2. Given the elementary liquid phase reaction A + B → C with k₁ = 0.35 L/mol·h. a. Calculate the conversion of species A after 4 h in a batch reactor if CA0 = CB0 = 5 M. b. Calculate the volume of a CSTR necessary to reach 95% conversion of species A if the feed is equimolar in A and B with CA0 = 6 mol/L and vo = 1 L/h. c. Repeat part b for a PFR.
2. Given the elementary liquid phase reaction A + B → C with k₁ = 0.35 L/mol·h. a. Calculate the conversion of species A after 4 h in a batch reactor if CA0 = CB0 = 5 M. b. Calculate the volume of a CSTR necessary to reach 95% conversion of species A if the feed is equimolar in A and B with CA0 = 6 mol/L and vo = 1 L/h. c. Repeat part b for a PFR.
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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Transcribed Image Text:2. Given the elementary liquid phase reaction A + B → C with k₁ = 0.35 L/mol·h.
a. Calculate the conversion of species A after 4 h in a batch reactor if CA0 = CB0 = 5 M.
b. Calculate the volume of a CSTR necessary to reach 95% conversion of species A if the
feed is equimolar in A and B with CA0 = 6 mol/L and vo = 1 L/h.
c. Repeat part b for a PFR.
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