A + B> Ü liquid phase reaction will be carried out in 3L volume CSTR. The feed is at a volumetric flow rate of 0.5 L / min and contains A and B at concentrations of 0.01 mol / L. Since the rate model of the reaction is (- ra) = (200 L / mol.min) CẠCB; %3D a) Find the conversion rate of A. b) Calculate the required PFR volume to achieve the same conversion. c) Find the conversion ratio to be achieved if the reaction is performed at 3 L volume PFR under CSTR operating conditions.
A + B> Ü liquid phase reaction will be carried out in 3L volume CSTR. The feed is at a volumetric flow rate of 0.5 L / min and contains A and B at concentrations of 0.01 mol / L. Since the rate model of the reaction is (- ra) = (200 L / mol.min) CẠCB; %3D a) Find the conversion rate of A. b) Calculate the required PFR volume to achieve the same conversion. c) Find the conversion ratio to be achieved if the reaction is performed at 3 L volume PFR under CSTR operating conditions.
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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A + B> Ü liquid phase reaction will be carried out in 3L
volume CSTR. The feed is at a volumetric flow rate of
0.5 L/ min and contains A and B at concentrations of
0.01 mol / L. Since the rate model of the reaction is (-
ra) = (200 L / mol.min) CẠCB;
a) Find the conversion rate of A.
b) Calculate the required PER volume to achieve the
same conversion.
c) Find the conversion ratio to be achieved if the
reaction is performed at 3 L volume PFR under CSTR
operating conditions.
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