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DaatianA single vapar-liquid oquilibrium point for the water (1) anl Cystem is esperimentally meaured at 30C. The eperiment provides the felowing informtion 030. 023, andP-10.1P Ue is informationetimte he ytem presre and vaporphase mole faction whenn0K

DaatianA single vapar-liquid oquilibrium point for the water (1) anl Cystem is esperimentally meaured at 30C. The eperiment provides the felowing informtion 030. 023, andP-10.1P Ue is informationetimte he ytem presre and vaporphase mole faction whenn0K

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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Use Antoine's oquaticn to estimate the pure components vapor peessure. Assame that the excess molar Gibbs free energy and the activity coeficients can be correlated using the following oquations A RT Iny, - Anj. In y, - An
Transcribed Image Text:Use Antoine's oquaticn to estimate the pure components vapor peessure. Assame that the excess molar Gibbs free energy and the activity coeficients can be correlated using the following oquations A RT Iny, - Anj. In y, - An
Shaotan: A single vapor-liquid equilibrium point for the water (1) + ethanol C ystem is experimentally measured at 30C. The experiment peovides the following information: 0.30, n 0.23, and P 10.1 kPA. Use this information to estimate the system pressure and vapor phase mole fraction when aOK
Transcribed Image Text:Shaotan: A single vapor-liquid equilibrium point for the water (1) + ethanol C ystem is experimentally measured at 30C. The experiment peovides the following information: 0.30, n 0.23, and P 10.1 kPA. Use this information to estimate the system pressure and vapor phase mole fraction when aOK
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