LPG Plant
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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
|
Utilities Consumption
Power consumption
Power consumption(KW)
| |
feed gas compressor
|
767
|
R-22 refrigerating machine
|
348
|
R-23 refrigerating machine
|
215
|
Total power consumption
|
1330
|
Circulating water
Fuel gas
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