The impact of an intermediate reboiler or condenser on the distillatio
n of ideal binary mixtures into pure product streams is studied using
a simplified model. The advantage of heuristics derived from this stud
y is that they can quickly tell a process engineer if an intermediate
reboiler ol condenser is going to be effective in improving the effici
ency and, of the two options, which one would be more effective. The h
euristics simply states that if the actual fraction of liquid in a giv
en feed is less than that with the maximum thermodynamic efficiency fo
r distillation with no intermediate reboiler or condenser then an inte
rmediate condenser not only substantially improves the thermodynamic e
fficiency but is also more effective than an intermediate reboiler. An
analogous heuristics exists for the intermediate reboiler when the fr
action of liquid in the feed is greater than the optimum. Quick identi
fication of cases that can achieve a substantial improvement in effici
ency provides an incentive to search for the proper utilities needed f
or the intermediate reboiler or condenser. When relatively pure feed s
treams (concentration of either component greater than 90%) are distil
led, the extremely low efficiencies of distillation can be remarkably
improved by using an intermediate reboiler or condenser.