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A reaction and separator, are configured as shown in the diagram, to produce pure streams of component B and C from A. The plant conversion of A is 86%, while the reactor conversion is 28%. The fresh feed, stream 1, is composed of 88 mol% component A and the balance an inert substance, I. Other information is shown in the diagram: LAplant Purge n1 100 LAreactor- Reactor Separator Pure C A8. 20 Pure B Taking 100 mol/s of fresh feed as a basis, determine the following: a) n_4 the product C in mol/s b) n_8 the product B, in mol/s c) n_7 the purge in mol/s d) y A_7 the concentration of A in the purge in mol% e) nA_2, the mols/s of A in the reactor feed f) nA6, the mol/s of A in the recycle g) n_6, the flow of the recycle in mol/s h) n_2, the reactor feed in mol/s i) y A2, concentration of A in the reactor feed, in mol% i)n_3 the reactor effluent in mol/s

A reaction and separator, are configured as shown in the diagram, to produce pure streams of component B and C from A. The plant conversion of A is 86%, while the reactor conversion is 28%. The fresh feed, stream 1, is composed of 88 mol% component A and the balance an inert substance, I. Other information is shown in the diagram: LAplant Purge n1 100 LAreactor- Reactor Separator Pure C A8. 20 Pure B Taking 100 mol/s of fresh feed as a basis, determine the following: a) n_4 the product C in mol/s b) n_8 the product B, in mol/s c) n_7 the purge in mol/s d) y A_7 the concentration of A in the purge in mol% e) nA_2, the mols/s of A in the reactor feed f) nA6, the mol/s of A in the recycle g) n_6, the flow of the recycle in mol/s h) n_2, the reactor feed in mol/s i) y A2, concentration of A in the reactor feed, in mol% i)n_3 the reactor effluent in mol/s

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
Problem 1.1P
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a) 151.36

b) 75.68

c) 24.32

d)50.66

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A reaction and separator, are configured as shown in the diagram, to produce pure streams of component B and C from A. The plant conversion of A is 86%, while the reactor conversion is 28%. The fresh feed, stream 1, is composed of 88 mol% component A and the balance an inert substance, I. Other information is shown in the diagram: LAplant- y_C_6 = y_B_6 = 0 Purge n_1= 100 y_L1 3 Reactor Separator Pure C A 8• 20 Pure B Taking 100 mol/s of fresh feed as a basis, determine the following: a) n_4 the product C in mol/s b) n_8 the product B, in mol/s c) n_7 the purge in mol/s d) y_A7 the concentration of A in the purge in mol% e) n_A_2, the mols/s of A in the reactor feed f) n_A_6, the mol/s of A in the recycle g) n_6, the flow of the recycle in mol/s h) n_2, the reactor feed in mol/s i) y_A_2, concentration of A in the reactor feed, in mol% j) n_3 the reactor effluent in mol/s
Transcribed Image Text:A reaction and separator, are configured as shown in the diagram, to produce pure streams of component B and C from A. The plant conversion of A is 86%, while the reactor conversion is 28%. The fresh feed, stream 1, is composed of 88 mol% component A and the balance an inert substance, I. Other information is shown in the diagram: LAplant- y_C_6 = y_B_6 = 0 Purge n_1= 100 y_L1 3 Reactor Separator Pure C A 8• 20 Pure B Taking 100 mol/s of fresh feed as a basis, determine the following: a) n_4 the product C in mol/s b) n_8 the product B, in mol/s c) n_7 the purge in mol/s d) y_A7 the concentration of A in the purge in mol% e) n_A_2, the mols/s of A in the reactor feed f) n_A_6, the mol/s of A in the recycle g) n_6, the flow of the recycle in mol/s h) n_2, the reactor feed in mol/s i) y_A_2, concentration of A in the reactor feed, in mol% j) n_3 the reactor effluent in mol/s
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