CHEMICAL ENGINEERING

(Amelia) #1

236 CHEMICAL ENGINEERING VOLUME 1 SOLUTIONS


Calculate the time taken for the liquid level to fall to 5 cm below the top of the
tube, neglecting the effects of bulk flow in the vapour. 1 kmol occupies 22.4m^3 .Molec-
ular weights of acetone, dibutyl phthalateD58 and 279 kg/kmol respectively. Liquid
densities of acetone, dibutyl phthalateD764 and 1048 kg/m^3 respectively. Vapour pres-
sure of acetone at 315 KD 60 .5kN/m^2. Diffusivity of acetone vapour in air at 315 KD
0 .123 cm^2 /s.

Solution

Considering the situation when the liquid has fallen to a depthhcm below the top of the
tube, volume of acetone evaporatedD/ 4
 0. 6
2 h 1. 15
D 0. 283 h 1. 15
cm^3.
At this time, the amount of dibutyl phthalate is:

 2 ð 1. 048 / 278
D 0 .00754 mol

and the amount of acetoneD[2 0. 283 h 1. 15
]0. 764 / 58 D 0. 0306  0. 00372 h

∴ Mole fraction of acetoneD

0. 0306  0. 00372 h
 0. 00754 C 0. 0306  0. 00372 h

D


 8. 23 h

10. 24 h

Partial pressure of acetoneD 60. 5

(


8. 23 h
10. 24 h

)


kN/m^2

Molar concentration of acetone vapour at the liquid surface

D


(


60. 5


101. 3


)


ð

(


273


315


)


ð

(


1


22400


)(


8. 23 h
10. 24 h

)


D 2. 31 ð 10 ^5

(


8. 23 h
10. 24 h

)


mol/cm^3

Rate of evaporation of acetone:NAD

dh
dt

ð

0. 764


58


D 0. 0132 dh/dt
mol/cm^2 s

DD/h
ðmolar concentration at surfaceD 0. 123 /h
2. 31 ð 10 ^5

(


8. 23 h
10. 24 h

)


∴ 0. 0132


dh
dt

D


1


h

ð 2. 84 ð 10 ^6

(


8. 23 h
10. 24 h

)


and:

(


10. 24 h
8. 23 h

)


hdhD

dt
4650

The time for the liquid level to fall from 1.15 cm to 5 cm below the top of the tube is
obtained by integrating this equation:

∫ 5


1. 15

(


10. 24 h
8. 23 h

)


hdhD

1


4650


∫t

0

dtD

∫ 5


1. 15

(


h 2. 02 

16. 6


h 8. 23

)


dhD

1


4650


∫t

0

dt

and: tD79500 s 
79 .5ks³22 h
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