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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 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%

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 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%

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 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 LA reactor Reactor Separator Pure C A B• 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) 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 LA reactor Reactor Separator Pure C A B• 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) 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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