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(a) Table Q2(a) shows the vapor-liquid data for a mixture of acetone(A) and water(W) at 1.01 bar. Determine the relative volatility for 65 mol% acetone(A) and 35 mol% water(W) at 340 K and 1.01 bar using appropriate diagram based on the data provided in Table Q2(a). [Remember to snap the graph together with your answer scripts.] Table Q2(a): Vapor-liquid data for mixture of acetone and water at 1.01 bar. (Source: Reinders W.; de Minjer C.H.: VI. The System Water-Acetone- Chloroform. Recl.Trav.Chim.Pays-Bas 66 (1947) 573-604) Temperature, K mole fraction A in liquid | Mole fraction A in vapor phase, x phase, y 372.5 368.25 355.25 349.35 0.008 0.138 0.033 0.479 0.052 0.604 345.35 0.072 0.675 338.15 0.171 0.776 336.45 0.237 0.8 335.15 0.318 0.822 334.15 0.42 0.839 331.35 0.736 0.909 331.35 1 1

(a) Table Q2(a) shows the vapor-liquid data for a mixture of acetone(A) and water(W) at 1.01 bar. Determine the relative volatility for 65 mol% acetone(A) and 35 mol% water(W) at 340 K and 1.01 bar using appropriate diagram based on the data provided in Table Q2(a). [Remember to snap the graph together with your answer scripts.] Table Q2(a): Vapor-liquid data for mixture of acetone and water at 1.01 bar. (Source: Reinders W.; de Minjer C.H.: VI. The System Water-Acetone- Chloroform. Recl.Trav.Chim.Pays-Bas 66 (1947) 573-604) Temperature, K mole fraction A in liquid | Mole fraction A in vapor phase, x phase, y 372.5 368.25 355.25 349.35 0.008 0.138 0.033 0.479 0.052 0.604 345.35 0.072 0.675 338.15 0.171 0.776 336.45 0.237 0.8 335.15 0.318 0.822 334.15 0.42 0.839 331.35 0.736 0.909 331.35 1 1

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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(a) Table Q2(a) shows the vapor-liquid data for a mixture of acetone(A) and water(W) at 1.01 bar. Determine the relative volatility for 65 mol% acetone(A) and 35 mol% water(W) at 340 K and 1.01 bar using appropriate diagram based on the data provided in Table Q2(a). [Remember to snap the graph together with your answer scripts.] Table Q2(a): Vapor-liquid data for mixture of acetone and water at 1.01 bar. (Source: Reinders W.; de Minjer C.H.: VI. The System Water-Acetone- Chloroform. Recl.Trav.Chim.Pays-Bas 66 (1947) 573-604) Temperature, mole fraction A in liquid | Mole fraction A in vapor phase, x K phase, y 372.5 368.25 0.008 0.138 355.25 0.033 0.479 349.35 0.052 0.604 345.35 0.072 0.675 338.15 0.171 0.776 336.45 0.237 0.8 335.15 0.318 0.822 334.15 0.42 0.839 331.35 0.736 0.909 331.35 1 1
Transcribed Image Text:(a) Table Q2(a) shows the vapor-liquid data for a mixture of acetone(A) and water(W) at 1.01 bar. Determine the relative volatility for 65 mol% acetone(A) and 35 mol% water(W) at 340 K and 1.01 bar using appropriate diagram based on the data provided in Table Q2(a). [Remember to snap the graph together with your answer scripts.] Table Q2(a): Vapor-liquid data for mixture of acetone and water at 1.01 bar. (Source: Reinders W.; de Minjer C.H.: VI. The System Water-Acetone- Chloroform. Recl.Trav.Chim.Pays-Bas 66 (1947) 573-604) Temperature, mole fraction A in liquid | Mole fraction A in vapor phase, x K phase, y 372.5 368.25 0.008 0.138 355.25 0.033 0.479 349.35 0.052 0.604 345.35 0.072 0.675 338.15 0.171 0.776 336.45 0.237 0.8 335.15 0.318 0.822 334.15 0.42 0.839 331.35 0.736 0.909 331.35 1 1
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