Topic: Catalytic Rxn in Packed Bed Reactor PROVIDE HANDWRITTEN SOLUTION PLEASE Based on the topic stated and the data obtained, the rxn A+B=C follows the mechanism given below. Step Adsorption Surface Reaction Desorption Rate Law TAD = KA (PACv – CAS) КА Cc.s] T3 = K₂ [C₁SPB - CCS] Ks TD = KD [CC.S - PBCv| Кр Derive an expression that concerns the -TA' (overall rate of rxn). Note: mass transfer effects are negligible and desorption rate is rate limiting

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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Topic: Catalytic Rxn in Packed Bed Reactor
PROVIDE HANDWRITTEN SOLUTION PLEASE
Based on the topic stated and the data obtained, the rxn A+B=C follows the mechanism
given below.
Step
Adsorption
Surface Reaction
Desorption
Rate Law
TAD = KA (PACv – CAS)
КА
Cc.s]
73 = ks [CA.SPB - CCS]
Ks
TD = KD [CC.S - PBCv|
Кр
Derive an expression that concerns the -TA'
(overall rate of rxn).
Note: mass transfer effects are negligible and desorption rate is rate limiting
Transcribed Image Text:Topic: Catalytic Rxn in Packed Bed Reactor PROVIDE HANDWRITTEN SOLUTION PLEASE Based on the topic stated and the data obtained, the rxn A+B=C follows the mechanism given below. Step Adsorption Surface Reaction Desorption Rate Law TAD = KA (PACv – CAS) КА Cc.s] 73 = ks [CA.SPB - CCS] Ks TD = KD [CC.S - PBCv| Кр Derive an expression that concerns the -TA' (overall rate of rxn). Note: mass transfer effects are negligible and desorption rate is rate limiting
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