An irreversible gas-phase reaction is carried out in a batch reactor at 25°C. The reaction is A+B C The rate of disappearance of reactant A is given by the following function: (-ra)= KCACB (mol/m³.s), where k= 3.5*10-5 m³/mol.s The reactor is filled with an equal number of moles of A and B. The initial concentration of A is CAO = 50 mol/m³. Calculate the fractional conversion of A after 500s for the following three types of batch reactors. Assume ideal gases. a. Constant-volume reactor b. Constant-pressure reactor c. Variable-volume reactor where V = Vo (1 + 0.001t)
An irreversible gas-phase reaction is carried out in a batch reactor at 25°C. The reaction is A+B C The rate of disappearance of reactant A is given by the following function: (-ra)= KCACB (mol/m³.s), where k= 3.5*10-5 m³/mol.s The reactor is filled with an equal number of moles of A and B. The initial concentration of A is CAO = 50 mol/m³. Calculate the fractional conversion of A after 500s for the following three types of batch reactors. Assume ideal gases. a. Constant-volume reactor b. Constant-pressure reactor c. Variable-volume reactor where V = Vo (1 + 0.001t)
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:An irreversible gas-phase reaction is carried out in a batch reactor at 25°C. The reaction is
A+B C
The rate of disappearance of reactant A is given by the following function:
(-A) =KCACB (mol/m³.s), where k= 3.5*10-5 m³/mol.s
The reactor is filled with an equal number of moles of A and B. The initial concentration of A is CAO = 50
mol/m³. Calculate the fractional conversion of A after 500s for the following three types of batch reactors.
Assume ideal gases.
a. Constant-volume reactor
b. Constant-pressure reactor
c. Variable-volume reactor where V = Vo (1 + 0.001t)
ole
B wk
eme
ers
m
JE
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