The exothermic reaction of stillbene (A) to form the economically important trospophene (B) and methane (C), i.e., A B+C was carried out adiabatically and the following data recorded: X 0 0.2 0.4 0.45 0.5 0.6 0.8 0.9 -A (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. (a) What are the PFR and CSTR-volumes necessary to achieve 40% conversion? (VPFR VCSTR = 24 dm³) = 72 dm³. (b) Over what range of conversions would the CSTR and PFR reactor volumes be identical? (c) What is the maximum conversion that can be achieved in a 105-dm³ CSTR?
The exothermic reaction of stillbene (A) to form the economically important trospophene (B) and methane (C), i.e., A B+C was carried out adiabatically and the following data recorded: X 0 0.2 0.4 0.45 0.5 0.6 0.8 0.9 -A (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. (a) What are the PFR and CSTR-volumes necessary to achieve 40% conversion? (VPFR VCSTR = 24 dm³) = 72 dm³. (b) Over what range of conversions would the CSTR and PFR reactor volumes be identical? (c) What is the maximum conversion that can be achieved in a 105-dm³ CSTR?
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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