Calculate the time to reduce the number of moles of A to 1% of its initial value in a constant-volume batch reactor for the same reaction and data in Example 1-2. Suggest two ways to work this problem incorrectly.
Calculate the time to reduce the number of moles of A to 1% of its initial value in a constant-volume batch reactor for the same reaction and data in Example 1-2. Suggest two ways to work this problem incorrectly.
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
Related questions
Question
Calculate the time to reduce the number of moles of A to 1% of its initial
value in a constant-volume batch reactor for the same reaction and data in
Example 1-2. Suggest two ways to work this problem incorrectly.
![Consider the liquid phase cis - trans isomerization of 2-butene
H
H
H
CH3
ĆH3
CH3
ĆH;
H
cis-2-butene
trans-2-butene
which we will write symbolically as
A
→ B
The reaction is first order in A (-rA = kCA) and is carried out in a tubular reactor in
which the volumetric flow rate, v, is constant, i.e., v = vo .
CAO
CA = 0.1CAO
A B
V = 0 V
Vo
V1](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F84978478-0164-4ee9-9d49-e489a1d7bd3d%2F1951fb8d-a01f-476d-9069-8df6da9fcc7f%2F5t6tr47_processed.png&w=3840&q=75)
Transcribed Image Text:Consider the liquid phase cis - trans isomerization of 2-butene
H
H
H
CH3
ĆH3
CH3
ĆH;
H
cis-2-butene
trans-2-butene
which we will write symbolically as
A
→ B
The reaction is first order in A (-rA = kCA) and is carried out in a tubular reactor in
which the volumetric flow rate, v, is constant, i.e., v = vo .
CAO
CA = 0.1CAO
A B
V = 0 V
Vo
V1
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