The gas-phase reaction is to be carried out isothermally first in a flow reactor. The molar feed is 50% H2 and 50% N2, at a pressure of 16.4 atm and at a temperature of 227°C.(b) Express the concentrations in mol/dm3 of each for the reacting species as a function of conversion. Evaluate CA0, and then calculate the concentrations of ammonia and hydrogen when the conversion of H2 is 60%. (c) Suppose by chance the reaction is elementary with = 40 dm3/mol/s. Write the rate of reaction solely as a function of conversion for (1) a flow reactor and for (2) a constant-volume batch reactor.
The gas-phase reaction is to be carried out isothermally first in a flow reactor. The molar feed is 50% H2 and 50% N2, at a pressure of 16.4 atm and at a temperature of 227°C.(b) Express the concentrations in mol/dm3 of each for the reacting species as a function of conversion. Evaluate CA0, and then calculate the concentrations of ammonia and hydrogen when the conversion of H2 is 60%. (c) Suppose by chance the reaction is elementary with = 40 dm3/mol/s. Write the rate of reaction solely as a function of conversion for (1) a flow reactor and for (2) 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 is to be carried out isothermally first in a flow reactor. The molar feed is 50% H2 and 50% N2, at a pressure of 16.4 atm and at a temperature of 227°C.
(b) Express the concentrations in mol/dm3 of each for the reacting species as a function of conversion. Evaluate CA0, and then calculate the concentrations of ammonia and hydrogen when the conversion of H2 is 60%.
(c) Suppose by chance the reaction is elementary with = 40 dm3/mol/s. Write the rate of reaction solely as a function of conversion for (1) a flow reactor and for (2) a constant-volume batch reactor.
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