Chapter 11 Transport Process and Unit Operations C.J. Geankoplis
11.7-3 Vaporization of Multicomponent Alcohol Mixture
The vapor-pressure data are given below.
T (˚C) |
Vapor Pressure (mmHg) |
|||
Methanol |
Ethanol |
n-Propanol |
n-Butanol |
|
50 |
415 |
220.0 |
88.9 |
33.7 |
60 |
629 |
351.5 |
148.9 |
59.2 |
65 |
767 |
438 |
190.1 |
77.7 |
70 |
929 |
542 |
240.6 |
99.6 |
75 |
1119 |
665 |
301.9 |
131.3 |
80 |
1339 |
812 |
376.0 |
165.0 |
85 |
1593 |
984 |
465 |
206.1 |
90 |
1884 |
1185 |
571 |
225.9 |
100 |
2598 |
1706 |
843 |
387.6 |
Following is the composition of a liquid alcohol
mixture to be fed to a distillation tower at 101.32 kPa: methyl alcohol (xA
= 0.30), ethyl alcohol xB = 0.20), n-propyl alcohol (xC =
0.15), and n-butyl alcohol (xD = 0.35). Calculate the following
assuming that the mixture follow Raoult;s law.
(a)
Boiling
point and composition of vapor in equilibrium.
(b)
Dew
point and composition of liquid in equilibrium.
(c)
The
temperature and composition of both phases when 40% of the feed is vaporized in
a flash distillation.
Solving:
(a)
Using trial and error method
Trial |
T (°C) |
P^0_A |
P^0_B |
P^0_C |
P^0_D |
Sigma XiP^0_i |
1 |
80 |
1339 |
812 |
376.0 |
165.0 |
678.25 |
2 |
85 |
1593 |
984 |
465 |
206.1 |
816.585 |
3 |
83 |
1481.4 |
915.2 |
429.4 |
189.66 |
761.251 |
Value for T= 83°C determined
by using interpolation. Data 1 use at T = 80°C and data 2 use at T = 85°C.
The closest value is T =
83°C, and it becoming the boiling point.
(b)
Using trial and error method
Trial |
T (°C) |
P^0_A |
P^0_B |
P^0_C |
P^0_D |
Sigma Xi/P^0_i |
1 |
90 |
1884 |
1185 |
571 |
225.9 |
0.00214 |
2 |
100 |
2598 |
1706 |
843 |
387.6 |
0.001314 |
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