Bilaga 5 input data till uppgift 3
COMPONENTS
C1 CH4 C1 /
C2 C2H6 C2 /
C3 C3H8 C3 /
I-C4 C4H10-2 I-C4 /
N-C4 C4H10-1 N-C4 /
I-C5 C5H12-2 I-C5 /
N-C5 C5H12-1 N-C5
FLOWSHEET
BLOCK FEEDVVX IN=7 OUT=DESTFEED
BLOCK PUMP IN=FEED OUT=7
BLOCK KOLONN IN=DESTFEED OUT=DEST BOTTEN
BLOCK BOTVVX IN=BOTTEN OUT=8
PROPERTIES RK-SOAVE
PROP-REPLACE IDEAL SYSOP0A
PROP-REPLACE STEAM-TA SYSOP12
PROP-REPLACE RK-SOAVE SYSOP3
PROP VLMX VLMX20 / MULMX MULMX03 / SIGLMX SIGLMX02 / &
MUVMX MUVMX01 / KVMX KVMX01
MODEL-PARAME ESRKS
STREAM FEED
SUBSTREAM MIXED TEMP=35 PRES=12.8 MOLE-FLOW=431
MOLE-FRAC C1 0.01 / C2 0.09 / C3 0.306 / I-C4 0.151 / &
N-C4 0.417 / I-C5 0.022 / N-C5 0.004
BLOCK BOTVVX HEATER
PARAM TEMP=18 PRES=0
BLOCK FEEDVVX HEATER
PARAM PRES=18 DUTY=550000
BLOCK KOLONN RADFRAC
PARAM NSTAGE=14
FEEDS DESTFEED 9 ON-STAGE
PRODUCTS DEST 1 L / BOTTEN 14 L
P-SPEC 1 16.7
COL-SPECS D:F=0.36 DP-COL=1.3 MOLE-RDV=0 MOLE-RR=1.976
BLOCK PUMP PUMP
PARAM PRES=18
DESIGN-SPEC BOT
DEFINE XC1 BLOCK-VAR BLOCK=KOLONN VARIABLE=X SENTENCE=COMPS &
ID1=C1 ID2=14
DEFINE XC2 BLOCK-VAR BLOCK=KOLONN VARIABLE=X SENTENCE=COMPS &
ID1=C2 ID2=14
DEFINE XC3 BLOCK-VAR BLOCK=KOLONN VARIABLE=X SENTENCE=COMPS &
ID1=C3 ID2=14
SPEC "XC1+XC2+XC3" TO "0.1"
TOL-SPEC "0.001"
VARY BLOCK-VAR BLOCK=KOLONN VARIABLE=MOLE-RR &
SENTENCE=COL-SPECS
LIMITS "1" "10"
DESIGN-SPEC DES
DEFINE XC1 MASS-FRAC STREAM=BOTTEN SUBSTREAM=MIXED &
COMPONENT=C1
DEFINE XC2 MOLE-FRAC STREAM=BOTTEN SUBSTREAM=MIXED &
COMPONENT=C2
DEFINE XC3 MOLE-FRAC STREAM=BOTTEN SUBSTREAM=MIXED &
COMPONENT=C3
DEFINE XC4I MOLE-FRAC STREAM=DEST SUBSTREAM=MIXED &
COMPONENT=I-C4
DEFINE XC4N MOLE-FRAC STREAM=DEST SUBSTREAM=MIXED &
COMPONENT=N-C4
DEFINE XC5I MOLE-FRAC STREAM=DEST SUBSTREAM=MIXED &
COMPONENT=I-C5
DEFINE XC5N MOLE-FRAC STREAM=DEST SUBSTREAM=MIXED &
COMPONENT=N-C5
SPEC "XC4I+XC4N+XC5I+XC5N" TO "0.05"
TOL-SPEC "0.001"
VARY BLOCK-VAR BLOCK=KOLONN VARIABLE=MOLE-FLOW &
SENTENCE=PRODUCTS ID1=BOTTEN
LIMITS "1" "300"
STREAM-REPOR MOLEFLOW MOLEFRAC