- The operating conditions were 25 °C, 1 atm for the diffusing of Oxygen through a non- diffusing water. The equilibrium equation: y 1.4 x, the individual mass transfer coefficient of the gas phase Kc and the bulk gas concentration are (1.15*10$ kmol/s.m2, 0.6) respectively. The individual mass transfer coefficient of the liquid phase KL and the bulk liquid concentration are (1.32*105 kmol/s.m2, 0.15) respectively. Find the interface concentration in gas and liquid phase and then find the percent resistance in liquid phase.
- The operating conditions were 25 °C, 1 atm for the diffusing of Oxygen through a non- diffusing water. The equilibrium equation: y 1.4 x, the individual mass transfer coefficient of the gas phase Kc and the bulk gas concentration are (1.15*10$ kmol/s.m2, 0.6) respectively. The individual mass transfer coefficient of the liquid phase KL and the bulk liquid concentration are (1.32*105 kmol/s.m2, 0.15) respectively. Find the interface concentration in gas and liquid phase and then find the percent resistance in liquid phase.
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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