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A product code-named ‘Brookdale’ is produced via isothermal and non-elementary reaction. The data for this reaction is provided in Table 1. CAo/-rA Conversion. XA 10 0.0 15 0.1 40 0.2 50 0.3 40 0.4 25 0.5 15 0.6 10 0.7 15 0.8 30 0.9 40 1.0 The production company plans to reduce cost by minimizing the reactor size. As a process engineer, design of arrangement that consists of CSTR and PFR. Assume that the volumetric flow rate is constant in both reactors (v0 =1 L/min) and the required conversion (X2) from the second reactor is 70%. By using Levenspiel plot, suggest which arrangement is suitable to give minimum total reactor volume and determine conversion (X1) that exit the first reactor. Justify based on the plot

A product code-named ‘Brookdale’ is produced via isothermal and non-elementary reaction. The data for this reaction is provided in Table 1. CAo/-rA Conversion. XA 10 0.0 15 0.1 40 0.2 50 0.3 40 0.4 25 0.5 15 0.6 10 0.7 15 0.8 30 0.9 40 1.0 The production company plans to reduce cost by minimizing the reactor size. As a process engineer, design of arrangement that consists of CSTR and PFR. Assume that the volumetric flow rate is constant in both reactors (v0 =1 L/min) and the required conversion (X2) from the second reactor is 70%. By using Levenspiel plot, suggest which arrangement is suitable to give minimum total reactor volume and determine conversion (X1) that exit the first reactor. Justify based on the plot

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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A product code-named ‘Brookdale’ is produced via isothermal and non-elementary reaction. The data for this reaction is provided in Table 1.

CAo/-rA

Conversion. XA

10

0.0

15

0.1

40

0.2

50

0.3

40

0.4

25

0.5

15

0.6

10

0.7

15

0.8

30

0.9

40

1.0

The production company plans to reduce cost by minimizing the reactor size. As a process engineer, design of arrangement that consists of CSTR and PFR. Assume that the volumetric flow rate is constant in both reactors (v0 =1 L/min) and the required conversion (X2) from the second reactor is 70%. By using Levenspiel plot, suggest which arrangement is suitable to give minimum total reactor volume and determine conversion (X1) that exit the first reactor. Justify based on the plot.

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