The reservoir gas has a mixture composition at 200 °F and 2500 psia as tabulated in table 2 below. Table 2: Gas mixture composition. Gas components Weight, Ib Methane 28 Ethane 3.5 Propane 1.8...

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The reservoir gas has a mixture composition at 200 °F and 2500 psia as tabulated in table 2 below.<br>Table 2: Gas mixture composition.<br>Gas components<br>Weight, Ib<br>Methane<br>28<br>Ethane<br>3.5<br>Propane<br>1.8<br>Hydrogen<br>Sulphide<br>4<br>Carbon Dioxide<br>12<br>Nitrogen<br>3.5<br>Total<br>52.8<br>Calculate:<br>a) Weight fraction for each component.<br>b) Mole fraction for each component.<br>c) Pseudo critical pressure for the mixture (psia).<br>d) Pseudo critical temperature for the mixture (°R).<br>e) Find the compressibility factor (z).<br>f) Gas viscosity at 200°F and 14.7 psia, la (cp).<br>g) Gas viscosity at reservoir condition, µ (cp).<br>

Extracted text: The reservoir gas has a mixture composition at 200 °F and 2500 psia as tabulated in table 2 below. Table 2: Gas mixture composition. Gas components Weight, Ib Methane 28 Ethane 3.5 Propane 1.8 Hydrogen Sulphide 4 Carbon Dioxide 12 Nitrogen 3.5 Total 52.8 Calculate: a) Weight fraction for each component. b) Mole fraction for each component. c) Pseudo critical pressure for the mixture (psia). d) Pseudo critical temperature for the mixture (°R). e) Find the compressibility factor (z). f) Gas viscosity at 200°F and 14.7 psia, la (cp). g) Gas viscosity at reservoir condition, µ (cp).

Jun 10, 2022
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