The operational performance of a paper production plant can be significantl
y improved by appropriate process interventions. This paper deals with ener
gy aspects of the most important section of such a plant, the paper drying
section. A significant intervention that would lower the operational cost o
f the drying process is proposed. It refers to the recompression of low pre
ssure steam leaving the dryers by means of a thermocompressor that would ut
ilize high pressure steam coming from the plant burners. The mathematical m
odel of the thermocompressor is evaluated and its design procedure is formu
lated as a mathematical programming problem involving appropriate objective
function and constraints.