an overhead product containing 95 mol% solvent and to recover 95% of the solvent in the feed. The feed 4) A solvent is to be recovered by distillation from its aqueous solution. It is necessary to prod operating reflux ratio, L/D, be 1.33 times the minimum value. A total condenser will be employed. For necessary heat in the form of open steam. For the preliminary design, it has been suggested that the is availiable at the plant site in two streams, one containing 40 mol% A and the other 60 mol% A Each stream has a total flow rate of 50 kmol/h, and each will be fed into the column as saturated liquid at their optimal location. Since the less volatile component is water, it has been proposed to supply the tnts system, it is estimated that the overall column efficiencu will be 70%. The relative volatility mag be assumed to be constant at 3.0. a. How many plates will be required? b. What will be the bottoms composition?

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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4) A solvent is to be recovered by distillation from its aqueous solution. It is necessary to produce
an overhead product containing 95 mol% solvent and to recover 95% of the solvent in the feed. The feed
operating reflux ratio, L/D, be 1.33 times the minimum value. A total condenser will be employed. For
necessary heat in the form of open steam. For the preliminary design, it has been suggested that the
is availiable at the plant site in two streams, one containing 40 mol% A and the other 60 mol% A. Each
stream has a total flow rate of 50 kmol/h, and each will be fed into the column as saturated liquid at
this system, it is estimated that the overall column efficiency will be 70%. The relative volatility may be
their optimal location. Since the less volatile component is water, it has been proposed to supply the
assumed to be constant at 3.0.
a. How many plates will be required?
b. What will be the bottoms composition?
Transcribed Image Text:4) A solvent is to be recovered by distillation from its aqueous solution. It is necessary to produce an overhead product containing 95 mol% solvent and to recover 95% of the solvent in the feed. The feed operating reflux ratio, L/D, be 1.33 times the minimum value. A total condenser will be employed. For necessary heat in the form of open steam. For the preliminary design, it has been suggested that the is availiable at the plant site in two streams, one containing 40 mol% A and the other 60 mol% A. Each stream has a total flow rate of 50 kmol/h, and each will be fed into the column as saturated liquid at this system, it is estimated that the overall column efficiency will be 70%. The relative volatility may be their optimal location. Since the less volatile component is water, it has been proposed to supply the assumed to be constant at 3.0. a. How many plates will be required? b. What will be the bottoms composition?
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