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2-F,+ A mixture containing 45.1 mol % propanc, 18.3 mol , isobutane, and 36.6 mol , n-butane is flashed in a drum at 367 K and 2.41 MPa. Estimate the mole fraction of the original mixture vaporized at equilibrium, and the compositions of the liquid and vapor phases. Equitibrium vaporization constants at these conditions may be taken lo be K 1.42 Propane Isobutane 0.86 n-Butane 0.72

2-F,+ A mixture containing 45.1 mol % propanc, 18.3 mol , isobutane, and 36.6 mol , n-butane is flashed in a drum at 367 K and 2.41 MPa. Estimate the mole fraction of the original mixture vaporized at equilibrium, and the compositions of the liquid and vapor phases. Equitibrium vaporization constants at these conditions may be taken lo be K 1.42 Propane Isobutane 0.86 n-Butane 0.72

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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2-F,+ A mixture containing 45.1 mol % propanc, 18.3 mol , isobutane, and 36.6 mol , n-butane is flashed in a drum at 367 K and 241 MPa. Estimate the mole fraction of the original mixture vaporized at equilibrium, and the compositions of the liquid and vapor phases. Equitibrium vaporization constants at these conditions may be laken lo be K Propane 1.42 Isobutane 0.86 n-Butane 0.72
Transcribed Image Text:2-F,+ A mixture containing 45.1 mol % propanc, 18.3 mol , isobutane, and 36.6 mol , n-butane is flashed in a drum at 367 K and 241 MPa. Estimate the mole fraction of the original mixture vaporized at equilibrium, and the compositions of the liquid and vapor phases. Equitibrium vaporization constants at these conditions may be laken lo be K Propane 1.42 Isobutane 0.86 n-Butane 0.72
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