(c) product and two undesired products. Selectivity and conversion are crucial in order to optimize the formation of desired products and it can be achieved by choosing the right reactor scheme and reaction system. The reaction scheme can be written as: Trambouze reaction is composed of three parallel reactions that produced one desired -riA = rx = k1 = 0.0001 ớ/dm³ • s k2 A B -r2A = rB = K2CA = (0.0015s¬1)CA k3 AY -T34 = ry = k3CZ = (0.008 dm³ /mol·s)Cỉ CSTR was selected for this reaction in order to achieve maximum selectivity. The entrance concentration of A, CAO was 0.2 mol/dm3 and the volumetric flowrate was 2 dm/s. The selectivity value and conversion obtained were 0.84 and 0.72, respectively. If the volumetric flowrate varies in the range of 1 to 8 dm/s, briefly discuss the outcomes of the reaction i.e reactor volume, conversion, selectivity etc. The results are shown in Figure 1. 2000 1.0 Selectivity, S, E) 0.8 1500 - 0.6 1000 - Conversion, X, H 040 500 Concentration of A. C Imolidm) 0.2 00 8 Volumetric flow rate, u̟ [ [dm³/s] Figure 1 Change of volume by varying volumetric flowrate in a CSTR system K; C SY (up) a 'eunjo
(c) product and two undesired products. Selectivity and conversion are crucial in order to optimize the formation of desired products and it can be achieved by choosing the right reactor scheme and reaction system. The reaction scheme can be written as: Trambouze reaction is composed of three parallel reactions that produced one desired -riA = rx = k1 = 0.0001 ớ/dm³ • s k2 A B -r2A = rB = K2CA = (0.0015s¬1)CA k3 AY -T34 = ry = k3CZ = (0.008 dm³ /mol·s)Cỉ CSTR was selected for this reaction in order to achieve maximum selectivity. The entrance concentration of A, CAO was 0.2 mol/dm3 and the volumetric flowrate was 2 dm/s. The selectivity value and conversion obtained were 0.84 and 0.72, respectively. If the volumetric flowrate varies in the range of 1 to 8 dm/s, briefly discuss the outcomes of the reaction i.e reactor volume, conversion, selectivity etc. The results are shown in Figure 1. 2000 1.0 Selectivity, S, E) 0.8 1500 - 0.6 1000 - Conversion, X, H 040 500 Concentration of A. C Imolidm) 0.2 00 8 Volumetric flow rate, u̟ [ [dm³/s] Figure 1 Change of volume by varying volumetric flowrate in a CSTR system K; C SY (up) a 'eunjo
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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Question
![(c)
product and two undesired products. Selectivity and conversion are crucial in order to optimize
the formation of desired products and it can be achieved by choosing the right reactor scheme
and reaction system. The reaction scheme can be written as:
Trambouze reaction is composed of three parallel reactions that produced one desired
k1
A→X
-rA = rx = k1 = 0.0001mot/dm3 · s
k2
В
A
-r2A = TB = k2Ca = (0.0015s¬1)Ca
-T34 = ry = k3C = (0.008 dm°/mol·sC;
AY
CSTR was selected for this reaction in order to achieve maximum selectivity. The entrance
concentration of A, CAo Was 0.2 mol/dm3 and the volumetric flowrate was 2 dm³/s. The
selectivity value and conversion obtained were 0.84 and 0.72, respectively. If the volumetric
flowrate varies in the range of 1 to 8 dm³/s, briefly discuss the outcomes of the reaction i.e
reactor volume, conversion, selectivity etc. The results are shown in Figure 1.
2000
1.0
Selectivity, S, l)
0.8
1500 -
-0.6
1000 -
Conversion, X, []
040
500-
Concentration of A. C [molidm)
-0.2
-0.0
6
8
Volumetric flow rate, u_[ [dm³/s]
Figure 1 Change of volume by varying volumetric flowrate in a CSTR system
up) A 'aunjon](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F71b18f0c-7823-46e1-9451-7a45df815682%2F7d12e460-07cb-4c50-81f9-00704c2fff79%2Fsdi4l2q_processed.jpeg&w=3840&q=75)
Transcribed Image Text:(c)
product and two undesired products. Selectivity and conversion are crucial in order to optimize
the formation of desired products and it can be achieved by choosing the right reactor scheme
and reaction system. The reaction scheme can be written as:
Trambouze reaction is composed of three parallel reactions that produced one desired
k1
A→X
-rA = rx = k1 = 0.0001mot/dm3 · s
k2
В
A
-r2A = TB = k2Ca = (0.0015s¬1)Ca
-T34 = ry = k3C = (0.008 dm°/mol·sC;
AY
CSTR was selected for this reaction in order to achieve maximum selectivity. The entrance
concentration of A, CAo Was 0.2 mol/dm3 and the volumetric flowrate was 2 dm³/s. The
selectivity value and conversion obtained were 0.84 and 0.72, respectively. If the volumetric
flowrate varies in the range of 1 to 8 dm³/s, briefly discuss the outcomes of the reaction i.e
reactor volume, conversion, selectivity etc. The results are shown in Figure 1.
2000
1.0
Selectivity, S, l)
0.8
1500 -
-0.6
1000 -
Conversion, X, []
040
500-
Concentration of A. C [molidm)
-0.2
-0.0
6
8
Volumetric flow rate, u_[ [dm³/s]
Figure 1 Change of volume by varying volumetric flowrate in a CSTR system
up) A 'aunjon
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