The absorption of solute A from a mixture is done in a wetted wall column by a solvent at 1 atm and 25 0C. The value of mass transfer coefficient is 9.0*10-4 m/s. At a point, the mole fraction of A in the liquid gas interface is 2.0*10-5 in the liquid phase. Partial pressure of A in the gas phase is 0.08 atm. Henry’s law relation is pA = 600(xA) in atm. Calculate the rate of Absorption of A.

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
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The absorption of solute A from a mixture is done in a wetted wall column by a solvent at 1 atm and 25 0C. The value of mass transfer coefficient is 9.0*10-4 m/s. At a point, the mole fraction of A in the liquid gas interface is 2.0*10-5 in the liquid phase. Partial pressure of A in the gas phase is 0.08 atm. Henry’s law relation is pA = 600(xA) in atm. Calculate the rate of Absorption of A.

The absorption of solute A from a mixture is done in a wetted wall column by a solvent
at 1 atm and 25 °C. The value of mass transfer coefficient is 9.0*104 m/s. At a point, the
mole fraction of A in the liquid gas interface is 2.0*10-$ in the liquid phase. Partial
pressure of A in the gas phase is 0.08 atm. Henry’s law relation is
PA = 600(xA) in atm. Calculate the rate of Absorption of A.
Transcribed Image Text:The absorption of solute A from a mixture is done in a wetted wall column by a solvent at 1 atm and 25 °C. The value of mass transfer coefficient is 9.0*104 m/s. At a point, the mole fraction of A in the liquid gas interface is 2.0*10-$ in the liquid phase. Partial pressure of A in the gas phase is 0.08 atm. Henry’s law relation is PA = 600(xA) in atm. Calculate the rate of Absorption of A.
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