BLOCK: B2 MODEL: FLASH3
------------------------------
INLET STREAM: 6
OUTLET VAPOR STREAM: 7
FIRST LIQUID OUTLET: 9
SECOND LIQUID OUTLET: 8
PROPERTY OPTION SET: PENG-ROB STANDARD PR EQUATION OF STATE

*** MASS AND ENERGY BALANCE ***
IN OUT RELATIVE DIFF.
TOTAL BALANCE
MOLE(KMOL/SEC) 0.277778E-01 0.277778E-01 0.00000
MASS(KG/SEC ) 1.11045 1.11045 -0.399919E-15
ENTHALPY(WATT ) -0.518597E+07 -0.518597E+07 -0.102879E-06

*** CO2 EQUIVALENT SUMMARY ***
FEED STREAMS CO2E 1.11408 KG/SEC
PRODUCT STREAMS CO2E 1.11408 KG/SEC
NET STREAMS CO2E PRODUCTION 0.00000 KG/SEC
UTILITIES CO2E PRODUCTION 0.00000 KG/SEC
TOTAL CO2E PRODUCTION 0.00000 KG/SEC

*** INPUT DATA ***
THREE PHASE PQ FLASH
SPECIFIED PRESSURE N/SQM 100,000.
SPECIFIED HEAT DUTY WATT 0.0
MAXIMUM NO. ITERATIONS 30
CONVERGENCE TOLERANCE 0.000100000
NO KEY COMPONENT IS SPECIFIED
KEY LIQUID STREAM: 8

*** RESULTS ***
OUTLET TEMPERATURE K 306.50
OUTLET PRESSURE N/SQM 0.10000E+06
VAPOR FRACTION 0.62722
1ST LIQUID/TOTAL LIQUID 1.0000

V-L1-L2 PHASE EQUILIBRIUM :

COMP F(I) X1(I) X2(I) Y(I) K1(I) K2(I)
METHANE 0.100 0.190E-06 0.190E-06 0.159 0.840E+06 187.
ETHANE 0.300E-01 0.603E-07 0.603E-07 0.478E-01 0.793E+06 34.6
PROPANE 0.400E-01 0.996E-08 0.996E-08 0.638E-01 0.640E+07 11.6
BUTANE 0.800E-01 0.216E-08 0.216E-08 0.128 0.590E+08 3.33
PENTAN 0.250 0.320E-09 0.320E-09 0.399 0.125E+10 0.922
WATER 0.400 1.00 1.00 0.434E-01 0.434E-01 2.03
N-BUTANE 0.100 0.270E-08 0.270E-08 0.159 0.590E+08 3.33