A non-ideal solution system at 120°F has the following overall composition as shown in Table 2. Table 2: Composition of system. Component % Mole Propane Butane Calculate: a. ته د ن م م C. Pentane e. Hexane The bubble point pressure. b. Composition of vapor (y) at bubble point pressure. The dew point pressure. d. Composition of liquid (x₁) at dew point pressure. Sketch phase diagram of the system. 50 25 15 10
A non-ideal solution system at 120°F has the following overall composition as shown in Table 2. Table 2: Composition of system. Component % Mole Propane Butane Calculate: a. ته د ن م م C. Pentane e. Hexane The bubble point pressure. b. Composition of vapor (y) at bubble point pressure. The dew point pressure. d. Composition of liquid (x₁) at dew point pressure. Sketch phase diagram of the system. 50 25 15 10
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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Transcribed Image Text:A non-ideal solution system at 120°F has the following overall composition as shown in Table 2.
Table 2: Composition of system.
Component % Mole
Propane
50
Butane
25
Pentane
15
Hexane
10
Calculate:
a.
The bubble point pressure.
b.
Composition of vapor (y) at bubble point pressure.
C.
The dew point pressure.
d.
Composition of liquid (x) at dew point pressure.
Sketch phase diagram of the system.
e.
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Step 1: Calculate (a)bubble point pressure (b)composition of vapor (c)the dew point pressure.
VIEWStep 2: Find saturation pressure for each component.
VIEWStep 3: Find the bubble point pressure.
VIEWStep 4: Calculate composition of vapor at bubble point.
VIEWStep 5: Calculate the Dew point pressure.
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