LPG Plant

Process Routes and Solution of LPG Plant
According to the gas source and usages, we design to remove the heavy hydrocarbon in feed gas, produce LPG and stable light hydrocarbon at the same time make dry gas.
Feed Gas and Products

Name Feed Dry gas LPG Condensate Excess propane
Vapour Fraction 1.00 1.00 0.00 0.00 0.00
Temperature [C] 36.11 25.97 38.89 40.00 41.11
Pressure [bar_g] 6.89 22.41 5.88 0.69 12.78
Molar Flow [Nm3/h] 13500.48 12019.98 852.50 253.66 270.37
Mass Flow [kg/h] 13252.95 9735.29 2051.88 844.74 537.45
Act. Volume Flow [m3/h] 1889.00 533.60 3.89 1.38 1.15
Mole Fractions
Nitrogen 0.000300 0.000334 0.000000 0.000000 0.000000
CO2 0.007400 0.008247 0.000000 0.000000 0.000001
Methane 0.816900 0.910451 0.000000 0.000000 0.000001
Ethane 0.035700 0.039724 0.000429 0.000000 0.001508
Propane 0.066000 0.030576 0.300235 0.000000 0.964253
i-Butane 0.026400 0.005703 0.324863 0.000679 0.029613
n-Butane 0.027600 0.004127 0.371057 0.010088 0.004616
i-Pentane 0.009700 0.000551 0.003140 0.475632 0.000007
n-Pentane 0.006400 0.000251 0.000275 0.325197 0.000001
n-Hexane 0.003600 0.000036 0.000000 0.188404 0.000000
H2O 0.000000 0.000000 0.000000 0.000000 0.000000