A simple (i.e. single equilibrium stage) batch still is being used to separate benzene from o-xylene; a system which may be assumed to have a constant relative volatility of 6.7. The feed to the still is 1000 mol of 60 mol% benzene. The process is run until the instantaneous distillate composition is 70 mol% benzene. Determine: a)the composition and amount of the residue remaining in the still pot. b)the amount and average composition of the distillate. c)the time required for the process to run if the boil-up rate is 50 mol/h
A simple (i.e. single equilibrium stage) batch still is being used to separate benzene from o-xylene; a system which may be assumed to have a constant relative volatility of 6.7. The feed to the still is 1000 mol of 60 mol% benzene. The process is run until the instantaneous distillate composition is 70 mol% benzene. Determine: a)the composition and amount of the residue remaining in the still pot. b)the amount and average composition of the distillate. c)the time required for the process to run if the boil-up rate is 50 mol/h
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 simple (i.e. single equilibrium stage) batch still is being used to separate benzene from o-xylene; a system which may be assumed to have a constant relative volatility of 6.7. The feed to the still is 1000 mol of 60 mol% benzene. The process is run until the instantaneous distillate composition is 70 mol% benzene. Determine:
a)the composition and amount of the residue remaining in the still pot.
b)the amount and average composition of the distillate.
c)the time required for the process to run if the boil-up rate is 50 mol/h.
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