Data from the following table were obtained for the gas phase decomposition of reactant A in a constant volume batch reactor at 100°C fed with pure A. The stoichiometry of the reaction is 2A → R + S. Calculate the size of the plug flow reactor, operating at 100°C and 1 atm, capable of treating 100 moles/h of a feeding that contains 20% inerts to obtain a 95% conversion of A. T(s) PA (atm) 0 1.00 20 0.80 40 0.68 60 0.56 80 0.45 100 0.37 140 0.25 200 0.14 260 0.08 330 0.04 420 0.02
Data from the following table were obtained for the gas phase decomposition of reactant A in a constant volume batch reactor at 100°C fed with pure A. The stoichiometry of the reaction is 2A → R + S. Calculate the size of the plug flow reactor, operating at 100°C and 1 atm, capable of treating 100 moles/h of a feeding that contains 20% inerts to obtain a 95% conversion of A. T(s) PA (atm) 0 1.00 20 0.80 40 0.68 60 0.56 80 0.45 100 0.37 140 0.25 200 0.14 260 0.08 330 0.04 420 0.02
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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Data from the following table were obtained for the gas phase decomposition of reactant A in a constant volume batch reactor at 100°C fed with pure A. The stoichiometry of the reaction is 2A → R + S. Calculate the size of the plug flow reactor, operating at 100°C and 1 atm, capable of treating 100 moles/h of a feeding that contains 20% inerts to obtain a 95% conversion of A.
|
T(s) |
PA (atm) |
|
0 |
1.00 |
|
20 |
0.80 |
|
40 |
0.68 |
|
60 |
0.56 |
|
80 |
0.45 |
|
100 |
0.37 |
|
140 |
0.25 |
|
200 |
0.14 |
|
260 |
0.08 |
|
330 |
0.04 |
|
420 |
0.02 |
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