The following exothermic, reversible, gas-phase reaction is to be carried out in a CSTR: A =B The reaction is reversible and the rate is given by: r = k(CA- CB/Kc) The heat of reaction is -20 kcal/mol and the component heat capacities are CPA = CPB = 50 cal/mol/K. Both the heat of reaction and the heat capacities may be assumed constant. At 298K, the equilibrium constant, Kc, is 10". Determine the maximum possible conversion if the reactor operates adiabatically and the feed contains pure A at a temperature of 300K.

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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The following exothermic, reversible, gas-phase reaction is to be carried out in a CSTR:
AB
The reaction is reversible and the rate is given by:
r = k(CA – CB/Kc)
The heat of reaction is -20 kcal/mol and the component heat capacities are CPA = CPB = 50 cal/mol/K. Both the heat of reaction and the heat capacities may be assumed constant. At 298K, the
equilibrium constant, Kc, is 10°.
Determine the maximum possible conversion if the reactor operates adiabatically and the feed contains pure A at a temperature of 300K.
Transcribed Image Text:The following exothermic, reversible, gas-phase reaction is to be carried out in a CSTR: AB The reaction is reversible and the rate is given by: r = k(CA – CB/Kc) The heat of reaction is -20 kcal/mol and the component heat capacities are CPA = CPB = 50 cal/mol/K. Both the heat of reaction and the heat capacities may be assumed constant. At 298K, the equilibrium constant, Kc, is 10°. Determine the maximum possible conversion if the reactor operates adiabatically and the feed contains pure A at a temperature of 300K.
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