Consider a gas-phase reaction 2A→R + 2S with unknown kinetics. If a space velocity of 1/min is needed for 90% conversion of A in a plug flow reactor, find the corresponding space-time and mean residence time or holding time of fluid in the plug flow 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
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5.1. Consider a gas-phase reaction 2A→R + 2S with unknown kinetics. If a
space velocity of 1/min is needed for 90% conversion of A in a plug flow
reactor, find the corresponding space-time and mean residence time or
holding time of fluid in the plug flow reactor.
5.3. A stream of aqueous monomer A (1 mol/liter, 4 liter/min) enters a 2-liter
mixed flow reactor, is radiated therein, and polymerizes as follows:
A
T...
In the exit stream CA = 0.01 mol/liter, and for a particular reaction product
W, Cw = 0.0002 mol/liter. Find the rate of reaction of A and the rate of
formation of W.
Transcribed Image Text:5.1. Consider a gas-phase reaction 2A→R + 2S with unknown kinetics. If a space velocity of 1/min is needed for 90% conversion of A in a plug flow reactor, find the corresponding space-time and mean residence time or holding time of fluid in the plug flow reactor. 5.3. A stream of aqueous monomer A (1 mol/liter, 4 liter/min) enters a 2-liter mixed flow reactor, is radiated therein, and polymerizes as follows: A T... In the exit stream CA = 0.01 mol/liter, and for a particular reaction product W, Cw = 0.0002 mol/liter. Find the rate of reaction of A and the rate of formation of W.
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