6.13. A reaction A B is to be carried out in a system consisting of a PFR and a CFSTR operated at steady state. Compare the results for the two reaction expressions below for (a) PFR → CFSTR and (b) CFSTR→ PFR. System characteristics: VPFR = 100 m³ VCFSTR = 1000 m³ Q = 0.05 m³/s = CA₁ = 150 g/m³ First-order reaction:

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Chapter1: Introduction
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6.13. A reaction A → B is to be carried out in a system consisting of a
PFR and a CFSTR operated at steady state. Compare the results for
the two reaction expressions below for (a) PFR → CFSTR and (b)
CFSTR→ PFR.
System characteristics:
VPFR = 100 m³
1000 m³
VCFSTR
=
Q = 0.05 m³/s
CA, = 150 g/m³
First-order reaction:
TA=-10-5 C₁ g/m³-s
Second-order reaction:
TA=-10-5Cg/m³/s
Transcribed Image Text:6.13. A reaction A → B is to be carried out in a system consisting of a PFR and a CFSTR operated at steady state. Compare the results for the two reaction expressions below for (a) PFR → CFSTR and (b) CFSTR→ PFR. System characteristics: VPFR = 100 m³ 1000 m³ VCFSTR = Q = 0.05 m³/s CA, = 150 g/m³ First-order reaction: TA=-10-5 C₁ g/m³-s Second-order reaction: TA=-10-5Cg/m³/s
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