Absorption column which removes acetone from natural gas stream of 3000 Kmol/hr. The inlet gas 5 % of acetone and the outlet gas stream 0.3 % of acetone. Assume pure water enters the tower at the rate of 3500 Kmol/hr. Viscosity of water 0.303 N.m.sec/ m2, volatility of natural gas 2.3, MW of gas 10 Kg/Kmol, MW of water 18 Kg/Kmol, density of natural gas 4.8 Kg/ m3 and density of water 1000 Kg / m3. Design absorption column of packing type is intalox saddles ceramic of 1 inch and operating line is 0.1? (H.T. U= 1m).Calculate the actual height of absorption column in m? Select one: а. 13 b. 15 С. 10 d. 8

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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Absorption column which removes acetone
from natural gas stream of 3000 Kmol/hr.
The inlet gas 5 % of acetone and the outlet
gas stream 0.3 % of acetone. Assume pure
water enters the tower at the rate of 3500
Kmol/hr. Viscosity of water 0.303 N.m.sec/
m2, volatility of natural gas 2.3, MW of gas
10 Kg/Kmol, MW of water 18 Kg/Kmol,
density of natural gas 4.8 Kg/ m3 and
density of water 1000 Kg / m3. Design
absorption column of packing type is intalox
saddles ceramic of 1 inch and operating line
is 0.1? (H.T. U= 1m).Calculate the actual
height of absorption column in m?
Select one:
a. 13
b. 15
С. 10
d. 8
Transcribed Image Text:Absorption column which removes acetone from natural gas stream of 3000 Kmol/hr. The inlet gas 5 % of acetone and the outlet gas stream 0.3 % of acetone. Assume pure water enters the tower at the rate of 3500 Kmol/hr. Viscosity of water 0.303 N.m.sec/ m2, volatility of natural gas 2.3, MW of gas 10 Kg/Kmol, MW of water 18 Kg/Kmol, density of natural gas 4.8 Kg/ m3 and density of water 1000 Kg / m3. Design absorption column of packing type is intalox saddles ceramic of 1 inch and operating line is 0.1? (H.T. U= 1m).Calculate the actual height of absorption column in m? Select one: a. 13 b. 15 С. 10 d. 8
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