Page 33 - Process simulation and control using Aspen

26 PROCESS SIMULATION AND CONTROL USING ASPEN

TOTAL BALANCE
MOLE( LBMOL/HR) 220.462 220.462 0.000000E+00
MASS(LB/HR) 15906.4 15906.4 -0.782159E-11
ENTHALPY(BTU/HR) -0.165833E+08 -0.147349E+08-0.111463

ASPEN PLUS PLAT: WIN32 VER: 11.1 06/10/2007 PAGE 3
FLASH CALCULATIONS
PHYSICAL PROPERTIES SECTION

COMPONENTS
ID TYPE FORMULA NAME OR ALIAS REPORT NAME
C3H8 C C3H8 C3H8 C3H8
N-C4H10 C C4H10-1 C4H10-1 N-C4H10
N-C5H12 C C5H12-1 C5H12-1 N-C5H12
N-C6H14 C C6H14-1 C6H14-1 N-C6H14

ASPEN PLUS PLAT: WIN32 VER: 11.1 06/10/2007 PAGE 4
FLASH CALCULATIONS
U-O-S BLOCK SECTION

BLOCK: FLASH MODEL: FLASH2
INLET STREAM: F
OUTLET VAPOR STREAM: V
OUTLET LIQUID STREAM: L
PROPERTY OPTION SET: SYSOP0 IDEAL LIQUID / IDEAL GAS

***
MASS AND ENERGY BALANCE ***
IN OUT RELATIVE DIFF.
TOTAL BALANCE
MOLE(LBMOL/HR) 220.462 220.462 0 000000E+00
.
MASS(LB/HR) 15906.4 15906.4 -0 . 782136E-11
ENTHALPY(BTU/HR) -0.165833E+08 -0.147349E+08 -0.111463

INPUT DATA
TWO PHASE TP FLASH
SPECIFIED TEMPERATURE F 200.000
SPECIFIED PRESSURE PSI 100.000
MAXIMUM NO. ITERATIONS 30
CONVERGENCE TOLERANCE 0 000100000
.
*** RESULTS ***

OUTLET TEMPERATURE F 200.00