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1.The following non-elenentary liquid phase reaction A Products 0.5 has the kinetics of 一TA 0.45+ k, CA where : reaction rate of A (kmol/m³.s) CA k, and k2 : concentration of A (kmol/m3) : reaction rate constants for the steps when the reaction is occuring. This reaction is carried out in a CSTR at constant temperature. Assuming steady state operation of the reactor; a) Construct the model of the process, b) Calculate the conversion at the exit of the reactor using the suitable method. DATA: Vo = 0.25 m /s CA.0 = 0.4 kmol/ms Inlet flowrate, Inlet concentration of A, Volumeof the reactor, V = 0.5 m3 Rate constants, k: = 0.2 s k2 = 0.05 ms/kmol

1.The following non-elenentary liquid phase reaction A Products 0.5 has the kinetics of 一TA 0.45+ k, CA where : reaction rate of A (kmol/m³.s) CA k, and k2 : concentration of A (kmol/m3) : reaction rate constants for the steps when the reaction is occuring. This reaction is carried out in a CSTR at constant temperature. Assuming steady state operation of the reactor; a) Construct the model of the process, b) Calculate the conversion at the exit of the reactor using the suitable method. DATA: Vo = 0.25 m /s CA.0 = 0.4 kmol/ms Inlet flowrate, Inlet concentration of A, Volumeof the reactor, V = 0.5 m3 Rate constants, k: = 0.2 s k2 = 0.05 ms/kmol

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
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1.The following non-elementary liquid phase reaction A Products 0.5 k,c5 has the kinetics of TA 0.45+ k, CA where TA : reaction rate of A (kmol/m³.s) CA : concentration of A (kmol/m²) k, and k2 : reaction rate constants for the steps when the reaction is occuring. This reaction is carried out in a CSTR at constant temperature. Assuming steady state operation of the reactor; a) Construct the model of the process, b) Calculate the conversion at the exit of the reactor using the suitable method. DATA: Inlet flowrate, Vo = 0.25 m/s CA.O 0.4 kmol/m3 Inlet concentration ofA, V = 0.5 m2 Volumeof the reactor, k. = 0.2 s- Rate constants, ka = 0.05 m/kmol
Transcribed Image Text:1.The following non-elementary liquid phase reaction A Products 0.5 k,c5 has the kinetics of TA 0.45+ k, CA where TA : reaction rate of A (kmol/m³.s) CA : concentration of A (kmol/m²) k, and k2 : reaction rate constants for the steps when the reaction is occuring. This reaction is carried out in a CSTR at constant temperature. Assuming steady state operation of the reactor; a) Construct the model of the process, b) Calculate the conversion at the exit of the reactor using the suitable method. DATA: Inlet flowrate, Vo = 0.25 m/s CA.O 0.4 kmol/m3 Inlet concentration ofA, V = 0.5 m2 Volumeof the reactor, k. = 0.2 s- Rate constants, ka = 0.05 m/kmol
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