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Acetone vapour is considered toxic to the environment (as well as human health). As Example 5.1. an engineer in the chemical plant, you are asked to design an acetonerecovery system having the flow sheet illustrated on the next page. In this Example, to make the calculation simple, all concentrations of both gases and liquids are in presented in weight (mass) percent (please note, however, that, normally, for gas phase, the concentration is presented in “volume“ and “mole“ basis) Calculate the values of A, F, W, B, and D in kg per hour, if given G = 1,400 kg/h water (100%) w ka/h Air TA ko/h Air 99.5 water O.5% Condenser Distillattet D ka/ Aceton e 99.0% water 1.0% Absorber Distillation column 2) column Bottonm B kg/h Acetone 4.0% water 96.0% kg/h Acetone 19.09% water 81.0% Feed G kg/h Acetone 3.0% Air 95.0% Water 2.0%

Acetone vapour is considered toxic to the environment (as well as human health). As Example 5.1. an engineer in the chemical plant, you are asked to design an acetonerecovery system having the flow sheet illustrated on the next page. In this Example, to make the calculation simple, all concentrations of both gases and liquids are in presented in weight (mass) percent (please note, however, that, normally, for gas phase, the concentration is presented in “volume“ and “mole“ basis) Calculate the values of A, F, W, B, and D in kg per hour, if given G = 1,400 kg/h water (100%) w ka/h Air TA ko/h Air 99.5 water O.5% Condenser Distillattet D ka/ Aceton e 99.0% water 1.0% Absorber Distillation column 2) column Bottonm B kg/h Acetone 4.0% water 96.0% kg/h Acetone 19.09% water 81.0% Feed G kg/h Acetone 3.0% Air 95.0% Water 2.0%

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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Example 5.1. an engineer in the chemical plant, you are asked to design an acetonerecovery system having the flow sheet illustrated on the next page. In this Example, to make the calculation simple, all concentrations of both gases and liquids are in presented in weight (mass) percent (please note, Acetone vapour is considered toxic to the environment (as well as human health). As however, that, normally, for gas phase, the concentration is presented in “volume“ and “mole“ basis) Calculate the values of A, F, W, B, and D in kg per hour, if given G = 1,400 kg/h water (100%) w Ka/h Air tA ka/h Air 99.5 water O.5% Condenser Distillattet D kO/ Aceton e 99.0% water 1.0% Absorber Distillation column 2) column -Bottom ka/h Acetone 19.09% water 81.0% B kg/h Acetone 4.0% water 96.0% Feed G kg/h Acetone 3.0% Air 95.0% Water 2.0%
Transcribed Image Text:Example 5.1. an engineer in the chemical plant, you are asked to design an acetonerecovery system having the flow sheet illustrated on the next page. In this Example, to make the calculation simple, all concentrations of both gases and liquids are in presented in weight (mass) percent (please note, Acetone vapour is considered toxic to the environment (as well as human health). As however, that, normally, for gas phase, the concentration is presented in “volume“ and “mole“ basis) Calculate the values of A, F, W, B, and D in kg per hour, if given G = 1,400 kg/h water (100%) w Ka/h Air tA ka/h Air 99.5 water O.5% Condenser Distillattet D kO/ Aceton e 99.0% water 1.0% Absorber Distillation column 2) column -Bottom ka/h Acetone 19.09% water 81.0% B kg/h Acetone 4.0% water 96.0% Feed G kg/h Acetone 3.0% Air 95.0% Water 2.0%
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