1- Pure (A) is fed at a volumetric flow rate 1000 dm*h and at a concentration of 0.005 Ibmol/dm’ to an existing CSTR, which is connected in series to an existing tubular reactor. If the volume of the CSTR is 1200 dm® and the tubular reactor volume is 600 dm?, what are the intermediate and final conversion that can be achieve with the existing system? The reciprocal rate is plotted as a function of conversion for the conditions at which the reaction is to be carried: A — Products A —— Product 4000 3000 Fao A (dm?) 1000 0 02 04 06 08 Conversion, X 1- Pure (A) is fed at a volumetric flow rate 1000 dm³/h and at a concentration of 0.005Ibmol/dm' to an existing CSTR, which is connected in series to an existing tubular reactor.If the volume of the CSTR is 1200 dm and the tubular reactor volume is 600 dm, whatare the intermediate and final conversion that can be achieve with the existing system?The reciprocal rate is plotted as a function of conversion for the conditions at which thereaction is to be carried:A → ProductsProduct40003000EFA(dm)TA200010000.20.40.60.8Conversion, X

V = 1000 dm3/hr Cao = 0.005 lb.mol/dm3

Answered: re (A) is fed at a volumetric flow rate…

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

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1- Pure (A) is fed at a volumetric flow rate 1000 dm*h and at a concentration of 0.005 Ibmol/dm’ to an existing CSTR, which is connected in series to an existing tubular reactor. If the volume of the CSTR is 1200 dm® and the tubular reactor volume is 600 dm?, what are the intermediate and final conversion that can be achieve with the existing system? The reciprocal rate is plotted as a function of conversion for the conditions at which the reaction is to be carried: A — Products A —— Product 4000 3000 Fao A (dm?) 1000 0 02 04 06 08 Conversion, X

1- Pure (A) is fed at a volumetric flow rate 1000 dm³/h and at a concentration of 0.005
Ibmol/dm' to an existing CSTR, which is connected in series to an existing tubular reactor.
If the volume of the CSTR is 1200 dm and the tubular reactor volume is 600 dm, what
are the intermediate and final conversion that can be achieve with the existing system?
The reciprocal rate is plotted as a function of conversion for the conditions at which the
reaction is to be carried:
A → Products
Product
4000
3000
E
FA
(dm)
TA
2000
1000
0.2
0.4
0.6
0.8
Conversion, X

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