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(D) For two PFRs in series where each PFR is 1.6 m^3, determine the conversion after each reactor.

(D) For two PFRs in series where each PFR is 1.6 m^3, determine the conversion after each reactor.

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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(D) For two PFRs in series where each PFR is 1.6 m^3, determine the conversion after each reactor.
Transcribed Image Text:(D) For two PFRs in series where each PFR is 1.6 m^3, determine the conversion after each reactor.
XA 0.0 mol -TA ³-sec 1 (m³-sec) -TA mol FAO (m³-sec -TA mol 0.49 0.1 0.41 0.2 0.34 0.4 0.199 Reaction A → B 0.6 0.117 mol sec PureA T = 500K & P = 830 kPa (8.2 atm) Feed Flow Rate = 0.8 0.7 0.083 0.8 0.054
Transcribed Image Text:XA 0.0 mol -TA ³-sec 1 (m³-sec) -TA mol FAO (m³-sec -TA mol 0.49 0.1 0.41 0.2 0.34 0.4 0.199 Reaction A → B 0.6 0.117 mol sec PureA T = 500K & P = 830 kPa (8.2 atm) Feed Flow Rate = 0.8 0.7 0.083 0.8 0.054
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