A solute A is to be recovered from an inert carrier gas B by absorption into a solvent. The gas entering into the absorber flows at a rate of 500 kmol/hr with y = 0.3 and leaving the absorber with y₁ = 0.01. Solvent enters the absorber at the rate of 1500 kmol/hr with x= 0.001. The equilibrium relationship is y₁ = 2.8xA. The carrier gas may be considered insoluble in the solvent and the solvent may be considered nonvolatile. Construct the x-y plots for the equilibrium and operating lines using both mole fraction and solute-free coordinates.

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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Chapter1: Introduction
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A solute A is to be recovered from an inert carrier gas B by absorption into a solvent. The gas entering into the absorber flows at a rate of
500 kmol/hr with y = 0.3 and leaving the absorber with y₁ = 0.01. Solvent enters the absorber at the rate of 1500 kmol/hr with x=
0.001. The equilibrium relationship is y₁ = 2.8xA. The carrier gas may be considered insoluble in the solvent and the solvent may be
considered nonvolatile. Construct the x-y plots for the equilibrium and operating lines using both mole fraction and solute-free coordinates.
Transcribed Image Text:A solute A is to be recovered from an inert carrier gas B by absorption into a solvent. The gas entering into the absorber flows at a rate of 500 kmol/hr with y = 0.3 and leaving the absorber with y₁ = 0.01. Solvent enters the absorber at the rate of 1500 kmol/hr with x= 0.001. The equilibrium relationship is y₁ = 2.8xA. The carrier gas may be considered insoluble in the solvent and the solvent may be considered nonvolatile. Construct the x-y plots for the equilibrium and operating lines using both mole fraction and solute-free coordinates.
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