MONO,PCT) NCFILL=SIMSCI, NCBLEND=MISS VANA(PPM) NCFILL=NOFILL, NCBLEND=ZERO NICK(PPM) NCFILL=NOFILL, NCBLEND=ZERO
FRZP GAMMA=1, REFINDEX=10000, REFVALUE=60, NCFILL=NOFILL, & NCBLEND=EXCL
RON(C) GAMMA=0.05, REFINDEX=10000, REFVALUE=333.15, NCFILL=SIMSCI, & NCBLEND=MISS
MON(C) GAMMA=0.05, REFINDEX=10000, REFVALUE=333.15, NCFILL=SIMSCI, & NCBLEND=MISS
SMOK NCFILL=SIMSCI, NCBLEND=EXCL
METHOD SYSTEM=GS, TRANSPORT=PETR, REFPROPS=SIMSCI, KVIS(LV)=SIMS, & CLOU(LV)=SIMS, POUR(LV)=INDEX, FLPO(LV)=NELS, SULF(WT)=SUM, & CETA(WT)=API, AROM(TOTA,LV)=SUM, NAPH(LV)=SUM, &
PARA(TOTAL,LV)=SUM, PARA(ISO,LV)=SUM, OLEF(MONO,LV)=SUM, & VANA(WT)=SUM, NICK(WT)=SUM, FRZP(LV)=INDEX, RON(C,LV)=SIMS, & MON(C,LV)=SIMS, SET=GS02
KVIS GAMMA=-3.5, REFINDEX=71.5, REFVALUE=1, NCFILL=SIMSCI, & NCBLEND=EXCL
CLOU GAMMA=0.05, REFINDEX=10000, REFVALUE=60, NCFILL=NOFILL, & NCBLEND=EXCL
POUR GAMMA=0.08, REFINDEX=10000, REFVALUE=60, NCFILL=API, & NCBLEND=EXCL
FLPO NCFILL=NOFILL, NCBLEND=EXCL SULF(PCT) NCFILL=NOFILL, NCBLEND=MISS AROM(TOTA,PCT) NCFILL=NOFILL, NCBLEND=MISS NAPH(PCT) NCFILL=SIMSCI, NCBLEND=MISS PARA(TOTAL,PCT) NCFILL=SIMSCI, NCBLEND=MISS PARA(ISO,PCT) NCFILL=SIMSCI, NCBLEND=MISS OLEF(MONO,PCT) NCFILL=SIMSCI, NCBLEND=MISS VANA(PPM) NCFILL=NOFILL, NCBLEND=ZERO NICK(PPM) NCFILL=NOFILL, NCBLEND=ZERO
FRZP GAMMA=1, REFINDEX=10000, REFVALUE=60, NCFILL=NOFILL, & NCBLEND=EXCL
RON(C) GAMMA=0.05, REFINDEX=10000, REFVALUE=333.15, NCFILL=SIMSCI, & NCBLEND=MISS
MON(C) GAMMA=0.05, REFINDEX=10000, REFVALUE=333.15, NCFILL=SIMSCI, & NCBLEND=MISS
METHOD SYSTEM=SRK, SET=SRK01 STREAM DATA (adsbygoogle = window.adsbygoogle || []).push({});
PROPERTY STREAM=CRUDE-BH, TEMPERATURE=360, PRESSURE=2.45, PHASE=M, & RATE(WT)=690624, ASSAY=WT
TBP STREAM=CRUDE-BH, DATA=4.39,200/12.82,315/20.06,400/28.44,500/ & 38.65,600/50.76,700/63.34,800/76.18,900/85.92,1050, TEMP=F SPGR STREAM=CRUDE-BH, AVERAGE=0.82894, DATA=4.39,0.6816/ & 12.82,0.746/20.06,0.7734/28.44,0.7972/38.65,0.816/ & 50.76,0.8285/63.34,0.8437/76.18,0.8539/85.92,0.8904/ & 99.73,0.9313
