A tray distillation column fractionates a mixture of n-hexane, n-heptane, and n-octane. The
liquid leaving the last tray (lowermost tray) is introduced to a reboiler which operates at 413
K and 3.07 bara. The composition of the liquid entering the reboiler is shown in Table 2.
Table 2. Composition of liquid entering reboiler.
Composition (mol basis)
Component
n-hexane
n-heptane
n-octane
0.12
0.78
0.1
a. Calculate the boil-up ratio of this operation.
[10 marks]
b. Determine the composition of the vapor entering the last tray (lowermost tray) of the
column.
[10 marks]
2
c. There is a suggestion from a newly joined process engineer to increase the reboiler
temperature to 420 K while maintaining the pressure and feed composition the same.
Evaluate the feasibility of this suggestion. You need to support your evaluation with
detailed calculations.
[10 marks]
Fig: 1