A value of kG was experimentally determined to be 1.08 lb mol/h•ft2•atm for A diffusing through stagnant B. For the same flow and concentrations, it is desired to predict k’G and the flux of A for equimolar counter diffusion. Determine the mass transfer coefficients using other units. The partial pressures are pA1 = 0.20 atm, pA2 = 0.05 atm, and P = 1.0 atm total. Use SI and AES units.
A value of kG was experimentally determined to be 1.08 lb mol/h•ft2•atm for A diffusing through stagnant B. For the same flow and concentrations, it is desired to predict k’G and the flux of A for equimolar counter diffusion. Determine the mass transfer coefficients using other units. The partial pressures are pA1 = 0.20 atm, pA2 = 0.05 atm, and P = 1.0 atm total. Use SI and AES units.
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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A value of kG was experimentally determined to be 1.08 lb mol/h•ft2•atm for A diffusing through stagnant B. For the same flow and concentrations, it is desired to predict k’G and the flux of A for equimolar counter diffusion. Determine the
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