LIGHTEND STREAM=CRUDE-BH, COMPOSITION(WT)=5,2E-6/6,3.1E-5/ & 7,0.000327/8,0.000488/9,0.002122/11,0.003741/12,0.00627/ & 13,0.0003/14,0.000243/15,0.00053/16,0.003885/17,0.002099/ & 18,0.008528, PERCENT(WT)=2.86, NORMALIZE
SULF STREAM=CRUDE-BH, AVERAGE(PCT)=0.03, DATA(PCT)=10.73,0.001/ & 15.04,0.0015/19.86,0.003/24.23,0.01/28.56,0.016/33.19,0.02/ & 38.3,0.022/43.88,0.025/49.87,0.028/55.98,0.031/62.15,0.033/ & 68.83,0.036/74.89,0.04/79.06,0.042/82.17,0.045/85.03,0.05/ & 93.22,0.09
WAX STREAM=CRUDE-BH, AVERAGE(PCT)=29.8
POUR STREAM=CRUDE-BH, AVERAGE=33, DATA=33.19,-10.556/38.3,-5.556/ & 43.88,5/49.87,10/55.98,35/62.15,41.667/68.83,50.444/ &
74.89,52.222/79.06,61/82.17,63/85.03,63.333 CARB STREAM=CRUDE-BH, AVERAGE(PCT)=85.31
H2 STREAM=CRUDE-BH, AVERAGE(PCT)=14.35 VANA STREAM=CRUDE-BH, AVERAGE(PPM)=0.02 NICK STREAM=CRUDE-BH, AVERAGE(PPM)=0.22 NITR(TOTA) STREAM=CRUDE-BH, AVERAGE(PCT)=0.04 CCR STREAM=CRUDE-BH, AVERAGE(PCT)=0.62 ASH STREAM=CRUDE-BH, AVERAGE(PCT)=0.015 ASPH(C7) STREAM=CRUDE-BH, AVERAGE(PCT)=0.15
FRZP STREAM=CRUDE-BH, DATA=10.73,-58/15.04,-56.944/19.86,-46.611/ & 24.23,-28.65/28.56,-19.189/33.19,-3.111/38.3,-1
CLOU STREAM=CRUDE-BH, DATA=15.04,-60/19.86,-51/24.23,-34/28.56,-24/ & 33.19,-6/38.3,-1.444/43.88,10.556/49.87,12.778
PROPERTY STREAM=STEAM1, TEMPERATURE=350, PRESSURE=2.4, PHASE=M, & RATE(WT)=16000, COMPOSITION(M)=4,1
PROPERTY STREAM=STEAM2, TEMPERATURE=350, PRESSURE=2.32, PHASE=M, & RATE(WT)=5069.99, COMPOSITION(M)=4,1
PROPERTY STREAM=STEAM3, TEMPERATURE=350, PRESSURE=2.31, PHASE=M, & RATE(WT)=2600, COMPOSITION(M)=4,1
PROPERTY STREAM=S8, TEMPERATURE=360, PRESSURE=2.45, PHASE=M, & COMPOSITION(WT,KG/H)=4,2010
PROPERTY STREAM=DUBAI, TEMPERATURE=360, PRESSURE=2.45, PHASE=M, & RATE(WT)=121875, ASSAY=LV
TBP STREAM=DUBAI, DATA=3.67,120.7/5,160/10,220/15,270/20,320/ & 25,380/30,430/35,500/40,550/45,600/50,650/55,700/60,750/ & 65,800/70,850/75,910/80,970/85,1050/90,1180/95,1400, TEMP=F SPGR STREAM=DUBAI, AVERAGE=0.869699, DATA=5,0.675/10,0.725/ & 15,0.75/20,0.77/25,0.79/30,0.81/35,0.83/40,0.845/45,0.865/ & 50,0.875/55,0.89/60,0.9/65,0.915/70,0.93/75,0.95/80,0.97/ & 85,0.995/90,1.02
