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Essentially 1 atm pressure throughout system cw, Benzene product cw Makeup phenol 30°C 1 atm 35 50.1 kmol/h kmol/h 300 Cyclohexane product 30 15 500 kmol/hr 200 kmol/h 1-atm bubble-point liquid cw 10 kmol/h Phenol Cyclohexane 55 Benzene гесycle 45 Steam Steam 2. 2.

Essentially 1 atm pressure throughout system cw, Benzene product cw Makeup phenol 30°C 1 atm 35 50.1 kmol/h kmol/h 300 Cyclohexane product 30 15 500 kmol/hr 200 kmol/h 1-atm bubble-point liquid cw 10 kmol/h Phenol Cyclohexane 55 Benzene гесycle 45 Steam Steam 2. 2.

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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A system for separating a binary mixture by extractive distillation,followed by ordinary distillation for recovery and recycle of the solvent, is shown in figure . Are the design variables shown sufficient to specify the problem completely? If not, what additional design variables(s) should be selected?

Essentially 1 atm pressure throughout system cw, Benzene product cw Makeup phenol 30°C 1 atm 35 50.1 kmol/h kmol/h 300 Cyclohexane product 30 15 500 kmol/hr 200 kmol/h 1-atm bubble-point liquid cw 10 kmol/h Phenol Cyclohexane 55 Benzene гесycle 45 Steam Steam 2. 2.
Transcribed Image Text:Essentially 1 atm pressure throughout system cw, Benzene product cw Makeup phenol 30°C 1 atm 35 50.1 kmol/h kmol/h 300 Cyclohexane product 30 15 500 kmol/hr 200 kmol/h 1-atm bubble-point liquid cw 10 kmol/h Phenol Cyclohexane 55 Benzene гесycle 45 Steam Steam 2. 2.
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