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Define: a. Rate of reaction in moles/hour.m3 b. The limiting location or stage i.e. having the main resistance

Define: a. Rate of reaction in moles/hour.m3 b. The limiting location or stage i.e. having the main resistance

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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A reaction A (g→l) + B(I) → R(1) with -rA=KCACB In the packed bed reactor with conditions kAga = 0.1 mol/hour.m2.Pa kAla = 100 m3liquid/m3.hour a = 100 m2/m3 fl=0.01 m3liquid/m3reactor Dal=Dbl = 10-6 m2/hour (diffusivity) k = 10 m3liquid/mol.hour HA = 105 Pa.m3 lig/mol 3 %3D РА 3 100 Ра CB = 100 mol/m3 liquid %3D Define: a. Rate of reaction in moles/hour.m3 b. The limiting location or stage i.e. having the main resistance
Transcribed Image Text:A reaction A (g→l) + B(I) → R(1) with -rA=KCACB In the packed bed reactor with conditions kAga = 0.1 mol/hour.m2.Pa kAla = 100 m3liquid/m3.hour a = 100 m2/m3 fl=0.01 m3liquid/m3reactor Dal=Dbl = 10-6 m2/hour (diffusivity) k = 10 m3liquid/mol.hour HA = 105 Pa.m3 lig/mol 3 %3D РА 3 100 Ра CB = 100 mol/m3 liquid %3D Define: a. Rate of reaction in moles/hour.m3 b. The limiting location or stage i.e. having the main resistance
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