Blaise and Agatha are investigating parallel gas phase reactions between acetic acid (AA, CH3COOH) and hydrogen (H, H₂). The reaction products are ethanol (E, C₂H5OH) and water (W, H₂O) for the first reaction, and ethyl acetate (EA, C4H80₂) and water for the second reaction. The reactor operates at steady state with 164 mol/min acetic acid and 102 mol/min hydrogen entering at 101°C. The reactor effluent exits at 259°C. The conversion of acetic acid is measured as 36.2%, and the conversion of hydrogen is 77.5%. Using atom balances, determine some unknown component molar flow rates. n2, E Ex: 16.4 mol/min n2,EA== Ex: 15.0 mol/min ń₂,w Ex: 83.8 mol/min
Blaise and Agatha are investigating parallel gas phase reactions between acetic acid (AA, CH3COOH) and hydrogen (H, H₂). The reaction products are ethanol (E, C₂H5OH) and water (W, H₂O) for the first reaction, and ethyl acetate (EA, C4H80₂) and water for the second reaction. The reactor operates at steady state with 164 mol/min acetic acid and 102 mol/min hydrogen entering at 101°C. The reactor effluent exits at 259°C. The conversion of acetic acid is measured as 36.2%, and the conversion of hydrogen is 77.5%. Using atom balances, determine some unknown component molar flow rates. n2, E Ex: 16.4 mol/min n2,EA== Ex: 15.0 mol/min ń₂,w Ex: 83.8 mol/min
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:Blaise and Agatha are investigating parallel gas phase reactions between acetic acid (AA, CH3COOH)
and hydrogen (H, H₂). The reaction products are ethanol (E, C₂H5OH) and water (W, H₂O) for the first
reaction, and ethyl acetate (EA, C4H802) and water for the second reaction. The reactor operates at
steady state with 164 mol/min acetic acid and 102 mol/min hydrogen entering at 101°C. The reactor
effluent exits at 259°C. The conversion of acetic acid is measured as 36.2%, and the conversion of
hydrogen is 77.5%.
Using atom balances, determine some unknown component molar flow rates.
n₂, E
Ex: 16.4
Check
n₂, EA
mol/min Ex: 15.0
Next
mol/min
ń2,w =
Ex: 83.8
mol/min
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