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5. The following is a set of VLE data for the system methanol (1) and benzene (2) at 90°C. Methanol (1) – Benzene (2) T=90°C Experimental Data P, mmHg yi X1 1865 0.117 0.502 2218 0.376 0.618 2273 0.549 0.650 2292 0.707 0.689 2208 0.856 0.765 Determine vapor-phase composition and pressure prediction at 90°C using the Margules equation with x1 = 0.549

5. The following is a set of VLE data for the system methanol (1) and benzene (2) at 90°C. Methanol (1) – Benzene (2) T=90°C Experimental Data P, mmHg yi X1 1865 0.117 0.502 2218 0.376 0.618 2273 0.549 0.650 2292 0.707 0.689 2208 0.856 0.765 Determine vapor-phase composition and pressure prediction at 90°C using the Margules equation with x1 = 0.549

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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5. The following is a set of VLE data for the system methanol (1) and benzene (2) at 90°C. Methanol (1) – Benzene (2) T=90°C Experimental Data P, mmHg X1 1865 0.117 0.502 2218 0.376 0.618 2273 0.549 0.650 2292 0.707 0.689 2208 0.856 0.765 Determine vapor-phase composition and pressure prediction at 90°C using the Margules equation with x1 = 0.549
Transcribed Image Text:5. The following is a set of VLE data for the system methanol (1) and benzene (2) at 90°C. Methanol (1) – Benzene (2) T=90°C Experimental Data P, mmHg X1 1865 0.117 0.502 2218 0.376 0.618 2273 0.549 0.650 2292 0.707 0.689 2208 0.856 0.765 Determine vapor-phase composition and pressure prediction at 90°C using the Margules equation with x1 = 0.549
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