How a novel design of continuous distillation columns may impact the perfor
mance of conventional controllers when it is required to accurately control
the purity of both products in a binary separation is analyzed. The propos
ed column layout is characterized by the presence of a middle vessel, to wh
ich two streams are fed: the liquid flow coming from the rectifying section
and the feed to be separated. The actual liquid flow to the column is dete
rmined by the middle-vessel level controller. For different control configu
rations and conventional proportional-integral control, it is shown that us
ing a middle-vessel column provides a way to reduce the interaction between
the composition loops, in such a way that the control performance of middl
e-vessel columns may be made remarkably superior to that of the conventiona
l columns. The results obtained are supported by a theoretical analysis bas
ed on the frequency-dependent relative gain array tool.