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elationship is given as y = 30.5 x*. Calculate (a) the molar flux of gas (b) bulk liquid hase concentration ( c) the overall liquid phase mass transfer coefficient and (d) the ndividual and overall gas phase driving forces

elationship is given as y = 30.5 x*. Calculate (a) the molar flux of gas (b) bulk liquid hase concentration ( c) the overall liquid phase mass transfer coefficient and (d) the ndividual and overall gas phase driving forces

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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Solute A is being absorbed from a mixture of insoluble gas in a wetted wall column in pure water at 303 K and 1.45 bar pressure. The gas phase mass transfer coefficient is 90.3 kmol/(h)(m³)(kmol/m'). It is known that 14 % of the total resistance lies in the gas phase. At a point in the column the concentration of A in bulk gas is 0.065 mol.fr. and the interfacial concentration of A in the liquid is 0.0021 mol.fr. The equilibrium relationship is given as y = 30.5 x*. Calculate (a) the molar flux of gas (b) bulk liquid phase concentration ( c) the overall liquid phase mass transfer coefficient and (d) the individual and overall gas phase driving forces
Transcribed Image Text:Solute A is being absorbed from a mixture of insoluble gas in a wetted wall column in pure water at 303 K and 1.45 bar pressure. The gas phase mass transfer coefficient is 90.3 kmol/(h)(m³)(kmol/m'). It is known that 14 % of the total resistance lies in the gas phase. At a point in the column the concentration of A in bulk gas is 0.065 mol.fr. and the interfacial concentration of A in the liquid is 0.0021 mol.fr. The equilibrium relationship is given as y = 30.5 x*. Calculate (a) the molar flux of gas (b) bulk liquid phase concentration ( c) the overall liquid phase mass transfer coefficient and (d) the individual and overall gas phase driving forces
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