Using the Depriester chart, calculate what fraction of liquid and what fraction of vapor will exist in equilibrium when a mixture of hydrocarbons as detailed below is vaporized at 150°F and 50 psia. Substance Composition Ethane 0,0079 Propane 0.1321 i-Butane 0.0849 n-Butane 0.2690 i-Pentane 0.0589 n-pentane 0.1321 n-hexane 0.3151 total 100
Using the Depriester chart, calculate what fraction of liquid and what fraction of vapor will exist in equilibrium when a mixture of hydrocarbons as detailed below is vaporized at 150°F and 50 psia. Substance Composition Ethane 0,0079 Propane 0.1321 i-Butane 0.0849 n-Butane 0.2690 i-Pentane 0.0589 n-pentane 0.1321 n-hexane 0.3151 total 100
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:Using the Depriester chart, calculate what
fraction of liquid and what fraction of vapor will
exist in equilibrium when a mixture of
hydrocarbons as detailed below is vaporized at
150°F and 50 psia.
Substance
Composition
Ethane
0,0079
Propane
0.1321
i-Butane
0.0849
n-Butane
0.2690
i-Pentane
0.0589
n-pentane
0.1321
n-hexane
0.3151
total
100
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