Q1) Sulfur dioxide (A) is being absorbed into water in a packed column, where bulk conditions are 50°C, 2 atm, yaA= 0.08, and x = 0.001, whereas the liquid concentration is estimated to be 55 kmol/m'. Experimental values of the mass transfer coefficients are: k=0.18 m/hr, kg = 0.04 kmol/ (hr-m²-kPa). The equilibrium data for the system is plotted as in Fig.-QI: 007 006 y 00s- 002- 05 x 10 Figure-QI: Equilibrium concentration of (A) in water ii- Estimate the mole fractions at the interface ( i.e. Xai and ya). iii- Calculate the overall mass transfer coefficient (K',). iv- Calculate the percent resistance in the liquid phase and the flux NA.
Q1) Sulfur dioxide (A) is being absorbed into water in a packed column, where bulk conditions are 50°C, 2 atm, yaA= 0.08, and x = 0.001, whereas the liquid concentration is estimated to be 55 kmol/m'. Experimental values of the mass transfer coefficients are: k=0.18 m/hr, kg = 0.04 kmol/ (hr-m²-kPa). The equilibrium data for the system is plotted as in Fig.-QI: 007 006 y 00s- 002- 05 x 10 Figure-QI: Equilibrium concentration of (A) in water ii- Estimate the mole fractions at the interface ( i.e. Xai and ya). iii- Calculate the overall mass transfer coefficient (K',). iv- Calculate the percent resistance in the liquid phase and the flux NA.
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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