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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
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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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
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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