The complex rxn is carried out in a batch reactor:   k1= 6 (min)-1, kD= 4 (min)-1, kU= 3 (min)-1, Ca0 (initial conc. of A) =8 mol/L. (i) Find out dCa/dt, dCb/dt, dCd/dt, dCu/dt, (ii) Find out the instaneous yield of B only in terms of Ca and Cb. What is the numerical value of the instaneous yield when Ca=Cb (iii) Find out the overall selectivity of D. (iv) Find out the time when B reaches the highest concentration (Tmax)

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
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The complex rxn is carried out in a batch reactor:

 

k1= 6 (min)-1, kD= 4 (min)-1, kU= 3 (min)-1, Ca0 (initial conc. of A) =8 mol/L.

(i) Find out dCa/dt, dCb/dt, dCd/dt, dCu/dt,

(ii) Find out the instaneous yield of B only in terms of Ca and Cb. What is the numerical value of the instaneous yield when Ca=Cb

(iii) Find out the overall selectivity of D.

(iv) Find out the time when B reaches the highest concentration (Tmax)

kp „D
k1
A-^-B
А
ku •U
Transcribed Image Text:kp „D k1 A-^-B А ku •U
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