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The elementary, second order, liquid pha se reaction A+B>C+D is conducted in an isothermal plug flow reactor of 1 m capacity. The inlet volumetric flow rate is 10 m/hr and CAo = C30 =2 kmol/m'. At these conditions, conversion of A is 50%. Now, if stirred tank reactor of 2m capacity is installed in series, upstream of the plug flow reactor as shown in below figure, then what conversion can be expected in the new arrangement ofreactors?

The elementary, second order, liquid pha se reaction A+B>C+D is conducted in an isothermal plug flow reactor of 1 m capacity. The inlet volumetric flow rate is 10 m/hr and CAo = C30 =2 kmol/m'. At these conditions, conversion of A is 50%. Now, if stirred tank reactor of 2m capacity is installed in series, upstream of the plug flow reactor as shown in below figure, then what conversion can be expected in the new arrangement ofreactors?

Introduction to Chemical Engineering Thermodynamics
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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Question 5 The elementary, second order, liquid phase reaction A+B C+D is conducted in an isothermal plug flow reactor of 1 m° capacity. The inlet volumetric flow rate is 10 m/hr and CAO = CB0 = 2 kmol/m³. At these conditions, conversion of A is 50%. Now, if stirred tank reactor of 2m' capacity is installed in series, upstream of the plug flow reactor as shown in below figure, then what conversion can be expected in the new arrangement of reactors? CAL CA2 2 m I m Formulae V - r. 40 40
Transcribed Image Text:Question 5 The elementary, second order, liquid phase reaction A+B C+D is conducted in an isothermal plug flow reactor of 1 m° capacity. The inlet volumetric flow rate is 10 m/hr and CAO = CB0 = 2 kmol/m³. At these conditions, conversion of A is 50%. Now, if stirred tank reactor of 2m' capacity is installed in series, upstream of the plug flow reactor as shown in below figure, then what conversion can be expected in the new arrangement of reactors? CAL CA2 2 m I m Formulae V - r. 40 40
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