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I posted this question before but didn't get the explanation, can I get an explanation on how to get fugacity coefficient using the written formula I attached, thanks.

I posted this question before but didn't get the explanation, can I get an explanation on how to get fugacity coefficient using the written formula I attached, thanks.

Introduction to Chemical Engineering Thermodynamics
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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I posted this question before but didn't get the explanation, can I get an explanation on how to get fugacity coefficient using the written formula I attached, thanks.
O ㅇㅇ In / fi (pure) 미 P T ㅣ | | 2-1 dp 렇
Transcribed Image Text:O ㅇㅇ In / fi (pure) 미 P T ㅣ | | 2-1 dp 렇
4 @85°C - A unit-operation in the manufacture of a light oil produces the oil at 200 K and 30 bar along with some CH4 gas. At equilibrium, this binary system of CH4 (1) and light oil (2) consists of a vapour phase containing 95 mol % CH4 and a liquid phase that contains the oil and a small amount of dissolved CH4. The fugacity of CH4 in the liquid phase at 200 K is given by Henry's law with the constant k₁= 200 bar. Determine the mole fraction of CH4 in the liquid phase. 0.989 Assume that CH4 in the vapour phase obeys the Lewis-Randall rule. The P-V-T behaviour of CH4 is described by the truncated virial equation: Z = 1 + BP/RT which may be used to calculate the thermodynamic properties of pure CH4. The second virial coefficient, B = -105 cm³ mol-1 for CH4 at 200 K. given (4 (1) P= 36 ber oil (2) T= 200k
Transcribed Image Text:4 @85°C - A unit-operation in the manufacture of a light oil produces the oil at 200 K and 30 bar along with some CH4 gas. At equilibrium, this binary system of CH4 (1) and light oil (2) consists of a vapour phase containing 95 mol % CH4 and a liquid phase that contains the oil and a small amount of dissolved CH4. The fugacity of CH4 in the liquid phase at 200 K is given by Henry's law with the constant k₁= 200 bar. Determine the mole fraction of CH4 in the liquid phase. 0.989 Assume that CH4 in the vapour phase obeys the Lewis-Randall rule. The P-V-T behaviour of CH4 is described by the truncated virial equation: Z = 1 + BP/RT which may be used to calculate the thermodynamic properties of pure CH4. The second virial coefficient, B = -105 cm³ mol-1 for CH4 at 200 K. given (4 (1) P= 36 ber oil (2) T= 200k
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