If a continuous stirred tank reactor of volume (i.e contents) 0.025m³ is installed in series upstream of the plug flow reactor, what is the new overall conversion? All other parameters being unchanged.

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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Company 2 are looking a bimolecular irreversible reaction,
A+B=C+D
To be carried out in a liquid phase plug flow reactor. Given the reaction is second order and
the mass flow of A and B are respectively 85kg/hr and 110kg/hr. The reactor has a volume
of 0.15m³ and is operated isothermally at 112°C giving a conversion of 70%. Can you
conduct the following sub tasks:
If a continuous stirred tank reactor of volume (i.e contents) 0.025m³ is
installed in series upstream of the plug flow reactor, what is the new
overall conversion? All other parameters being unchanged.
Transcribed Image Text:Company 2 are looking a bimolecular irreversible reaction, A+B=C+D To be carried out in a liquid phase plug flow reactor. Given the reaction is second order and the mass flow of A and B are respectively 85kg/hr and 110kg/hr. The reactor has a volume of 0.15m³ and is operated isothermally at 112°C giving a conversion of 70%. Can you conduct the following sub tasks: If a continuous stirred tank reactor of volume (i.e contents) 0.025m³ is installed in series upstream of the plug flow reactor, what is the new overall conversion? All other parameters being unchanged.
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