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kmol/h Component Feed Product 1 Ethane 30 30 Propane 200 192 n-butane 370 4 n-pentane 350 n-hexane 50 Product 1 Product 2 Feed Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid Vapor 313 Liquid 394 364 19,480 25,040 25,640 33.13 36.64 54.84

kmol/h Component Feed Product 1 Ethane 30 30 Propane 200 192 n-butane 370 4 n-pentane 350 n-hexane 50 Product 1 Product 2 Feed Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid Vapor 313 Liquid 394 364 19,480 25,040 25,640 33.13 36.64 54.84

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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Minimum work of separation.
A refinery stream is separated at 1,500 kPa into two products under the conditions shown below. Using the data given, compute the minimum work of separation, Wmin, in kJ/h for T0 =298.15 K.

kmol/h Component Feed Product 1 Ethane 30 30 Propane 200 192 n-butane 370 4 n-pentane 350 n-hexane 50
Transcribed Image Text:kmol/h Component Feed Product 1 Ethane 30 30 Propane 200 192 n-butane 370 4 n-pentane 350 n-hexane 50
Product 1 Product 2 Feed Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid Vapor 313 Liquid 394 364 19,480 25,040 25,640 33.13 36.64 54.84
Transcribed Image Text:Product 1 Product 2 Feed Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid Vapor 313 Liquid 394 364 19,480 25,040 25,640 33.13 36.64 54.84
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