LIGHTEND STREAM=DUBAI, COMPOSITION(LV)=6,0.0002/7,0.0028/ & 8,0.0023/9,0.0088/11,0.0087/12,0.0128/13,0.0011, & PERCENT(LV)=3.67, NORMALIZE
SULF STREAM=DUBAI, AVERAGE(PCT)=2.1, DATA(PCT)=15,0.0004/20,0.0012/ & 25,0.0024/30,0.0048/35,0.0092/40,0.0136/45,0.0184/50,0.0224/ & 55,0.0244/60,0.0252/65,0.0264/70,0.0276/75,0.0296/80,0.032/ & 85,0.0356/90,0.0392
MERC STREAM=DUBAI, AVERAGE(PPM)=100 UNIT OPERATIONS MIXER UID=M1 FEED CRUDE-BH,S8,DUBAI PRODUCT M=FEED COLUMN UID=T-1101 PARAMETER TRAY=26,IO FEED STEAM1,26/KER-V,8/LGO-V,15/HGO-V,21/FEED,25 PRODUCT OVHD(M)=TOPPING, LDRAW(WT)=KER1,9,68778, &
LDRAW(WT)=LGO1,16,216022, LDRAW(WT)=HGO1,22,87959.9, & BTMS(WT)=RES,407063, SUPERSEDE=OFF
DUTY 1,1,-0.0209,PAROHC1 DUTY 2,8,-0.009,PAROHC2
DUTY 3,15,-0.031,PAROHC3 DUTY 4,21,-0.004925,PAROHC4
PA NAME=PA1, FROM=2, TO=1, PHASE=L, DNAME=PAROHC1, TEMP=77 PA NAME=PA2, FROM=9, TO=8, PHASE=L, DNAME=PAROHC2, & RATE(WT)=211120
PA NAME=PA3, FROM=16, TO=15, PHASE=L, DNAME=PAROHC3, & RATE(WT)=758678
PA NAME=PA4, FROM=22, TO=21, PHASE=L, DNAME=PAROHC4, & RATE(WT)=134995
PSPEC PTOP=1.5, DPCOLUMN=0.4 PRINT PROPTABLE=BRIEF, SUMMARY=LV
ESTIMATE MODEL=REFINING, TTEMP=128, BTEMP=350 TEMPERATURE 1,128
SPEC(CHANGE) TRAY=1, TEMPERATURE(C), VALUE=124
SPEC ID=COL2SPEC5, STREAM=RES, RATE(WT,KG/H),TOTAL,WET, & VALUE=406250 VARY DNAME=PAROHC1 VARY DRAW=KER1,LGO1,HGO1 SIDESTRIPPER UID=SS1 PARAMETER TRAY=7,IO=15 FEED KER1,1
PRODUCT OVHD(M)=KER-V, BTMS(WT)=KEROSEN,51188, SUPERSEDE=ON DUTY 1,7,0.0028,REBOILER (adsbygoogle = window.adsbygoogle || []).push({});
PSPEC PTOP=1.6, DPCOLUMN=0.1 PRINT PROPTABLE=PART
ESTIMATE MODEL=SIMPLE
SPEC ID=SCOL1SPEC1, STREAM=KEROSEN, RATE(WT,KG/H),TOTAL,WET, & VALUE=51188
REBOILER TYPE=KETTLE SIDESTRIPPER UID=SS2 PARAMETER TRAY=2,IO FEED LGO1,1/STEAM2,2
PRODUCT OVHD(M)=LGO-V, BTMS(WT)=LGO,171880, SUPERSEDE=ON PSPEC PTOP=1.7, DPCOLUMN=0.1
PRINT PROPTABLE=PART ESTIMATE MODEL=SIMPLE
SPEC ID=SCOL2SPEC1, STREAM=LGO, RATE(WT,KG/H),TOTAL,WET, & VALUE=171440
SIDESTRIPPER UID=SS3 PARAMETER TRAY=2,IO=15 FEED HGO1,1/STEAM3,2
PRODUCT OVHD(M)=HGO-V, BTMS(WT)=HGO,69874.9, SUPERSEDE=ON PSPEC PTOP=1.9, DPCOLUMN=0.1
