2. The reaction A → B is to be carried out in a flow reactor. Data for the reaction is given below. You have two CSTRs and two PFRS, each with a volume of 2 L. ΧΑ FAO-TA (L) 0.0 1.112 0.1 1.363 0.2 0.4 1.663 2.563 0.6 4.425 Calculate the conversion for each reactor in the following arrangements: a. Two CSTRS in series 0.7 0.8 6.325 10.0 b. Two PFRs in series c. Two CSTRs in parallel with the feed, FA0, divided equally between the two reactors. d. Two PFRs in parallel with the feed divided equally between the two reactors. e. A CSTR followed by a PFR f. A PFR followed by a CSTR g. A PFR followed by two CSTRS

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
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2. The reaction A → B is to be carried out in a flow reactor. Data for the reaction is given
below. You have two CSTRs and two PFRS, each with a volume of 2 L.
ΧΑ
FAO-TA (L)
0.0
1.112
0.1
1.363
0.2
0.4
1.663
2.563
0.6
4.425
Calculate the conversion for each reactor in the following arrangements:
a. Two CSTRS in series
0.7
0.8
6.325
10.0
b. Two PFRs in series
c. Two CSTRs in parallel with the feed, FA0, divided equally between the two reactors.
d. Two PFRs in parallel with the feed divided equally between the two reactors.
e. A CSTR followed by a PFR
f.
A PFR followed by a CSTR
g. A PFR followed by two CSTRS
Transcribed Image Text:2. The reaction A → B is to be carried out in a flow reactor. Data for the reaction is given below. You have two CSTRs and two PFRS, each with a volume of 2 L. ΧΑ FAO-TA (L) 0.0 1.112 0.1 1.363 0.2 0.4 1.663 2.563 0.6 4.425 Calculate the conversion for each reactor in the following arrangements: a. Two CSTRS in series 0.7 0.8 6.325 10.0 b. Two PFRs in series c. Two CSTRs in parallel with the feed, FA0, divided equally between the two reactors. d. Two PFRs in parallel with the feed divided equally between the two reactors. e. A CSTR followed by a PFR f. A PFR followed by a CSTR g. A PFR followed by two CSTRS
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