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EXERCISES Section 2.1 2.1. 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 e minimum work of separation, Wmins in kJ/h for To 298.15 K. kmol/h Component Feed Product 1 Ethane Propane n-butane n-pentane n-hexane 30 200 370 350 50 30 192 4 0 Product 1 Vapor 25,040 Feed Product 2 Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid 364 19,480 Liquid 394 25,640 36.64 33.13 54.84

EXERCISES Section 2.1 2.1. 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 e minimum work of separation, Wmins in kJ/h for To 298.15 K. kmol/h Component Feed Product 1 Ethane Propane n-butane n-pentane n-hexane 30 200 370 350 50 30 192 4 0 Product 1 Vapor 25,040 Feed Product 2 Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid 364 19,480 Liquid 394 25,640 36.64 33.13 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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EXERCISES Section 2.1 2.1. 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 e minimum work of separation, Wmins in kJ/h for To 298.15 K. kmol/h Component Feed Product 1 Ethane Propane n-butane n-pentane n-hexane 30 200 370 350 50 30 192 4 0 Product 1 Vapor 25,040 Feed Product 2 Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid 364 19,480 Liquid 394 25,640 36.64 33.13 54.84
Transcribed Image Text:EXERCISES Section 2.1 2.1. 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 e minimum work of separation, Wmins in kJ/h for To 298.15 K. kmol/h Component Feed Product 1 Ethane Propane n-butane n-pentane n-hexane 30 200 370 350 50 30 192 4 0 Product 1 Vapor 25,040 Feed Product 2 Phase condition Temperature, K Enthalpy, kJ/kmol Entropy, kJ/kmol-K Liquid 364 19,480 Liquid 394 25,640 36.64 33.13 54.84
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