A CSTR is being fed a 50 L/min stream containing 0.08 mol/L of reactant A. The reaction proceeds according to 2A → B with -A = k [A]³, with k = 2.5 L²/(mol)2-min. The concentration of A exit- ing the reactor is 0.03 mol/L.

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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10.15 A CSTR is being fed a 50 L/min stream containing 0.08 mol/L of
reactant A. The reaction proceeds according to 2A → B with -A
= k [A]³, with k = 2.5 L²/(mol)2-min. The concentration of A exit-
ing the reactor is 0.03 mol/L.
a. Calculate the volume of the reactor (L).
b. Given that B has a molecular weight of 75, and that the pro-
cess runs 24 hours per day, calculate the production rate of B
(kg/day).
Transcribed Image Text:10.15 A CSTR is being fed a 50 L/min stream containing 0.08 mol/L of reactant A. The reaction proceeds according to 2A → B with -A = k [A]³, with k = 2.5 L²/(mol)2-min. The concentration of A exit- ing the reactor is 0.03 mol/L. a. Calculate the volume of the reactor (L). b. Given that B has a molecular weight of 75, and that the pro- cess runs 24 hours per day, calculate the production rate of B (kg/day).
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