A 1-ft diameter packed column is used to scrub a soluble gas (MW = 22) from an air-gas mixture. Pure water enters the top of the col- umn at 1000 lb,/tr. The entering gas stream contains 5% soluble gas and 95% air. Ninety-five percent of the soluble gas is removed. Both the operating line and equilibriam curve may be assumed to be straight, The equation for the equilibrium curve is y = 1.2x, where x, y = mole fractions. The entering gas mixture iow rate is 800 lb,„/hr. The column operates at 30 °C and 1 atm, and k,a = 12.0 lbmol/hr-ft-Ay ka = 8.0 lbmol/hr-ft-Ar O = 1.0

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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Calculate or find:
Concentration of the soluble gas in the effluent liquid if the column is operated at minimum liquid flow rate

A 1-ft diameter packed column is used to scrub a soluble gas (MW
= 22) from an air-gas mixture. Pure water enters the top of the col-
umn at 1000 lb,/tr. The entering gas stream contains 5% soluble
gas and 95% air. Ninety-five percent of the soluble gas is removed.
Both the operating line and equilibriam curve may be assumed to
be straight, The equation for the equilibrium curve is y = 1.2x,
where x, y = mole fractions. The entering gas mixture iow rate is
800 lb,„/hr. The column operates at 30 °C and 1 atm, and
k,a = 12.0 lbmol/hr-ft-Ay
ka = 8.0 lbmol/hr-ft-Ar
O = 1.0
Transcribed Image Text:A 1-ft diameter packed column is used to scrub a soluble gas (MW = 22) from an air-gas mixture. Pure water enters the top of the col- umn at 1000 lb,/tr. The entering gas stream contains 5% soluble gas and 95% air. Ninety-five percent of the soluble gas is removed. Both the operating line and equilibriam curve may be assumed to be straight, The equation for the equilibrium curve is y = 1.2x, where x, y = mole fractions. The entering gas mixture iow rate is 800 lb,„/hr. The column operates at 30 °C and 1 atm, and k,a = 12.0 lbmol/hr-ft-Ay ka = 8.0 lbmol/hr-ft-Ar O = 1.0
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