4- For the irreversible gas phase reaction A— 2B The following correlation was determined from laboratory data. The initial concentration of A is 0.2 gmol/litre. -8 3 o m>.s For X 0.5; =3+10(X —0.5) =14 mol The volumetric flow rate is 5 m¥s. a. Over what range of conversions are the plug-flow reactor and CSTR volumes identical? b. What conversion will be achieved in a CSTR that has a volume of 90 L? c. What plug-flow reactor volume is necessary to achieve 70% conversion? d. What CSTR reactor volume is required if effluent from the plug-flow reactor in part (c) is fed to a CSTR to raise the conversion to 90%? e. If the reaction is carried out in a constant-pressure batch reactor in which pure A is fed to the reactor, what length of time is necessary to achieve 40 % conversion? 4- For the irreversible gas phase reactionA → 2BThe following correlation was determined from laboratory data. The initial concentration of Ais 0.2 gmol/litre.10-8For X < 0.5;-rAm3.s3mol%3D10-8m3.s= 3 + 10(X – 0.5)-TAFor X > 0.5;molThe volumetric flow rate is 5 m/s.a. Over what range of conversions are the plug-flow reactor and CSTR volumes identical?b. What conversion will be achieved in a CSTR that has a volume of 90 L?c. What plug-flow reactor volume is necessary to achieve 70% conversion?d. What CSTR reactor volume is required if effluent from the plug-flow reactor in part (c)is fed to a CSTR to raise the conversion to 90%?e. If the reaction is carried out in a constant-pressure batch reactor in which pure A is fedto the reactor, what length of time is necessary to achieve 40 % conversion?

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Answered: For the irreversible gas phase reaction…

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

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4- For the irreversible gas phase reaction A— 2B The following correlation was determined from laboratory data. The initial concentration of A is 0.2 gmol/litre. -8 3 o m>.s For X 0.5; =3+10(X —0.5) =14 mol The volumetric flow rate is 5 m¥s. a. Over what range of conversions are the plug-flow reactor and CSTR volumes identical? b. What conversion will be achieved in a CSTR that has a volume of 90 L? c. What plug-flow reactor volume is necessary to achieve 70% conversion? d. What CSTR reactor volume is required if effluent from the plug-flow reactor in part (c) is fed to a CSTR to raise the conversion to 90%? e. If the reaction is carried out in a constant-pressure batch reactor in which pure A is fed to the reactor, what length of time is necessary to achieve 40 % conversion?

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