Why the equation is 1-X1 -X2 ? So How to calculate and how to find the balance (mole balance, atomic balance(Co, H2,N2)species balance(Co, H2,N2),of the process in overall, mixing point,condenser 100 mo/hn, (mol M)n (mol CH, OH / h).reactorcond.32 mol COm64 mol H,/h4 mol N,7h13 mol N,/mol500 mol /hx, (mol N, mol)n, (mol /h)x, (mol CÔ / mol)1-X-X, (mol H2/ h)x, (mol CÓ / mol)1-x,-x, (mol H,/ h)Purge Methanol is synthesized from carbon monoxide and hydrogen in a catalytic reactor. The fresh feedto the process contains 32.0 mole% CO, 64.0% H2, and 4.0% N2. This stream is mixed with a recyclestream in a ratio 5 mol recycle/1 mol fresh feed to produce the feed to the reactor, which contains13.0 mole % N2. A low single-pass conversion is attained in the reactor. The reactor effluent goesto a condenser from which two streams emerge: a liquid product stream containing essentially allthe methanol formed in the reactor, and a gas stream containing all the CO, H2, and N2 leaving thereactor. The gas stream is split into two fractions: one is removed from the process as a purge stream,and the other is the recycle stream that combines with the fresh feed to the reactor.

The reason for the equation is to be mentioned. The steps to calculate the mole balance at the the…

Answered: 100 mo/h n, (mol M) n (mol CH, OH / h).…

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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Why the equation is 1-X₁ -X₂ ? So How to calculate and how to find the balance (mole balance, atomic balance(Co, H2,N2)species balance(Co, H2,N2),of the process in overall, mixing point,condenser

100 mo/h
n, (mol M)
n (mol CH, OH / h).
reactor
cond.
32 mol COm
64 mol H,/h
4 mol N,7h
13 mol N,/mol
500 mol /h
x, (mol N, mol)
n, (mol /h)
x, (mol CÔ / mol)
1-X-X, (mol H2/ h)
x, (mol CÓ / mol)
1-x,-x, (mol H,/ h)
Purge

Methanol is synthesized from carbon monoxide and hydrogen in a catalytic reactor. The fresh feed
to the process contains 32.0 mole% CO, 64.0% H2, and 4.0% N2. This stream is mixed with a recycle
stream in a ratio 5 mol recycle/1 mol fresh feed to produce the feed to the reactor, which contains
13.0 mole % N2. A low single-pass conversion is attained in the reactor. The reactor effluent goes
to a condenser from which two streams emerge: a liquid product stream containing essentially all
the methanol formed in the reactor, and a gas stream containing all the CO, H2, and N2 leaving the
reactor. The gas stream is split into two fractions: one is removed from the process as a purge stream,
and the other is the recycle stream that combines with the fresh feed to the reactor.

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