2021 CRÉ homework 1 1. For gas phase reaction A>B is carried out isothermally. We have the following reaction data: X= 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.85 -TA (mol/(dm s))= 0.0053 0.0052 0.005 0.0045 0.004 0.0033 0.0025 0.0018 0.00125 0.001 Plot 1/(-rA) vs. X.

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
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Chapter1: Introduction
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2021 CRÉ homework 1
1. For gas phase reaction A→B is carried out isothermally. We have the following reaction data:
X=
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.85
-TA (mol/(dm³ s))= 0.0053
0.0052
0.005
0.0045 0.004
0.0033 0.0025 0.0018 0.00125 0.001
Plot
1/(-ra) vs. X.
Transcribed Image Text:2021 CRÉ homework 1 1. For gas phase reaction A→B is carried out isothermally. We have the following reaction data: X= 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.85 -TA (mol/(dm³ s))= 0.0053 0.0052 0.005 0.0045 0.004 0.0033 0.0025 0.0018 0.00125 0.001 Plot 1/(-ra) vs. X.
2. Following the first problem. If the inlet volumetric flow rate is 2070 dm/h. The gas mixture contains
50% A and 50% inerts at 10 atm, enters the reactor at 300°F. Consider two CSTRS in series. If a 40%
conversion is achieved in the first reactor, what total reactor volume is required to accomplish an 80%
overall conversion?
3. For the data in problem 1 and 2, consider the series arrangement of a CSTR and a tubular flow reactor as
shoun below If the intermediate conversion Y. is0 7 which reactor scheme (A or R) chould he used to
Transcribed Image Text:2. Following the first problem. If the inlet volumetric flow rate is 2070 dm/h. The gas mixture contains 50% A and 50% inerts at 10 atm, enters the reactor at 300°F. Consider two CSTRS in series. If a 40% conversion is achieved in the first reactor, what total reactor volume is required to accomplish an 80% overall conversion? 3. For the data in problem 1 and 2, consider the series arrangement of a CSTR and a tubular flow reactor as shoun below If the intermediate conversion Y. is0 7 which reactor scheme (A or R) chould he used to
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