The following isothermal, isobaric, catalytic gas-phase oxidation reaction is carried out in a reactor: C₂H4(g) +0.50₂ (g)-CH₂OCH₂(g). The reactor is operated at 6 atm and 260 °C. The feed is a stoichiometric mixture of ethylene and oxygen. You may assume the reaction is elementary. Set up the stoichiometric table and express -r as a function of partial pressures. Express the partial pressures and as a function of conversion for fluidized batch reactor and for a PBR (PFR like). Write-r as a function of the rate constant and conversion only.

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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The following isothermal, isobaric, catalytic gas-phase oxidation
reaction is carried out in a reactor:
C₂H4(g) +0.50₂ (g)-CH₂OCH₂(g).
The reactor is operated at 6 atm and 260 °C. The feed is a
stoichiometric mixture of ethylene and oxygen. You may assume the
reaction is elementary.
Set up the stoichiometric table and express -r as a function of
partial pressures. Express the partial pressures and as a function
of conversion for fluidized batch reactor and for a PBR (PFR like).
Write-r as a function of the rate constant and conversion only.
Transcribed Image Text:The following isothermal, isobaric, catalytic gas-phase oxidation reaction is carried out in a reactor: C₂H4(g) +0.50₂ (g)-CH₂OCH₂(g). The reactor is operated at 6 atm and 260 °C. The feed is a stoichiometric mixture of ethylene and oxygen. You may assume the reaction is elementary. Set up the stoichiometric table and express -r as a function of partial pressures. Express the partial pressures and as a function of conversion for fluidized batch reactor and for a PBR (PFR like). Write-r as a function of the rate constant and conversion only.
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