The top product, P, from a pressure distillation column is taken off as vapour.
The vapour composition and vapour-liquid equilibria data
at two different temperatures are given in Table Q1.
(a) Stating clearly any assumptions used regarding the streams leaving the
reflux drum, calculate the composition of the liquid reflux, L.
(

for a reflux ratio, L/P, of 3.0.
© Outline the information that you would require and indicate the expected
operating conditions for the design of a column separating such a mixture
Component
Mole fraction in
product P
Equilibrium Constant
at T = 340K
Equilibrium Constant
at T = 350K
n - propane
0.50
2.33
2.67
n - butane
0.45
0.79
1.18
n - pentane
0.05
0.23
0.40