PRINT PROPTABLE=PART ESTIMATE MODEL=SIMPLE
SPEC ID=SCOL3SPEC1, STREAM=HGO, RATE(WT,KG/H),TOTAL,WET, & VALUE=69062
CALCULATOR UID=CA2 RESULT 1,OVERFLASH
WET, DIVIDE, STREAM=FEED, RATE(LV,M3/H),TOTAL,WET PROCEDURE
R(1)=P(1) RETURN HX UID=E-1111
HOT FEED=TOPPING, M=S4, DP=0.2, METH=GS01 OPER HTEMP=50
FLASH UID=D-1103 FEED S4
PRODUCT L=C10-, W=WATER1, V=GAS_MAINCOL ISO TEMPERATURE=50, PRESSURE=1.3 METHOD SET=GS02 PUMP UID=P1110 FEED C10- PRODUCT M=S6 OPERATION PRESSURE=13.1 METHOD SET=GS02 HX UID=E-1113
COLD FEED=S6, M=VAOVAN, DP=0.2, METH=GS02 OPER CTEMP=145 VALVE UID=V1 FEED VAOVAN PRODUCT M=STA_FEED OPERATION PRESSURE=10.25 METHOD SET=GS02 COLUMN UID=T3 PARAMETER TRAY=26,IO FEED STA_FEED,11
PRODUCT LDRAW(WT)=LPG,1,2181, WATER(M)=NUOC,1, &
OVHD(WT)=OFFGAS_STA, BTMS(WT)=NAPHTA_FULL,108000 CONDENSER TYPE=MIX
DUTY 1,1,,CONDENSER DUTY 2,26,,REBOILER
PSPEC PTOP=7.9, DPCOLUMN=0.25 PRINT PROPTABLE=PART
ESTIMATE MODEL=CONVENTIONAL, RRATIO=3
SPEC ID=COL2SPEC1, STREAM=OFFGAS_STA, RATE(WT,KG/H),TOTAL,WET, & VALUE=1
SPEC ID=COL2SPEC4, RRATIO(WT), VALUE=3 VARY DNAME=CONDENSER,REBOILER
REBOILER TYPE=KETTLE METHOD SET=GS02 CALCULATOR UID=CA1
RESULT 1,GAP KERO - FULLRANGE NAPHTHA/2,GAP LGO-HGO/ & 3,OVERLAP HGO-LGO
DEFINE P(1) AS STREAM=LGO, D86(5,C), MINUS, STREAM=KEROSEN, & D86(95,C)
DEFINE P(2) AS STREAM=KEROSEN, D86(5,C), MINUS, & STREAM=NAPHTA_FULL, D86(95,C)
D86(5,C) PROCEDURE R(1)=P(2) R(2)=P(1) R(3)=P(3) RETURN VALVE UID=V2 FEED NAPHTA_FULL PRODUCT M=S3 OPERATION PRESSURE=2 HX UID=E1 HOT FEED=S3, M=S7 OPER HTEMP=122 COLUMN UID=T4 PARAMETER TRAY=33,IO FEED S7,21 (adsbygoogle = window.adsbygoogle || []).push({});
PRODUCT OVHD(WT)=LIGH_NAPHTA,22809, BTMS(WT)=H_NAPHTA,79999.9 CONDENSER TYPE=BUBB
DUTY 1,1,,CONDENSER DUTY 2,33,0.05,REBOILER PSPEC PTOP=1.1, DPCOLUMN=0.6 PRINT PROPTABLE=PART
ESTIMATE MODEL=CONVENTIONAL, RRATIO=3
SPEC ID=COL4SPEC1, STREAM=LIGH_NAPHTA, RATE(WT,KG/H),TOTAL,WET, & VALUE=22809
SPEC ID=COL4SPEC2, RRATIO(WT), VALUE=1.7 VARY DNAME=CONDENSER,REBOILER
REBOILER TYPE=KETTLE METHOD SET=GS01 END