2. In the methanol synthesis described above, small quantities of non-reactive gaseous impurities (N2, hydrocarbons) are presented in the feed. They do not dissolve to any appreciative extent in the liquid methanol product, so they must be removed by a purge in the recycle line. If they are not removed, the concentration of impurities and the pressure will increase, to the detriment of the desired reaction. The feed gas contains 66.6% H₂, SOL33.33% CO and 0.1% non-reactive impurities. The plant produces 1000 gal/h of methanol at 70°F with a 15% conversion in the reactor. What must be the purge rate to maintain the impurity concentration in the recycle below 1% (by volume)? e 16212 PURGE: 66%H₂ 33% CO 1% impurities una (0 up of the ab Feed Gas 62 Cont 66.67% H₂ 22102 exp 33.33% CO 0.10% impurities 100°F, 300 atm MS[61.2 16 esco Olavic Lusts (20mple 118 Recycle gas (66.67% H₂, 33.33%CO) Condenser Reactor 300 atm 300°FUO Vine MOUS SOL Separator col Methanol Product

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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FUL2 9
In the methanol synthesis described above, small
quantities of non-reactive gaseous impurities (N2,
hydrocarbons) are presented in the feed. They do not
dissolve to any appreciative extent in the liquid methanol
on product, so they must be removed by a purge in the
corecycle line. If they are not removed, the concentration of
impurities and the pressure will increase, to the detriment
of the desired reaction. The feed gas contains 66.6% H₂,
ELSTOL 33.33% CO and 0.1% non-reactive impurities. The plant
produces 1000 gal/h of methanol at 70°F with a 15%
conversion in the reactor. What must be the purge rate to
(0 maintain the impurity concentration in the recycle below
uc1% (by volume)? Gre PURGE: 66%H₂
118
33% CO
1% impurities
2.
mas o que eu ab
Feed Gas 62' Chin
66.67% H₂
33.33% CO
0.10% impuritiessure
Separator
100°F, 300 atm MS
e eue C
relaciona clasic spel (20mple Methanol Product
122102 exu
Recycle gas (66.67% H₂, 33.33%CO)
Condenser
Reactor
300 atm
300°FUO Viney
QUGI SOL
Transcribed Image Text:FUL2 9 In the methanol synthesis described above, small quantities of non-reactive gaseous impurities (N2, hydrocarbons) are presented in the feed. They do not dissolve to any appreciative extent in the liquid methanol on product, so they must be removed by a purge in the corecycle line. If they are not removed, the concentration of impurities and the pressure will increase, to the detriment of the desired reaction. The feed gas contains 66.6% H₂, ELSTOL 33.33% CO and 0.1% non-reactive impurities. The plant produces 1000 gal/h of methanol at 70°F with a 15% conversion in the reactor. What must be the purge rate to (0 maintain the impurity concentration in the recycle below uc1% (by volume)? Gre PURGE: 66%H₂ 118 33% CO 1% impurities 2. mas o que eu ab Feed Gas 62' Chin 66.67% H₂ 33.33% CO 0.10% impuritiessure Separator 100°F, 300 atm MS e eue C relaciona clasic spel (20mple Methanol Product 122102 exu Recycle gas (66.67% H₂, 33.33%CO) Condenser Reactor 300 atm 300°FUO Viney QUGI SOL
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