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2. The liquid-vapor equilibrium of a mixture of toluene (boiling point Of 110.6 °C at 1 atm) and o-xylene (boiling point Of 144 C at 1 atm) can be adequately modeled by Raoult's law. For a mixture of 2 moles toluene and 3 moles o-xylene use the attached phase diagrams and calculate the following: a) Dew point and composition of the liquid b) Bubble point and composition of the vapor c) The aforementioned mixture is suddenly brought to 100 oC and 300 mm Hg. Calculate the composition of liquid and/or vapor phases as well as molar amounts of liquid and/or vapor Toluene/ o-Xylene at 100°C 550 500 450 I 400 350 300 250 200 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x or y (mole fraction) Toluene / o-xylene at 300 mm Hg 115 110 105 100 CO 9 95 90 85 80 75 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x o y (mole fraction)

2. The liquid-vapor equilibrium of a mixture of toluene (boiling point Of 110.6 °C at 1 atm) and o-xylene (boiling point Of 144 C at 1 atm) can be adequately modeled by Raoult's law. For a mixture of 2 moles toluene and 3 moles o-xylene use the attached phase diagrams and calculate the following: a) Dew point and composition of the liquid b) Bubble point and composition of the vapor c) The aforementioned mixture is suddenly brought to 100 oC and 300 mm Hg. Calculate the composition of liquid and/or vapor phases as well as molar amounts of liquid and/or vapor Toluene/ o-Xylene at 100°C 550 500 450 I 400 350 300 250 200 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x or y (mole fraction) Toluene / o-xylene at 300 mm Hg 115 110 105 100 CO 9 95 90 85 80 75 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x o y (mole fraction)

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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2. The liquid-vapor equilibrium of a mixture of toluene (boiling point Of 110.6 °C at 1 atm) and o-xylene (boiling point Of 144 C at 1 atm) can be adequately modeled by Raoult's law. For a mixture of 2 moles toluene and 3 moles o-xylene use the attached phase diagrams and calculate the following: a) Dew point and composition of the liquid b) Bubble point and composition of the vapor c) The aforementioned mixture is suddenly brought to 100 oC and 300 mm Hg. Calculate the composition of liquid and/or vapor phases as well as molar amounts of liquid and/or vapor Toluene/ o-Xylene at 100°C 550 500 450 I 400 350 300 250 200 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x or y (mole fraction) Toluene / o-xylene at 300 mm Hg 115 110 105 100 CO 9 95 90 85 80 75 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x o y (mole fraction)
Transcribed Image Text:2. The liquid-vapor equilibrium of a mixture of toluene (boiling point Of 110.6 °C at 1 atm) and o-xylene (boiling point Of 144 C at 1 atm) can be adequately modeled by Raoult's law. For a mixture of 2 moles toluene and 3 moles o-xylene use the attached phase diagrams and calculate the following: a) Dew point and composition of the liquid b) Bubble point and composition of the vapor c) The aforementioned mixture is suddenly brought to 100 oC and 300 mm Hg. Calculate the composition of liquid and/or vapor phases as well as molar amounts of liquid and/or vapor Toluene/ o-Xylene at 100°C 550 500 450 I 400 350 300 250 200 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x or y (mole fraction) Toluene / o-xylene at 300 mm Hg 115 110 105 100 CO 9 95 90 85 80 75 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 .0 x o y (mole fraction)
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