You can assume constant molar flow rates 3. A saturated vapor feed that is 90 %mol maleic anhydride and 10%mol benzoic acid is distilled at 99.8 torr to give a distillate that is 99.5 %mol maleic anhydride and a bottoms that is 0.5 %mol maleic anhydride. How many equilibrium stages are needed using a reflux ratio that is 1.6 times the minimum? The solution is ideal in both vapor and liquid stages. Vapor pressures can be estimated with the following Antoine equations in °C and torr:

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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You can assume constant molar flow rates
3. A saturated vapor feed that is 90 %mol maleic anhydride and 10%mol benzoic acid is distilled
at 99.8 torr to give a distillate that is 99.5 %mol maleic anhydride and a bottoms that is 0.5 %mol
maleic anhydride. How many equilibrium stages are needed using a reflux ratio that is 1.6 times
the minimum?
The solution is ideal in both vapor and liquid stages. Vapor pressures can be estimated with the
following Antoine equations in °C and torr:
Maleic anhydride: Pº = exp (16.6541
Benzoic acid: Ps =
exp (23.0155
4088.12
T+203.924
9336.97
T+321.434
Transcribed Image Text:You can assume constant molar flow rates 3. A saturated vapor feed that is 90 %mol maleic anhydride and 10%mol benzoic acid is distilled at 99.8 torr to give a distillate that is 99.5 %mol maleic anhydride and a bottoms that is 0.5 %mol maleic anhydride. How many equilibrium stages are needed using a reflux ratio that is 1.6 times the minimum? The solution is ideal in both vapor and liquid stages. Vapor pressures can be estimated with the following Antoine equations in °C and torr: Maleic anhydride: Pº = exp (16.6541 Benzoic acid: Ps = exp (23.0155 4088.12 T+203.924 9336.97 T+321.434
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