The synthesis of methanol from carbon monoxide and hydrogen is carried out in a continuous reactor in the gas phase at 7 atm (abs) pressure. The feed contains CO and H2 in a stoichiometric proportion and enters at 85°C, with a flow rate of 25 m^3/h. The product stream exits at 250°C. To maintain operating conditions, 25 kW are transferred from the reactor. Calculate: a. The molar flow of CO fed, n CO (mol/h) b. The molar flow rate of the reaction mixture, n (mol/h) c. The fractional conversion of CO, x d. The molar flow of CH3OH produced, n methanol (mol/h) e. The volumetric flow rate of the reaction product mixture, Vmr (m^3/s)

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
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The synthesis of methanol from carbon monoxide and hydrogen is carried out in a continuous reactor in the gas phase at 7 atm (abs) pressure. The feed contains CO and H2 in a stoichiometric proportion and enters at 85°C, with a flow rate of 25 m^3/h. The product stream exits at 250°C. To maintain operating conditions, 25 kW are transferred from the reactor. Calculate:

a. The molar flow of CO fed, n CO (mol/h)

b. The molar flow rate of the reaction mixture, n (mol/h)

c. The fractional conversion of CO, x

d. The molar flow of CH3OH produced, n methanol (mol/h)

e. The volumetric flow rate of the reaction product mixture, Vmr (m^3/s)

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