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Continuously Stirred Tank Reactor.

Continuously Stirred Tank Reactor.

Introduction to Chemical Engineering Thermodynamics
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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Topic: Fluidized Continuously Stirred Tank Reactor

A homogeneous gas phase rxn A + B → C was conducted in a fluidized bed Continuously Stirred Tank Reactor. The rxn is an elementary and reactant A and B are 1st order. Equimolar feed was utilized in CSTR given that the initial volumetric flow rate (Vo) = 100 liters/minute, initial pressure (Po) = 3 atmosphere, Tempt = 227 degC, and k = 0.15- The CSTR is isothermal and isobaric operated. Also, the system acts like an ideal gas. Determine the weight of the catalyst needed in order to achieve XA = 0.90 (conversion of A). moles kilogram catalyst-minute-atm² 2.
Transcribed Image Text:A homogeneous gas phase rxn A + B → C was conducted in a fluidized bed Continuously Stirred Tank Reactor. The rxn is an elementary and reactant A and B are 1st order. Equimolar feed was utilized in CSTR given that the initial volumetric flow rate (Vo) = 100 liters/minute, initial pressure (Po) = 3 atmosphere, Tempt = 227 degC, and k = 0.15- The CSTR is isothermal and isobaric operated. Also, the system acts like an ideal gas. Determine the weight of the catalyst needed in order to achieve XA = 0.90 (conversion of A). moles kilogram catalyst-minute-atm² 2.
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