For the reaction A B, the process flow diagram is shown in Figure The fresh fecd of A contains 0.5% of inerts by volume. 60% conversion of A per pass is obtained. The concentration of incrts going into the reactor at (1) must be held at 2% by volume. All streams are ideal gases and the process is at steady state. (a) How many moles necd to be recycled per mole of total feed to the reactor at (1)? (b) How many moles need to be purged? (c) What is the overall conversion of 4? NOTE:-You must be take the basis on point 1 Fresh feed, A, / (1) (2) B Reactor Separator (3) P, Purge, A,I Recycle, A, I

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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For the reaction A B, the process flow diagram is shown in Figure
The fresh feed of A contains 0.5% of inerts by volume. 60% conversion of A per pass is
obtained. The concentration of incrts going into the reactor at (1) must be held at 2% by
volume. All streams are ideal gases and the process is at steady state.
(a) How many moles necd to be recycled per mole of total feed to the reactor at (1)?
(b) How many moles need to be purged?
(c) What is the overall conversion of A?
NOTE:-You must be take the basis on point 1
Fresh feed, A, /
(1)
(2)
Separator
Reactor
(3)
P, Purge, A, I
Recycle, A, I
Transcribed Image Text:For the reaction A B, the process flow diagram is shown in Figure The fresh feed of A contains 0.5% of inerts by volume. 60% conversion of A per pass is obtained. The concentration of incrts going into the reactor at (1) must be held at 2% by volume. All streams are ideal gases and the process is at steady state. (a) How many moles necd to be recycled per mole of total feed to the reactor at (1)? (b) How many moles need to be purged? (c) What is the overall conversion of A? NOTE:-You must be take the basis on point 1 Fresh feed, A, / (1) (2) Separator Reactor (3) P, Purge, A, I Recycle, A, I
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