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A) Determine the reactor volumes in dm³, of a CSTR with a conversion X₁ = followed by a PFR that reaches conversion X₂ = 65% at the end of the two reactor process. = 20%

A) Determine the reactor volumes in dm³, of a CSTR with a conversion X₁ = followed by a PFR that reaches conversion X₂ = 65% at the end of the two reactor process. = 20%

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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An exothermic reaction of reactant (A) forms the economically important product (B) and sellable by- product (C),: A-→ B+C Which was carried out isothermally and the following data was recorded: XA | O mol -TA dm3-min/ 1.2 (dm³-min) mol -TA FAQ (dm³) -TA 0.83 333.33 mol min 0.1 1.8 0.56 222.22 0.2 1.8 0.56 0.3 3 0.33 0.5 3 = 20% 0.33 0.65 1.2 0.83 222.22 133.33 133.33 333.33 feed flow rate = 100. pure A A) Determine the reactor volumes in dm³, of a CSTR with a conversion X₁ followed by a PFR that reaches conversion X₂ 65% at the end of the two reactor process. 1 0.8 0.75 1.33 533.33 0.95 0.5464 1.83 732.06
Transcribed Image Text:An exothermic reaction of reactant (A) forms the economically important product (B) and sellable by- product (C),: A-→ B+C Which was carried out isothermally and the following data was recorded: XA | O mol -TA dm3-min/ 1.2 (dm³-min) mol -TA FAQ (dm³) -TA 0.83 333.33 mol min 0.1 1.8 0.56 222.22 0.2 1.8 0.56 0.3 3 0.33 0.5 3 = 20% 0.33 0.65 1.2 0.83 222.22 133.33 133.33 333.33 feed flow rate = 100. pure A A) Determine the reactor volumes in dm³, of a CSTR with a conversion X₁ followed by a PFR that reaches conversion X₂ 65% at the end of the two reactor process. 1 0.8 0.75 1.33 533.33 0.95 0.5464 1.83 732.06
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