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11.7-2. Boiling Point, Dew Point, and Flash Vaporization. Following is the composition 0.35), n-pentane 0.20). At a pressure of a liquid feed in mole fraction: n-butane (xA (хв — 0.20), п-hexane, (xс %3D 0.25), п-heptane (хр of 405.3 kPa calculate the following. (a) Boiling point and composition of the vapor in equilibrium.

11.7-2. Boiling Point, Dew Point, and Flash Vaporization. Following is the composition 0.35), n-pentane 0.20). At a pressure of a liquid feed in mole fraction: n-butane (xA (хв — 0.20), п-hexane, (xс %3D 0.25), п-heptane (хр of 405.3 kPa calculate the following. (a) Boiling point and composition of the vapor in equilibrium.

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
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11.7-2. Boiling Point, Dew Point, and Flash Vaporization. Following is the composition 0.35), n-pentane 0.20). At a pressure of a liquid feed in mole fraction: n-butane (xA (хв — 0.20), п-hexane, (xс %3D 0.25), п-heptane (хр of 405.3 kPa calculate the following. (a) Boiling point and composition of the vapor in equilibrium.
Transcribed Image Text:11.7-2. Boiling Point, Dew Point, and Flash Vaporization. Following is the composition 0.35), n-pentane 0.20). At a pressure of a liquid feed in mole fraction: n-butane (xA (хв — 0.20), п-hexane, (xс %3D 0.25), п-heptane (хр of 405.3 kPa calculate the following. (a) Boiling point and composition of the vapor in equilibrium.
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