4. The irreversible gas-phase non-elementary reaction A +2B C is to be carried out isothermally in a constant pressure batch reactor. The feed is at a temperature of 227°C, a pressure of 1013 kPa, and its composition is 33.3% A and 66.7% B. Laboratory data taken under identical conditions are as follows: -rA (mol/dm3.s)x 103 0.010 0.005 0.002 0.001 XA 0.0 0.2 0.4 0.6 a) Find the volume of a plug-flow reactor required to achieve 30% conversion of A for an entering volumetric flow rate of 2m3/min. b) Find the volume of a CSTR required to take the effluent from the plug-flow reactor (PFR) above and achieve 50% total conversion.
4. The irreversible gas-phase non-elementary reaction A +2B C is to be carried out isothermally in a constant pressure batch reactor. The feed is at a temperature of 227°C, a pressure of 1013 kPa, and its composition is 33.3% A and 66.7% B. Laboratory data taken under identical conditions are as follows: -rA (mol/dm3.s)x 103 0.010 0.005 0.002 0.001 XA 0.0 0.2 0.4 0.6 a) Find the volume of a plug-flow reactor required to achieve 30% conversion of A for an entering volumetric flow rate of 2m3/min. b) Find the volume of a CSTR required to take the effluent from the plug-flow reactor (PFR) above and achieve 50% total conversion.
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:d) WhấT Is ldedl ConDmlunon
4. The irreversible gas-phase non-elementary reaction
A + 2B C
is to be carried out isothermally in a constant pressure batch reactor. The feed is at a
temperature of 227°C, a pressure of 1013 kPa, and its composition is 33.3% A and 66.7% B.
Laboratory data taken under identical conditions are as follows:
-rA (mol/dm3.s) x 103 0.010 0.005 0.002 0.001
0.6
ХА
0.0
0.2
0.4
a) Find the volume of a plug-flow reactor required to achieve 30% conversion of A for an
entering volumetric flow rate of 2m3/min.
b) Find the volume of a CSTR required to take the effluent from the plug-flow reactor
(PFR) above and achieve 50% total conversion.
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