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11.1 The one parameter Margules equation can be used to model the VLLE at 308 K for a systerm of methanol (1) and cyclohexane (2). At this temperature the Margules parameter, A - 2.415. This information was used to estimate the pressure and composition for the system and the following result was noted: X = 0.166 x,2 - 0.834 V= 0.579 P= 42.2 kPa You are given the above information and requested to verity if the result of the estimation is correct.

11.1 The one parameter Margules equation can be used to model the VLLE at 308 K for a systerm of methanol (1) and cyclohexane (2). At this temperature the Margules parameter, A - 2.415. This information was used to estimate the pressure and composition for the system and the following result was noted: X = 0.166 x,2 - 0.834 V= 0.579 P= 42.2 kPa You are given the above information and requested to verity if the result of the estimation is correct.

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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11.1 The one parameter Margules equation can be used to model the VLLE at 308 K for a systerm of methanol (1) and cyclohexane (2). At this temperature the Margules parameter, A - 2.415. This information was used to estimate the pressure and composition for the system and the following result was noted: X1 = 0.166 x,2 = 0.834 V= 0.579 P= 42.2 kPa You are given the above information and requested to verify if the result of the estimation is correct.
Transcribed Image Text:11.1 The one parameter Margules equation can be used to model the VLLE at 308 K for a systerm of methanol (1) and cyclohexane (2). At this temperature the Margules parameter, A - 2.415. This information was used to estimate the pressure and composition for the system and the following result was noted: X1 = 0.166 x,2 = 0.834 V= 0.579 P= 42.2 kPa You are given the above information and requested to verify if the result of the estimation is correct.
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