he second-order liquid phase reaction C 6H 5COCH2Br + C6H5N⎯⎯→C6H5COCH2NC5H5Br is carried out in a batch reactor at 35°C. The specific reaction-rate constant is 0.0445 dm3/mol/min.Reactor 1 is charged with 1,000 dm3, where the concentration of each reactant after mixing is 2M. Now, consider the case when, after filling reactor 1, the drain at the bottom of the reactor is left open and it drains into reactor 2, mounted below it, at a volumtetric rate of 10 dm^3/min. i) what is the conversion and concentration of each species in reactor 2 that is filling up with the liquid feom reactor 1 after 10 and after 50 minutes? ii) at the end of 50 minutes, the contents of the two reactors are added together. What is the overall conversion after mixing?
he second-order liquid phase reaction C 6H 5COCH2Br + C6H5N⎯⎯→C6H5COCH2NC5H5Br is carried out in a batch reactor at 35°C. The specific reaction-rate constant is 0.0445 dm3/mol/min.Reactor 1 is charged with 1,000 dm3, where the concentration of each reactant after mixing is 2M. Now, consider the case when, after filling reactor 1, the drain at the bottom of the reactor is left open and it drains into reactor 2, mounted below it, at a volumtetric rate of 10 dm^3/min. i) what is the conversion and concentration of each species in reactor 2 that is filling up with the liquid feom reactor 1 after 10 and after 50 minutes? ii) at the end of 50 minutes, the contents of the two reactors are added together. What is the overall conversion after mixing?
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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The second-order liquid phase reaction
C 6H 5COCH2Br + C6H5N⎯⎯→C6H5COCH2NC5H5Br
is carried out in a batch reactor at 35°C. The specific reaction-rate constant is 0.0445 dm3/mol/min.Reactor 1 is charged with 1,000 dm3, where the concentration of each reactant after mixing is 2M.
Now, consider the case when, after filling reactor 1, the drain at the bottom of the reactor is left open and it drains into reactor 2, mounted below it, at a volumtetric rate of 10 dm^3/min.
i) what is the conversion and concentration of each species in reactor 2 that is filling up with the liquid feom reactor 1 after 10 and after 50 minutes?
ii) at the end of 50 minutes, the contents of the two reactors are added together. What is the overall conversion after mixing?
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