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Unformatted text preview: chlorobenzene with specified number of
equilibrium stages, boilup ratio, and reflux ratio.
Given: Feed is a saturated liquid of 54.5 mol% benzene. Column contains two equilibrium
plates with feed to the bottom plate. Column is equipped with total condenser and partial
reboiler. Boilup is V/F = 0.855. Reflux ratio, L/V = 0.5. Vaporliquid equilibrium data given.
Find: Compositions of distillate and bottoms, assuming constant molar overflow.
Analysis: Take as a basis, F = 100 mol/s. Therefore, vapor generated in reboiler = 0.855(100)
= 85.5 mol/s. Since the feed is a saturated liquid, this vapor rate continues up the column to the
condenser. L/V = 0.5, which is the slope of the operating line. Therefore, L = 0.5(85.5) = 42.75
mol/s. Therefore, the distillate rate = 85.5  42.75 = 42.75 mol/s. Passing to the reboiler is a
liquid rate of 42.75 + 100 = 142.75 mol/s. The bottoms rate = 142.75  85.5 = 57.25 mol/s. The
slope of the stripping section operating line is L / V = 142.75/85.5 = 1.67. The qline is a
vertical line because the feed is a saturated liquid. To solve for the compositions of the distillate
and bottoms on a McCabeThiele diagram, we must locate the operating lines to obtain three
equilibrium stages that satisfy an overall benzene material balance given by,
xFF = 54.4 = xDD + xBB = 42.75xD + 57.25xB
Solving Eq. (1),
xB = 0.952  0.7467 xD (1)
(2) Therefore, an approach to solving this exercise is to assume a value of xD and then compute the
value of xB from Eq. (2). Then construct the McCabeThiele diagram with the above operating
lines and qline to see if three stages are required with the feed to the second plate.
See plot below, where benzene mole fractions are plotted because it is the more volatile
component. It is seen that for benzene, xD = 0.90 and xB = 0.28. Exercise 7.14 (continued)
McCabeThiele Diagram Exercise 7.15
Subject: Effect of loss of plates in a distillation column separating a benzenetoluene mixture.
Given: Saturated vapor feed of 13,600 kg/h of 40 wt% benzene and 60 wt% toluene. Column
with 14 plates above the feed location. Plate efficiency is 50%. Reflux ratio is 3.5. Previously,
with 10 plates in the stripping section, column could achieve a distillate of 97 wt% benzene and a
bottoms of 98 wt% toluene. Vaporliquid equilibrium data in Exercise 7.13.
Assumptions: Constant molar overflow. Total condenser and partial reboiler.
Find: (a) If column with 10 inoperable plates can yield a distillate of 97 wt% benzene,
assuming that we no longer can achieve the 98 wt% bottoms product.
(b) The distillate flow rate.
(c) The composition of the bottoms.
Analysis: (a) First convert the feed to kmol/h and mole fractions, using molecular weights of
78.11 for benzene and 92.13. The result is:
Component
kmol/h Mole fraction
Benzene
69.65
0.44
Toluene
88.57
0.56
Total: 158.22
1.00
For a distillate of 97 wt% benzene, the mole fraction for benzene, the more volatile of the two
components, is,
97
7811
.
xD =
= 0.974
97
3
+
78.11 92.13
Wit...
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 Spring '11
 Levicky
 The Land

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