Reactor Design Consider an irreversible, liquid-phase, elementary reaction 2A ⟶ B taking place in two continuous stirred tank reactors (CSTRs) in series under the same temperature. The second CSTR is two times larger than the first reactor by volume. The intermediate conversion of A exiting the first reactor prior to entering the second reactor is 50%. What is the value of the Damköhler number for the first reactor What is the conversion of A exiting the second CSTR? If a plug flow reactor (PFR) with a volume two times larger than the first CSTR is used as the second reactor instead, what would the conversion of A exiting the PFR?
Reactor Design Consider an irreversible, liquid-phase, elementary reaction 2A ⟶ B taking place in two continuous stirred tank reactors (CSTRs) in series under the same temperature. The second CSTR is two times larger than the first reactor by volume. The intermediate conversion of A exiting the first reactor prior to entering the second reactor is 50%. What is the value of the Damköhler number for the first reactor What is the conversion of A exiting the second CSTR? If a plug flow reactor (PFR) with a volume two times larger than the first CSTR is used as the second reactor instead, what would the conversion of A exiting the PFR?
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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Reactor Design
Consider an irreversible, liquid-phase, elementary reaction 2A ⟶ B taking place in two continuous stirred tank reactors (CSTRs) in series under the same temperature. The second CSTR is two times larger than the first reactor by volume. The intermediate conversion of A exiting the first reactor prior to entering the second reactor is 50%.
What is the value of the Damköhler number for the first reactor
What is the conversion of A exiting the second CSTR?
If a plug flow reactor (PFR) with a volume two times larger than the first CSTR is
used as the second reactor instead, what would the conversion of A exiting the PFR?
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