A liquid is fed to a distillation column at 4 atm absolute pressure. Its composition as a mole fraction is: n-butane: 0.40, n-pentane: 0.25, n-hexane: 0.20, n-heptane: 0.15. Using the equilibrium distribution coefficients (K), find the temperature at which this liquid will begin to boil (bubble temperature). Calculate the concentration of the first vapor bubble formed.

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
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A liquid is fed to a distillation column at 4 atm absolute pressure. Its composition as a mole fraction is: n-butane: 0.40, n-pentane: 0.25, n-hexane: 0.20, n-heptane: 0.15. Using the equilibrium distribution coefficients (K), find the temperature at which this liquid will begin to boil (bubble temperature).
Calculate the concentration of the first vapor bubble formed.

10.0
5.0
n-bütan
n-pentan
1.0
0.5
n-hekzan
. 0.10
0.05
25
75
100
125
150
T(°C)
Hafif hidrokarbon sistemleri için 405.3 kPa (4.0 atm) mutlak
175
200
basınçıa K denge değerleri.
n-heptan
50
Transcribed Image Text:10.0 5.0 n-bütan n-pentan 1.0 0.5 n-hekzan . 0.10 0.05 25 75 100 125 150 T(°C) Hafif hidrokarbon sistemleri için 405.3 kPa (4.0 atm) mutlak 175 200 basınçıa K denge değerleri. n-heptan 50
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