An exothermic reaction, A→2B, takes place adiabatically in a constant volume stirred-tank reactor (CSTR). This liquid reaction occurs at constant volume in a 4,000 L reactor. The reaction can be considered to be first order & irreversible with the rate constant given by k=2.4x 10¹5 e-20,000/T min¹ where T is given in °R. (a) Using the information below derive a transfer function relating the exit temperature T to the inlet concentration C... State all assumptions that you make.

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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Available information:
Nominal steady state information:
T* = 150 °F
C =0.01 mol/L
Ai
F = 80 L/min
Other properties:
C₂ = 3.3 kJ/kg. K
P
p=0.8 g/L
-AHR = 500 kJ/mol @ 25°C
Transcribed Image Text:Available information: Nominal steady state information: T* = 150 °F C =0.01 mol/L Ai F = 80 L/min Other properties: C₂ = 3.3 kJ/kg. K P p=0.8 g/L -AHR = 500 kJ/mol @ 25°C
An exothermic reaction, A2B, takes place adiabatically in a constant volume stirred-tank
reactor (CSTR). This liquid reaction occurs at constant volume in a 4,000 L reactor. The reaction can
be considered to be first order & irreversible with the rate constant given by
k=2.4x10¹5 e-20,000/T min¹
where I' is given in °R.
(a) Using the information below derive a transfer function relating the exit temperature T to
the inlet concentration C₁. State all assumptions that you make.
Transcribed Image Text:An exothermic reaction, A2B, takes place adiabatically in a constant volume stirred-tank reactor (CSTR). This liquid reaction occurs at constant volume in a 4,000 L reactor. The reaction can be considered to be first order & irreversible with the rate constant given by k=2.4x10¹5 e-20,000/T min¹ where I' is given in °R. (a) Using the information below derive a transfer function relating the exit temperature T to the inlet concentration C₁. State all assumptions that you make.
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