An original feed (66.67% H2 by mole, 33.33% CO by mole) is mixed with the recycle (66.67% H2 by mole, 33.33% CO by mole) before entering the reactor. From the reactor, the product is condensed and separated from the unconverted gases. The density of the methanol product is 0.7917 g/cm3. For every 1000 gal/hr of methanol product; (3.785 L = 1 gal, 2.2 lb = 1 kg), calculate a) lbmoles/hr of methanol product, b) lbmole/hr of original feed, and c) lbmoles/hr of recycle.
An original feed (66.67% H2 by mole, 33.33% CO by mole) is mixed with the recycle (66.67% H2 by mole, 33.33% CO by mole) before entering the reactor. From the reactor, the product is condensed and separated from the unconverted gases. The density of the methanol product is 0.7917 g/cm3. For every 1000 gal/hr of methanol product; (3.785 L = 1 gal, 2.2 lb = 1 kg), calculate a) lbmoles/hr of methanol product, b) lbmole/hr of original feed, and c) lbmoles/hr of recycle.
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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Question
An original feed (66.67% H2 by
mole, 33.33% CO by mole) is mixed with the recycle (66.67% H2 by mole, 33.33% CO by
mole) before entering the reactor. From the reactor, the product is condensed and
separated from the unconverted gases. The density of the methanol product is 0.7917
g/cm3. For every 1000 gal/hr of methanol product; (3.785 L = 1 gal, 2.2 lb = 1 kg),
calculate a) lbmoles/hr of methanol product, b) lbmole/hr of original feed, and c)
lbmoles/hr of recycle.
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