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3. A flash unit is used to separate any mixture into liquid and vapour streams at equilibrium. The compositions of the streams depend on the quantity of the feed vaporized. If the vapour-liquid equilibrium relationship is expressed in terms of equilibrium constants; calculate Ø=V/F ratio using the Bisection Method (E-0.03). The following data and equation are given as; P1 -Σ 0.1 <0 <1 (-1 Component Benzene Toluene o-xylene f(0) = Z₁ Ø(K-1) +1 1=0 Zi(feed mole fraction) 0.15 0.35 0.50 K₁ 0.170 0.625 12.25

3. A flash unit is used to separate any mixture into liquid and vapour streams at equilibrium. The compositions of the streams depend on the quantity of the feed vaporized. If the vapour-liquid equilibrium relationship is expressed in terms of equilibrium constants; calculate Ø=V/F ratio using the Bisection Method (E-0.03). The following data and equation are given as; P1 -Σ 0.1 <0 <1 (-1 Component Benzene Toluene o-xylene f(0) = Z₁ Ø(K-1) +1 1=0 Zi(feed mole fraction) 0.15 0.35 0.50 K₁ 0.170 0.625 12.25

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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3. A flash unit is used to separate any mixture into liquid and vapour streams at equilibrium. The compositions of the streams depend on the quantity of the feed vaporized. If the vapour-liquid equilibrium relationship is expressed in terms of equilibrium constants; calculate Ø=V/F ratio using the Bisection Method (E-0.03). The following data and equation are given as; 0.1 <0 <1 Zi Ø(K-1) +1 f(0) = 0(K i=1 Component Benzene Toluene o-xylene 1=0 Zi(feed mole fraction) 0.15 0.35 0.50 K₁ 0.170 0.625 12.25
Transcribed Image Text:3. A flash unit is used to separate any mixture into liquid and vapour streams at equilibrium. The compositions of the streams depend on the quantity of the feed vaporized. If the vapour-liquid equilibrium relationship is expressed in terms of equilibrium constants; calculate Ø=V/F ratio using the Bisection Method (E-0.03). The following data and equation are given as; 0.1 <0 <1 Zi Ø(K-1) +1 f(0) = 0(K i=1 Component Benzene Toluene o-xylene 1=0 Zi(feed mole fraction) 0.15 0.35 0.50 K₁ 0.170 0.625 12.25
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