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  1. Mahmoud1984

    Extracting LPG

    I have a case where there is a quantity of natural gas of 50 MMSCFD having the following composition : N2 0.0988 CO2 0.65 C1 91.2626 C2 6.3481 C3 1.375 IC4 0.1703 NC4 0.0835 NEO C5 0.0005 IC5 0.0068 NC5 0.0022 C6+ 0.0024 Preesure is 55 barg and temperature is -10°C upstream the turbo expander...

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