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 F 20 (dm?) = 2000 1000 0 02 04 06 08 Conversion, X 1- Pure (A) is fed at a volumetric flow rate 1000 dm/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 dm3, 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:А — Prodиcts+ Product40003000FAO(dm)200010000.20.40.60.8Conversion, X

Volumetric flow rate = 1000 dm3/hour Concentration = 0.005 lb mol/dm3 Volume of CSTR = 1200 dm3 PFR…

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

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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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 F 20 (dm?) = 2000 1000 0 02 04 06 08 Conversion, X

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