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


The closest value is T = 100°C, and it becoming the dew point.


(c)


Trial

T (°C)

P^0_A

P^0_B

P^0_C

P^0_D

Sigma

1

85

1593

984

465

206.1

0.148

2

90

1884

1185

571

225.9

0.013

The closest value is T = 90°C. Then the temperature is 90°C.

That's answer for Question 11.7-3





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