10,000 6,000 4,000 2,000 1,000 o Critical points 600 400 Carbon dioxide 200 Triple point 100 Ethylene 60 40 Ethane 20 Sulfur dioxide (Solid CO,) Water 10 Methanol Propane 4 Methyl chloride i-Butane Ethyl chloride 0.6 0.4 n-Butane i-Pentane 0.2 n-Heptane Acetic Acid Acetone 0.1 -100 n-Pentane Ethanol -75 п-Нехапе Toluene -Oc tane- и n-Propyl benzene n-De cane Benzene -50 -25 o-Xylene- 25 50 75 Temperature, "E 100 150 luulinbinluulwuul 200 250 300 350 400 500 600 700 800 ШAL Vapor pressure, Ib/sq in. 2. Nitrobenzene Dowtherm A Mercury ППTTT
10,000 6,000 4,000 2,000 1,000 o Critical points 600 400 Carbon dioxide 200 Triple point 100 Ethylene 60 40 Ethane 20 Sulfur dioxide (Solid CO,) Water 10 Methanol Propane 4 Methyl chloride i-Butane Ethyl chloride 0.6 0.4 n-Butane i-Pentane 0.2 n-Heptane Acetic Acid Acetone 0.1 -100 n-Pentane Ethanol -75 п-Нехапе Toluene -Oc tane- и n-Propyl benzene n-De cane Benzene -50 -25 o-Xylene- 25 50 75 Temperature, "E 100 150 luulinbinluulwuul 200 250 300 350 400 500 600 700 800 ШAL Vapor pressure, Ib/sq in. 2. Nitrobenzene Dowtherm A Mercury ППTTT
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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Approximate Vapor–Liquid–Liquid Equilibrium.
A mixture of 1,000 kmol of 75 mol% water and 25 mol% n-octane is cooled under equilibrium conditions at a constant pressure of 133.3 kPa from a temperature of 136oC to a temperature of 25oC.Determine: (a) the initial phase condition, and (b) the temperature, phase amounts, and compositions when each phase change occurs.Assume that water and n-octane are immiscible liquids. The vaporpressure of octane is included in Figure 2.3.
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