Consider a solution of Brz in CCI4. This solution will behave as an ideal dilute solution for low concentrations of Br2. The vapor pressure of CC14 is 33.85 torr at T= 298K. The Henry's law constant for the solution is 122.36 torr. The non-standard unit for the Henry's law constant is due to the concentration of Br2 being expressed as mole fraction. Calculate the following for a Xer2 = .07solution: a. Vapor pressure of CCI4. | b. Vapor pressure of Brz. c. Total pressure. d. Composition of the vapor phase.
Consider a solution of Brz in CCI4. This solution will behave as an ideal dilute solution for low concentrations of Br2. The vapor pressure of CC14 is 33.85 torr at T= 298K. The Henry's law constant for the solution is 122.36 torr. The non-standard unit for the Henry's law constant is due to the concentration of Br2 being expressed as mole fraction. Calculate the following for a Xer2 = .07solution: a. Vapor pressure of CCI4. | b. Vapor pressure of Brz. c. Total pressure. d. Composition of the vapor phase.
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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Consider a solution of Br2 in CCl4
Transcribed Image Text:7. Consider a solution of Br2 in CCI4. This solution will behave as an ideal dilute solution for low
concentrations of Br2. The vapor pressure of CC14 is 33.85 torr at T= 298K. The Henry's law
constant for the solution is 122.36 torr. The non-standard unit for the Henry's law constant is
due to the concentration of Br2 being expressed as mole fraction. Calculate the following for a
XBr2 = .07solution:
a. Vapor pressure of CCl4.
|
b. Vapor pressure of Br2.
c. Total pressure.
d. Composition of the vapor phase.
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