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2 kmol/h of Ca a, average Comp. relative volatility C, C2 8.22 2.42 1.00 0.378 90°F Comp. kmol/h C, 160 0.150 C3 nC4 370 240 25 2 kmol/h of C2 తోలోతోతతటి

2 kmol/h of Ca a, average Comp. relative volatility C, C2 8.22 2.42 1.00 0.378 90°F Comp. kmol/h C, 160 0.150 C3 nC4 370 240 25 2 kmol/h of C2 తోలోతోతతటి

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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For the deethanizer in Figure , estimate the number of stages, assuming it is equal to 2.5 times Nmin.

2 kmol/h of Ca a, average Comp. relative volatility C, C2 8.22 2.42 1.00 0.378 90°F Comp. kmol/h C, 160 0.150 C3 nC4 370 240 25 2 kmol/h of C2 తోలోతోతతటి
Transcribed Image Text:2 kmol/h of Ca a, average Comp. relative volatility C, C2 8.22 2.42 1.00 0.378 90°F Comp. kmol/h C, 160 0.150 C3 nC4 370 240 25 2 kmol/h of C2 తోలోతోతతటి
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