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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: I. X 0.2 0.4 0.45 0.5 0.6 0.8 0.9 -TA (mol/dm³•min) 1.67 5.0 5.0 5.0 5.0 1.0 1.25 0.91 The entering molar flow rate of A was 300 mol/min.

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: I. X 0.2 0.4 0.45 0.5 0.6 0.8 0.9 -TA (mol/dm³•min) 1.67 5.0 5.0 5.0 5.0 1.0 1.25 0.91 The entering molar flow rate of A was 300 mol/min.

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: 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. What conversion can be achieved if a 72- dm³ PFR is followed in series by a 24- dm3 CSTR? Zoom
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: 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. What conversion can be achieved if a 72- dm³ PFR is followed in series by a 24- dm3 CSTR? Zoom
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