(A stripping column having a given number of trays)3 A saturated liquid mixture of benzene and toluene having 70 mole% benzene is fed continuously at a rate of 40 kmol/h to the top tray of a column having six theoretical trays. There is no reflux at the top. The rate of vapour generation in the reboiler is 30 kmol/h. Determine the equation of the operating line and the rates and compositions of the product. (Note: This column may be called a 'stripping column'.)

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
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(A stripping column having a given number of trays) A saturated liquid mixture of
benzene and toluene having 70 mole% benzene is fed continuously at a rate of 40 kmo/n
to the top tray of a column having six theoretical trays. There is no reflux at the top.
rate of vapour generation in the reboiler is 30 kmol/h. Determine the equation of the
operating line and the rates and compositions of the product. (Note: This column may be
called a 'stripping column'.)
The
Transcribed Image Text:(A stripping column having a given number of trays) A saturated liquid mixture of benzene and toluene having 70 mole% benzene is fed continuously at a rate of 40 kmo/n to the top tray of a column having six theoretical trays. There is no reflux at the top. rate of vapour generation in the reboiler is 30 kmol/h. Determine the equation of the operating line and the rates and compositions of the product. (Note: This column may be called a 'stripping column'.) The
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