The reservoir gas has a mixture composition at 200 °F and 2500 psia as tabulated i 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, u (cp).
The reservoir gas has a mixture composition at 200 °F and 2500 psia as tabulated i 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, u (cp).
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Transcribed Image 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).
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