Equilibrium Data 0.003 0.008 0.015 0.023 0.032 0.043 0.01 0.02 0.03 0.04 0.05 0.06 0.055 0.068 0.083 0.099 0.12 X 0.07 0.08 0.09 0.10 0.11 Y = moles CO2/mole air, X = moles CO/mole amine solution
Equilibrium Data 0.003 0.008 0.015 0.023 0.032 0.043 0.01 0.02 0.03 0.04 0.05 0.06 0.055 0.068 0.083 0.099 0.12 X 0.07 0.08 0.09 0.10 0.11 Y = moles CO2/mole air, X = moles CO/mole amine solution
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 exit gas from an alcohol fermenter consists of an air–CO2mixture containing 10 mol% CO2 that is to be absorbed in a 5.0-N solution of triethanolamine, containing 0.04 mol CO2 per mole of amine solution. If the column operates isothermally at 25oC, if the exit liquid contains 78.4% of the CO2 in the feed gas to the absorber,and if absorption is carried out in a six-theoretical-plate column, use the equilibrium data below to calculate: (a) exit gas composition, (b) moles of amine solution required per mole of feed gas.
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