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A liquid phase reaction is to be caried out using a combination of the two reactors in series. The first reactor is expected to have Xi = 0.3 and the second reactor will further convert the reactant, so that X2 = 0.8. Both reactors operate under isothermal conditions. The data for this reaction can be found in Table 1. The molar flow rate at feed (FA0) to first reactor is 52 mol/min. FA0, Xo X,=0.3 X,=0.8 Figurel: Reactor configuration for a liquid phase reaction а. Calculate the volume for first reactor for the configuration shown in Figure 1. b. Determine the total reactor volume using simil ar reactor configuration. C. If the arrangement of the reactor is changed, what is the total volume for both reactors? Give your comment on based on your answer. Table 1: Raw data -TA (mol/dm3-s) 0.0053 0.0 0.1 0.0052 0.2 0.0050 0.3 0.4 0.0045 0.0040 0.5 0.6 0.0033 0.0025 0.7 0.0018 0.8 0.00125 0.85 0.001

A liquid phase reaction is to be caried out using a combination of the two reactors in series. The first reactor is expected to have Xi = 0.3 and the second reactor will further convert the reactant, so that X2 = 0.8. Both reactors operate under isothermal conditions. The data for this reaction can be found in Table 1. The molar flow rate at feed (FA0) to first reactor is 52 mol/min. FA0, Xo X,=0.3 X,=0.8 Figurel: Reactor configuration for a liquid phase reaction а. Calculate the volume for first reactor for the configuration shown in Figure 1. b. Determine the total reactor volume using simil ar reactor configuration. C. If the arrangement of the reactor is changed, what is the total volume for both reactors? Give your comment on based on your answer. Table 1: Raw data -TA (mol/dm3-s) 0.0053 0.0 0.1 0.0052 0.2 0.0050 0.3 0.4 0.0045 0.0040 0.5 0.6 0.0033 0.0025 0.7 0.0018 0.8 0.00125 0.85 0.001

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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A liquid phase reaction is to be carried out using a combination of the two reactors in series. The first reactor is expected to have X1 = 0.3 and the second reactor will further convert the reactant, so that X2 = 0.8. Both reactors operate under isothermal conditions. The data for this reaction can be found in Table 1. The molar flow rate at feed (FA0) to first reactor is 52 mol/min. ww X,=0.3 A0; X, →Xx=0.8 Figurel: Reactor configuration for a liquid phase reaction Calculate the volume for first reactor for the configuration shown in Figure 1. b. а. Determine the total reactor volume using simil ar reactor configuration. If the arrangement of the reactor is changed, what is the total volume for both reactors? Give your comment on based on your answer. C. Table 1: Raw data -TA (mol/dm3-s) 0.0053 0.0 0.1 0.0052 0.2 0.0050 0.3 0.0045 0.4 0.0040 0.5 0.0033 0.6 0.0025 0.7 0.0018 0.8 0.00125 0.85 0.001
Transcribed Image Text:A liquid phase reaction is to be carried out using a combination of the two reactors in series. The first reactor is expected to have X1 = 0.3 and the second reactor will further convert the reactant, so that X2 = 0.8. Both reactors operate under isothermal conditions. The data for this reaction can be found in Table 1. The molar flow rate at feed (FA0) to first reactor is 52 mol/min. ww X,=0.3 A0; X, →Xx=0.8 Figurel: Reactor configuration for a liquid phase reaction Calculate the volume for first reactor for the configuration shown in Figure 1. b. а. Determine the total reactor volume using simil ar reactor configuration. If the arrangement of the reactor is changed, what is the total volume for both reactors? Give your comment on based on your answer. C. Table 1: Raw data -TA (mol/dm3-s) 0.0053 0.0 0.1 0.0052 0.2 0.0050 0.3 0.0045 0.4 0.0040 0.5 0.0033 0.6 0.0025 0.7 0.0018 0.8 0.00125 0.85 0.001
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