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(C) What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR?

(C) What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR?

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 can u help me with part C using refereced data 

(C) What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR?
Transcribed Image Text:(C) What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR?
XA RATE FAO/-RA 18000 (A) What are the PFR and CSTR volumes necessary to achieve a 40% for a single reactor process? Perf Eq for CSTR 0 1 Perform Equation of a PFR V FAO Reaction ASTILBENE → BTROSPHOPHENE + CMETHANE FeedFlow Rate = 300. = 0.2 1.67 10778.4 -TA V FAO = XAV= Adiabatic & Exothermic rxA dxA SA (-TA) 0.4 5 3600 mol sec PureA FAO (-TA) 0.45 5 3600 FAO → V = √XA F40 dx 0 -TA VCSTR VPFR ,reference table. = 4320 dm³ = 1440 dm³ 0.5 5 3600 → V = 0.6 5 3600 0.8 0.9 1.25 0.91 14400 19780.2 1 * 0.4 * 14400+ 0.4 * 3600 2
Transcribed Image Text:XA RATE FAO/-RA 18000 (A) What are the PFR and CSTR volumes necessary to achieve a 40% for a single reactor process? Perf Eq for CSTR 0 1 Perform Equation of a PFR V FAO Reaction ASTILBENE → BTROSPHOPHENE + CMETHANE FeedFlow Rate = 300. = 0.2 1.67 10778.4 -TA V FAO = XAV= Adiabatic & Exothermic rxA dxA SA (-TA) 0.4 5 3600 mol sec PureA FAO (-TA) 0.45 5 3600 FAO → V = √XA F40 dx 0 -TA VCSTR VPFR ,reference table. = 4320 dm³ = 1440 dm³ 0.5 5 3600 → V = 0.6 5 3600 0.8 0.9 1.25 0.91 14400 19780.2 1 * 0.4 * 14400+ 0.4 * 3600 2
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