CH4 70.79 18.40 C2 13.32 0.00 C3 7.11 0.00 iC4 1.60 0.00 nC4 2.60 0.00 iC5 0.40 0.00 nC5 0.40 0.00 nC6 0.08 0.00 Table B4. MP Resulting Streams - Process 1 (2S) for 10% CO2 in Raw Natural Gas Retentate 2 Permeate 35 35 Temperature (ºC) Pressure (bar) 49.5 4 Molar Flow 4.67 0.95 (MMsm3/d) N2 0.30 0.00 CO2 3.00 47.10 CH4 83.09 52.90 C2 6.01 0.00 C3 3.70 0.00 % Molar iC4 1.00 0.00 nC4 1.90 0.00 iC5 0.40 0.00 nC5 0.50 0.00 nC6 0.10 0.00 2S = 2-stages membrane permeation arrangement. B5. MP Resulting Streams - Process 1 (2S) for 30% CO2 in Raw Natural Gas Retentate 2 Permeate 35 35 Temperature (ºC) Pressure (bar) 49.5 4
CH4 70.79 18.40 C2 13.32 0.00 C3 7.11 0.00 iC4 1.60 0.00 nC4 2.60 0.00 iC5 0.40 0.00 nC5 0.40 0.00 nC6 0.08 0.00 Table B4. MP Resulting Streams - Process 1 (2S) for 10% CO2 in Raw Natural Gas Retentate 2 Permeate Temperature (ºC) 35 35 Pressure (bar) 49.5 4 Molar Flow (MMsm3/d) 4.67 0.95 % Molar N2 0.30 0.00 CO2 3.00 47.10 CH4 83.09 52.90 C2 6.01 0.00 C3 3.70 0.00 iC4 1.00 0.00 nC4 1.90 0.00 iC5 0.40 0.00 nC5 0.50 0.00 nC6 0.10 0.00 2S = 2-stages membrane permeation arrangement. B5. MP Resulting Streams - Process 1 (2S) for 30% CO2 in Raw Natural Gas Retentate 2 Permeate Temperature (ºC) 35 35 Pressure (bar) 49.5 4
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