Consider the following process flow chart with accompanying stream table. Note the stream denoted as S5 is a recycle stream. S5 MIXER REACTOR SEPARATOR S1 S3 S4 Stream si S2 S3 S4 S5 Components CO 30 yı Уз 0.3 y4 H2 59.4 118.8 59.4 59.4 CH;OH y2 34.4 29.7 ys termine: a. single pass conversion of hydrogen b. overall conversion of hydrogen c. overall conversion of carbon monoxide d. moles of methanol into reactor
Consider the following process flow chart with accompanying stream table. Note the stream denoted as S5 is a recycle stream. S5 MIXER REACTOR SEPARATOR S1 S3 S4 Stream si S2 S3 S4 S5 Components CO 30 yı Уз 0.3 y4 H2 59.4 118.8 59.4 59.4 CH;OH y2 34.4 29.7 ys termine: a. single pass conversion of hydrogen b. overall conversion of hydrogen c. overall conversion of carbon monoxide d. moles of methanol into reactor
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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The following is a material balance problem and I was wondering how to determine a. through d. and how to solve for the unknowns.

Transcribed Image Text:Consider the following process flow chart with accompanying stream table. Note the stream denoted
as S5 is a recycle stream.
S5
MIXER
REACTOR
SEPARATOR
S1
S3
S4
Stream
si
S2
S3
S4
S5
Components
CO
30
yı
Уз
0.3
y4
H2
59.4
118.8
59.4
59.4
CH;OH
y2
34.4
29.7
ys
termine:
a. single pass conversion of hydrogen
b. overall conversion of hydrogen
c. overall conversion of carbon monoxide
d. moles of methanol into reactor
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