It is desired to produce 46.4 mol/s of Ethylene glycol (EG). The reactor is to be operated isothermally. A 16.1 mol/L solution of ethylene oxide (EO) in water is mixed with an equal volumetric solution of water containing 0.9 wt% of the catalyst H₂SO4 and fed to a CSTR. The specific reaction-rate constant is 0.311 min-¹. If 80% conversion is to be achieved, determine the necessary CSTR volume. • If two 3.028m³ reactors were arranged in parallel with the feed equally divided, what would be the corresponding conversion? • If two 3.028m³ reactors were arranged in series, what would be the corresponding conversion?
It is desired to produce 46.4 mol/s of Ethylene glycol (EG). The reactor is to be operated isothermally. A 16.1 mol/L solution of ethylene oxide (EO) in water is mixed with an equal volumetric solution of water containing 0.9 wt% of the catalyst H₂SO4 and fed to a CSTR. The specific reaction-rate constant is 0.311 min-¹. If 80% conversion is to be achieved, determine the necessary CSTR volume. • If two 3.028m³ reactors were arranged in parallel with the feed equally divided, what would be the corresponding conversion? • If two 3.028m³ reactors were arranged in series, what would be the corresponding conversion?
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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Transcribed Image Text:It is desired to produce 46.4 mol/s of Ethylene glycol (EG). The reactor is to be
operated isothermally. A 16.1 mol/L solution of ethylene oxide (EO) in water is
mixed with an equal volumetric solution of water containing 0.9 wt% of the
catalyst H₂SO, and fed to a CSTR. The specific reaction-rate constant is 0.311 min-¹.
• If 80% conversion is to be achieved, determine the necessary CSTR volume.
• If two 3.028m³ reactors were arranged in parallel with the feed equally divided,
what would be the corresponding conversion?
• If two 3.028m³ reactors were arranged in series, what would be the
corresponding conversion?
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