Calgary, Alberta CANADA
Case Name: C:\Users\user\Downloads\CO2 Absorber.usc Unit Set: NewUser4
Date/Time: Thursday Feb 27 2025, 10:03:29
Material Stream: Bottom A-101-E
Fluid Package: Basis-1Property Package: General NRTL - Ideal
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (kgmole/h)
Mass Flow (kg/h)
Std Ideal Liq Vol Flow (m3/h) Molar Enthalpy (kJ/kgmole) Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall 0.0000
58.56 32.10 2.255e+004 6.140e+005 606.4 -2.996e+005 45.08 -6.758e+009 615.9
Aqueous Phase 1.0000
58.56 32.10 2.255e+004 6.140e+005 606.4 -2.996e+005 45.08 -6.758e+009 615.9
Liquid Phase 0.0000
58.56 32.10 2.255e-004 6.137e-003 6.058e-006 -2.996e+005 44.82 -67.56 6.156e-006
PROPERTIES
Overall Aqueous Phase Liquid Phase
COMPOSITION
Overall Phase
Vapour Fraction 0.0000 COMPONENTSHydrogen Nitrogen Methane Argon CO CO2 Oxygen Ethane Propane i-Butane n-Butane MDEAmine H2O
MOLAR FLOW (kgmole/h)
8.5224 13.440 0.12279 5.1719e-002 0.52228 69.051 0.00000 0.00000 0.00000 0.00000 0.00000 2036.1 20425
MOLE FRACTION 0.000378 0.000596 0.000005 0.000002 0.000023 0.003062 0.000000 0.000000 0.000000 0.000000 0.000000 0.090280 0.905654
MASS FLOW (kg/h)
17.181 376.48 1.9698 2.0661 14.629 3038.9 0.00000 0.00000 0.00000 0.00000 0.00000 2.4262e+005 3.6796e+005
MASS FRACTION 0.000028 0.000613 0.000003 0.000003 0.000024 0.004949 0.000000 0.000000 0.000000 0.000000 0.000000 0.395124 0.599255
LIQUID VOLUME FLOW (m3/h)
0.24594 0.46688 6.5794e-003 1.5079e-003 1.8301e-002 3.6820 0.00000 0.00000 0.00000 0.00000 0.00000 233.29 368.71
LIQUID VOLUME FRACTION
0.000406 0.000770 0.000011 0.000002 0.000030 0.006072 0.000000 0.000000 0.000000 0.000000 0.000000 0.384700 0.608009
Total 22553 1.0000 6.1403e+005 1.0000 606.41 1.0000
Aqueous Phase
Phase Fraction 1.000COMPONENTS Hydrogen Nitrogen Methane Argon CO CO2 Oxygen Ethane Propane i-Butane n-Butane MDEAmine H2O
MOLAR FLOW (kgmole/h)
8.5224 13.440 0.12279 5.1719e-002 0.52228 69.051 0.00000 0.00000 0.00000 0.00000 0.00000 2036.1 20425
MOLE FRACTION 0.000378 0.000596 0.000005 0.000002 0.000023 0.003062 0.000000 0.000000 0.000000 0.000000 0.000000 0.090280 0.905654
MASS FLOW (kg/h)
17.181 376.48 1.9698 2.0661 14.629 3038.9 0.00000 0.00000 0.00000 0.00000 0.00000 2.4262e+005 3.6796e+005
MASS FRACTION 0.000028 0.000613 0.000003 0.000003 0.000024 0.004949 0.000000 0.000000 0.000000 0.000000 0.000000 0.395124 0.599255
LIQUID VOLUME FLOW (m3/h)
0.24594 0.46688 6.5794e-003 1.5079e-003 1.8301e-002 3.6820 0.00000 0.00000 0.00000 0.00000 0.00000 233.29 368.71
LIQUID VOLUME FRACTION
0.000406 0.000770 0.000011 0.000002 0.000030 0.006072 0.000000 0.000000 0.000000 0.000000 0.000000 0.384700 0.608009
Total 22553 1.0000 6.1403e+005 1.0000 606.41 1.0000
Liquid Phase
Phase Fraction 1.000e-008 COMPONENTSHydrogen
MOLAR FLOW (kgmole/h)
5.8314e-008
MOLE FRACTION 0.000259
MASS FLOW (kg/h) 1.1756e-007
MASS FRACTION 0.000019
LIQUID VOLUME FLOW (m3/h)
1.6828e-009
LIQUID VOLUME FRACTION
0.000278
Honeywell International Inc. UniSim Design (R460.1 build 21106) Page 1 of 2
Licensed to: Printed by: user * Specified by user.
Calgary, Alberta CANADA
Case Name: C:\Users\user\Downloads\CO2 Absorber.usc Unit Set: NewUser4
Date/Time: Thursday Feb 27 2025, 10:03:29
Material Stream: Bottom A-101-E (continued)
Fluid Package: Basis-1Property Package: General NRTL - Ideal
COMPOSITION
Liquid Phase (continued)
Phase Fraction 1.000e-008 COMPONENTSNitrogen Methane Argon CO CO2 Oxygen Ethane Propane i-Butane n-Butane MDEAmine H2O
MOLAR FLOW (kgmole/h)
1.3598e-007 5.2246e-010 3.9456e-010 6.3385e-009 4.4490e-007 0.00000 0.00000 0.00000 0.00000 0.00000 2.0385e-005 2.0450e-004
MOLE FRACTION 0.000603 0.000002 0.000002 0.000028 0.001973 0.000000 0.000000 0.000000 0.000000 0.000000 0.090388 0.906745
MASS FLOW (kg/h) 3.8092e-006 8.3817e-009 1.5762e-008 1.7755e-007 1.9580e-005 0.00000 0.00000 0.00000 0.00000 0.00000 2.4291e-003 3.6841e-003
MASS FRACTION 0.000621 0.000001 0.000003 0.000029 0.003190 0.000000 0.000000 0.000000 0.000000 0.000000 0.395822 0.600314
LIQUID VOLUME FLOW (m3/h)
4.7239e-009 2.7996e-011 1.1504e-011 2.2211e-010 2.3723e-008 0.00000 0.00000 0.00000 0.00000 0.00000 2.3357e-006 3.6915e-006
LIQUID VOLUME FRACTION
0.000780 0.000005 0.000002 0.000037 0.003916 0.000000 0.000000 0.000000 0.000000 0.000000 0.385581 0.609401
Total 2.2553e-004 1.0000 6.1369e-003 1.0000 6.0576e-006 1.0000
K VALUE
COMPONENTS
Hydrogen Nitrogen Methane Argon CO CO2 Oxygen Ethane Propane i-Butane n-Butane MDEAmine H2O
MIXED
0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 --- --- --- --- --- 0.0000 0.0000
LIGHT
0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 --- --- --- --- --- 0.0000 0.0000
HEAVY
0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 --- --- --- --- --- 0.0000 0.0000
UNIT OPERATIONS
FEED TO PRODUCT FROM
Material Stream: liq @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Honeywell International Inc. UniSim Design (R460.1 build 21106) Page 2 of 2
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