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Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume of 100 dm³.

Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume of 100 dm³.

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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I. The exothermic reaction of stillbene (A) to form the economically important trospophene (B) and methane (C), that is, A > B+ C was carried out adiabatically and the following data recorded: X 0.2 0.4 0.45 0.5 0.6 0.8 0.9 -TA (mol/dm³-min) 1.0 1.67 5.0 5.0 5.0 5.0 1.25 0.91 The entering molar flow rate of A was 300 mol/min. Plot the conversion and rate of reaction as a function of PER reactor volume up to a volume of 100 dm³.
Transcribed Image Text:I. The exothermic reaction of stillbene (A) to form the economically important trospophene (B) and methane (C), that is, A > B+ C was carried out adiabatically and the following data recorded: X 0.2 0.4 0.45 0.5 0.6 0.8 0.9 -TA (mol/dm³-min) 1.0 1.67 5.0 5.0 5.0 5.0 1.25 0.91 The entering molar flow rate of A was 300 mol/min. Plot the conversion and rate of reaction as a function of PER reactor volume up to a volume of 100 dm³.
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