10.25 For the system ethylene(1)/propylene(2) as a gas, estimate f1. f2. 1. and 2 at 1 = 150 C. P 30 bar, and vi = 0.35: !! (a) Through application of Eqs. (10.63). (b) Assuming that the mixture is an ideal solution.

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
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10.25 For the system ethylene(1)/propylene(2) as a gas, estimate f1. f2. 1. and d2 at 1 =
150 C. P= 30 bar, and yj =0.35:
(a) Through apPplication of Eqs. (10.63).
(b) Assuming that the mixture is an ideal solution.
Transcribed Image Text:10.25 For the system ethylene(1)/propylene(2) as a gas, estimate f1. f2. 1. and d2 at 1 = 150 C. P= 30 bar, and yj =0.35: (a) Through apPplication of Eqs. (10.63). (b) Assuming that the mixture is an ideal solution.
Signature Panel
an T, 2
= B1 + (1- yı)y2812= B11+ y3812
Therefore,
P.
In 1=(B11+ yd12)
(10.63a)
RT
Similarly,
In 2
RT
(B22+ yi812)
(10.63b)
!!
378
CHAPTER 10. The Framework of Solution Thermodynamics
Equations (10.63) are readily extended for application to multicomponent gas mixtures; the
general equation is: 10
(10.64)
In d
RT
B+EE yy,(25 -6y)
where the dummy indices i and j run over all species, and
Transcribed Image Text:Signature Panel an T, 2 = B1 + (1- yı)y2812= B11+ y3812 Therefore, P. In 1=(B11+ yd12) (10.63a) RT Similarly, In 2 RT (B22+ yi812) (10.63b) !! 378 CHAPTER 10. The Framework of Solution Thermodynamics Equations (10.63) are readily extended for application to multicomponent gas mixtures; the general equation is: 10 (10.64) In d RT B+EE yy,(25 -6y) where the dummy indices i and j run over all species, and
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