(b) Ammonia is to be removed from air flow rate 1.67 kg/m²- min, by contact with pure water in backed absorption tower the entering gas stream contained 0.03 and the existing gas stream contained 0.004 mole fraction of NH3 mole fraction, the rate of pure water entering the column is 2.0 kg/m²- min ,the gas and liquid mass transfer coefficient are K x=255 kgmol/hr-m³, K-y 127.5 kgmol/hr-m³. Determine the height of the column if the equilibrium line y = 0.9x

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
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(b) Ammonia is to be removed from air flow rate 1.67 kg/m²- min, by contact with pure
water in backed absorption tower the entering gas stream contained 0.03 and the existing
gas stream contained 0.004 mole fraction of NH3 mole fraction, the rate of pure water
entering the column is 2.0 kg/m²- min ,the gas and liquid mass transfer coefficient are
K x=255 kgmol/hr-m³, K-y-127.5 kgmol/hr-m³. Determine the height of the
column if the equilibrium line y = 0.9x
Transcribed Image Text:(b) Ammonia is to be removed from air flow rate 1.67 kg/m²- min, by contact with pure water in backed absorption tower the entering gas stream contained 0.03 and the existing gas stream contained 0.004 mole fraction of NH3 mole fraction, the rate of pure water entering the column is 2.0 kg/m²- min ,the gas and liquid mass transfer coefficient are K x=255 kgmol/hr-m³, K-y-127.5 kgmol/hr-m³. Determine the height of the column if the equilibrium line y = 0.9x
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