a. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates of all species. b. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates of all species if the reaction is carried out in a constant-pressure batch reactor. c. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates of all species if the reaction is carried out in a constant-volume batch reactor.

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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The gas-phase reaction:
A= 3C
is carried out in a flow reactor with no pressure drop. Pure A enters at a temperature of 400 K and
dm
10 atm. At this temperature, Kc = 0.25(
a. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates
of all species.
b. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates
of all species if the reaction is carried out in a constant-pressure batch reactor.
c. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates
of all species if the reaction is carried out in a constant-volume batch reactor.
Transcribed Image Text:The gas-phase reaction: A= 3C is carried out in a flow reactor with no pressure drop. Pure A enters at a temperature of 400 K and dm 10 atm. At this temperature, Kc = 0.25( a. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates of all species. b. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates of all species if the reaction is carried out in a constant-pressure batch reactor. c. Calculate the equilibrium conversion, concentrations of all species, and the reaction rates of all species if the reaction is carried out in a constant-volume batch reactor.
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