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CP (kJ/mol) (J/mol-°C) Co (g) H2 (9) CH,OH (g) -110.52 29.24 28.91 83.5 -201.2

CP (kJ/mol) (J/mol-°C) Co (g) H2 (9) CH,OH (g) -110.52 29.24 28.91 83.5 -201.2

Introduction to Chemical Engineering Thermodynamics
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 synthesis of methanol from carbon monoxide and hydrogen is carried out in a continuous vapour-phase reactor at 1.00 atm. The feed contains CO and H2 in stoichiometric proportion and enters the reactor at 25°C and 1.00 atm at a rate of 17.0 to 21.0 m/h. The product stream emerges from the reactor at 127°C. The rate of heat transfer from the reactor is 3.00 to 10.00 kW. calculate the highest and lowest fractional conversion can be achieved by manipulating the two process variables. Assume that the gas is ideal. Give your conclusion. CP (J/mol-•C) (kJ/mol) co (g) H2 (9) CH;OH (g) -110.52 29.24 28.91 -201.2 83.5
Transcribed Image Text:The synthesis of methanol from carbon monoxide and hydrogen is carried out in a continuous vapour-phase reactor at 1.00 atm. The feed contains CO and H2 in stoichiometric proportion and enters the reactor at 25°C and 1.00 atm at a rate of 17.0 to 21.0 m/h. The product stream emerges from the reactor at 127°C. The rate of heat transfer from the reactor is 3.00 to 10.00 kW. calculate the highest and lowest fractional conversion can be achieved by manipulating the two process variables. Assume that the gas is ideal. Give your conclusion. CP (J/mol-•C) (kJ/mol) co (g) H2 (9) CH;OH (g) -110.52 29.24 28.91 -201.2 83.5
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