Page 34 - Process simulation and control using Aspen

INTRODUCTION AND STEPWISE ASPEN PLUS SIMULATION 27

OUTLET PRESSURE PSI 100.00
HEAT DUTY BTU/HR 0 . 18484E+07
VAPOR FRACTION 0 . 19274

V-L PHASE EQUILIBRIUM:
COMP F{I) X(I) Yd) K(I)
C3H8 0 . 10000 0 .52117E-01 0 .30055 5 .7668
N-C4H10 0 20000 0 16926 0 32874 1 9422
. . . .
N-C5H12 0 .30000 0 .31602 0 23290 0 .73697
.
N-C6H14 0 .40000 0 46260 0 .13781 0 .29790
.

ASPEN PLUS PLAT: WIN32 VER: 11.1 06/10/2007 PAGE 5
FLASH CALCULATIONS
STREAM SECTION
F L V
STREAM ID L V
FROM : FLASH FLASH
TO FLASH

SUBSTREAM: MIXED
PHASE: MIXED LIQUID VAPOR
COMPONENTS: LBMOL/HR
C3H8 22.0462 9 .2754 12.7709
N-C4H10 44 .0925 30.1237 13.9688
N-C5H12 66 .1387 56.2424 9 .8963
N-C6H14 88 .1849 82.3291 5 .8558
COMPONENTS: MOLE FRAC
C3H8 0.1000 5 .2117-02 0 .3005
N-C4H10 0 .2000 0 .1693 0 .3287
N-C5H12 0 .3000 0 .3160 0 .2329
N-C6H14 0 .4000 0 .4626 0 .1378
TOTAL FLOW:
LBMOL/HR 220.4623 177.9706 42.4917
LB/HR 1.5906+04 1 .3313+04 2593.7158
CUFT/HR 1839.5613 382.4385 3008.0650
STATE VARIABLES:
TEMP F 50.0000 200.0000 200.0000
PRES PSI 15.0000 100.0000 100.0000
VFRAC 1.8002-02 0 . 0 1 .0000
LFRAC 0.9820 1 .0000 0 .0
S FRAC 0.0 0 .0 0 .0