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Using the equilibrium data shown below for benzene-toluene system at 1 atm with relative volatility of 2.5: Molar composition Enthalpy (kJ/kg) Xa Ya hy 1 116.2 511.1 0.775 0.899 124.7 515.4 0.579 0.776 133.6 519.7 0.408 0.63 142.5 523.8 0.259 0.459 151.5 527.7 0.128 0.259 160.5 531.5 170.4 535.5

Using the equilibrium data shown below for benzene-toluene system at 1 atm with relative volatility of 2.5: Molar composition Enthalpy (kJ/kg) Xa Ya hy 1 116.2 511.1 0.775 0.899 124.7 515.4 0.579 0.776 133.6 519.7 0.408 0.63 142.5 523.8 0.259 0.459 151.5 527.7 0.128 0.259 160.5 531.5 170.4 535.5

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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Help me construct the enthalpy-composition (H-x-y) diagram of this benzene-toluene mixture.

Using the equilibrium data shown below for benzene-toluene system at 1 atm with relative volatility of 2.5: Molar composition Enthalpy (kJ/kg) Xa Ya hy 1 116.2 511.1 0.775 0.899 124.7 515.4 0.579 0.776 133.6 519.7 0.408 0.63 142.5 523.8 0.259 0.459 151.5 527.7 0.128 0.259 160.5 531.5 170.4 535.5
Transcribed Image Text:Using the equilibrium data shown below for benzene-toluene system at 1 atm with relative volatility of 2.5: Molar composition Enthalpy (kJ/kg) Xa Ya hy 1 116.2 511.1 0.775 0.899 124.7 515.4 0.579 0.776 133.6 519.7 0.408 0.63 142.5 523.8 0.259 0.459 151.5 527.7 0.128 0.259 160.5 531.5 170.4 535.5
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