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water 60 0.041 Calculate: 1. The composition and flow rates for all streams around the absorber 2. Number of theoretical stages required if Lo=2 Lo(min)

water 60 0.041 Calculate: 1. The composition and flow rates for all streams around the absorber 2. Number of theoretical stages required if Lo=2 Lo(min)

Introduction to Chemical Engineering Thermodynamics
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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I need a clear answer by hand, not by keyboard and fast answer within 20 minutes. Thank you | dybala Isothermal absorber operated at 10 atm and 350 k to recover 95% of methanol by using water (mile) as solvent Component methane methanol water Vn+1 (mol/h) 20 70 60 Ki 94.096 0.159 0.041 Calculate: 1. The composition and flow rates for all streams around the absorber 2. Number of theoretical stages required if Lo-2 Lo(min)
Transcribed Image Text:I need a clear answer by hand, not by keyboard and fast answer within 20 minutes. Thank you | dybala Isothermal absorber operated at 10 atm and 350 k to recover 95% of methanol by using water (mile) as solvent Component methane methanol water Vn+1 (mol/h) 20 70 60 Ki 94.096 0.159 0.041 Calculate: 1. The composition and flow rates for all streams around the absorber 2. Number of theoretical stages required if Lo-2 Lo(min)
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