Using a constant temperature and ideal continuously stirred tank reactor, a reversible rxn is done which is given below. The data for the kinetic constants for this rxn are k₁=0.5/minute and k-₁-0.075L/mole-minutes, respectively. This is an elementary rxn and the feed has pure reactant A which has a concentration of 2 moles/liter. Determine the equilibrium conversion as well as equilibrium concentration of A and B.
Using a constant temperature and ideal continuously stirred tank reactor, a reversible rxn is done which is given below. The data for the kinetic constants for this rxn are k₁=0.5/minute and k-₁-0.075L/mole-minutes, respectively. This is an elementary rxn and the feed has pure reactant A which has a concentration of 2 moles/liter. Determine the equilibrium conversion as well as equilibrium concentration of A and B.
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:Using a constant temperature and ideal continuously stirred tank reactor, a
reversible rxn is done which is given below. The data for the kinetic constants
for this rxn are k₁=0.5/minute and k-₁-0.075L/mole-minutes, respectively.
This is an elementary rxn and the feed has pure reactant A which has a
concentration of 2 moles/liter. Determine the equilibrium conversion as well
as equilibrium concentration of A and B.
Transcribed Image Text:A(g) = 2B (g)
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