x (mole) y (mole) 9000 L/min of a gas mixture containing 30% NH3, 70% Air by mole shall be treated in a packed absorber using 25 mm plastic Super Intalox saddles. 90% of the ammonia is to be 0.008093 0.004943 0.009014 0.105263 0.046517 0.209302 0.13205 absorbed using a water rate which is 1.5 times the minimum. Operating conditions are 1.5 atm and 10°C. 0.312139 0.31167 0.413793 0.656896 0.514286 4.213524 0.613636 4.922198- Given the equilibrium data, determine the tower diameter.

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
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Subject: Mass Transfer
Topic: Equilibrium Relations in Interphase Mass Transfer: Gas Absorption

Problem 1
x (mole)
y (mole)
9000 L/min of a gas mixture containing 30%
NH3, 70% Air by mole shall be treated in a
packed absorber using 25 mm plastic Super
Intalox saddles. 90% of the ammonia is to be
0.008093
0.004943
0.009014
0.105263
0.046517
0.209302
0.13205
absorbed using a water rate which is 1.5 times
the minimum. Operating conditions are 1.5 atm
and 10°C.
0.312139
0.31167
0.413793
0.656896
0.514286
4.21352+
0.613636
4.922198
Given the equilibrium data, determine the
tower diameter.
Transcribed Image Text:Problem 1 x (mole) y (mole) 9000 L/min of a gas mixture containing 30% NH3, 70% Air by mole shall be treated in a packed absorber using 25 mm plastic Super Intalox saddles. 90% of the ammonia is to be 0.008093 0.004943 0.009014 0.105263 0.046517 0.209302 0.13205 absorbed using a water rate which is 1.5 times the minimum. Operating conditions are 1.5 atm and 10°C. 0.312139 0.31167 0.413793 0.656896 0.514286 4.21352+ 0.613636 4.922198 Given the equilibrium data, determine the tower diameter.
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