(d) What conversion can be achieved if a 72-dm' PFR is followed in series by a 24-dm' CSTR? (e) What conversion can be achieved if a 24-dm' CSTR is followed in a series by a 72-dm' PFR? (f) Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume of 100 dm'.
(d) What conversion can be achieved if a 72-dm' PFR is followed in series by a 24-dm' CSTR? (e) What conversion can be achieved if a 24-dm' CSTR is followed in a series by a 72-dm' PFR? (f) Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume of 100 dm'.
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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
Transcribed Image Text:P2-4B The exothermic reaction of stillbene (A) to form the economically important trospophene (B) and
methane (C), i.e.,
A B+ C
was carried out adiabatically and the following data recorded:
0.2
0.4
0.45
0.5
0.6
0.8
0.9
-TA (mol/dm³-min)
1.0
1.67 5.0
5.0
5.0
5.0
1.25
0.91
The entering molar flow rate of A was 300 mol/min.
(a) What are the PFR and CSTR volumes necessary to achieve 40% conversion? (VPFR = 72 dm',
VCSTR = 24 dm³)
(b) Over what range of conversions would the CSTR and PFR reactor volumes be identical?
(c) What is the maximum conversion that can be achieved in a 105-dm3 CSTR?
(d) What conversion can be achieved if a 72-dm' PFR is followed in series by a 24-dm' CSTR?
(e) What conversion can be achieved if a 24-dm3 CSTR is followed in a series by a 72-dm3 PFR?
(f) Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume of
%3D
100 dm'.
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