The irreversible, first-order, liquid phase reactions AR S are currently carried out in two CSTRS in series. The desired product is R. Two streams are fed to the first reactor. One is a solution of A at a volumetric flow rate of 50 gal/min. The concentration of A in this stream is 3 Ibmol/gal. The second stream is pure solvent at a flow rate of 100 gal'min. There is no Ror S in either streams. Both reactors operate at 200°C; at this temperature k, - 0.3 min, kz 0.3 min-1. The volume of the first reactor is 500 gal and the volume of the second reactor is 750 gal. 1. What are the concentrations of A, R, and S in the effluent from the first reactor? 2. What are the concentrations of A, R, and S in the effluent from the second reactor? 3. Calculate the overall selectivity and overall yield at the exit of each reactor. 4. What can you conclude?

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
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Chapter1: Introduction
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The irreversible, first-order, liquid phase reactions
AR S
are currently carried out in two CSTRS in series. The desired product is R. Two streams are fed to the
first reactor. One is a solution of A at a volumetric flow rate of 50 gal/min. The concentration of A in
this stream is 3 Ibmol/gal. The second stream is pure solvent at a flow rate of 100 gal/min. There is
no R or S in either streams. Both reactors operate at 200°C; at this temperature k, = 0.3 min-1, k =
0.3 min-1. The volume of the first reactor is 500 gal and the volume of the second reactor is 750 gal.
1. What are the concentrations of 4, R, and S in the effluent from the first reactor?
2. What are the concentrations of A, R, and s in the effluent from the second reactor?
3. Calculate the overall selectivity and overall yield at the exit of cach reactor.
4. What can you conclude?
Transcribed Image Text:The irreversible, first-order, liquid phase reactions AR S are currently carried out in two CSTRS in series. The desired product is R. Two streams are fed to the first reactor. One is a solution of A at a volumetric flow rate of 50 gal/min. The concentration of A in this stream is 3 Ibmol/gal. The second stream is pure solvent at a flow rate of 100 gal/min. There is no R or S in either streams. Both reactors operate at 200°C; at this temperature k, = 0.3 min-1, k = 0.3 min-1. The volume of the first reactor is 500 gal and the volume of the second reactor is 750 gal. 1. What are the concentrations of 4, R, and S in the effluent from the first reactor? 2. What are the concentrations of A, R, and s in the effluent from the second reactor? 3. Calculate the overall selectivity and overall yield at the exit of cach reactor. 4. What can you conclude?
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