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2) The irreversible liquid phase reaction AB is to be carried out isother rate is 100 mol/min of A. The rate of the reaction was measured as a functio results are given below.

2) The irreversible liquid phase reaction AB is to be carried out isother rate is 100 mol/min of A. The rate of the reaction was measured as a functio results are given below.

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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2) The irreversible liquid phase reaction AB is to be carried out isothermally. The entering flow rate is 100 mol/min of A. The rate of the reaction was measured as a function of conversion and the results are given below. -TA (mol/min.L) 4.55 5.26 3.57 2.13 2.04 3.03 5.00 5.56 2.50 1.25 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 X 0 0.1 a) Supposing that you have a 12 L CSTR followed by a 4.5 L PFR, find the conversion that can be achieved using this arrangement? b) Is it possible to increase the conversion by reversing the order of these two reactors? c) What is the volume of single PFR that you would need for the same conversion in part (a)? d) What is the volume of single CSTR that you would need for the same conversion in part (a)?
Transcribed Image Text:2) The irreversible liquid phase reaction AB is to be carried out isothermally. The entering flow rate is 100 mol/min of A. The rate of the reaction was measured as a function of conversion and the results are given below. -TA (mol/min.L) 4.55 5.26 3.57 2.13 2.04 3.03 5.00 5.56 2.50 1.25 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 X 0 0.1 a) Supposing that you have a 12 L CSTR followed by a 4.5 L PFR, find the conversion that can be achieved using this arrangement? b) Is it possible to increase the conversion by reversing the order of these two reactors? c) What is the volume of single PFR that you would need for the same conversion in part (a)? d) What is the volume of single CSTR that you would need for the same conversion in part (a)?
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