Evaporation systems are separation processes widely used in chemical indust
ries. Some guidelines can be found in the literature for the process integr
ation of multiple effect evaporators. In the published methodologies some a
spects are neglected as boiling point rise, effect of pressure on latent he
at of water, sensible heat of liquid streams, heat of mixing, effects confi
guration and inclusion of accessories. In this work, a new graphical repres
entation for the integration of multiple effect evaporators was developed,
using rigorous physical properties. From this representation, an algorithm
for optimization of bleed streams was conceived using the concepts of Pinch
Analysis. As a case study, a crystal glucose plant was optimized using thi
s new methodology. The optimization of bleed streams showed as result a ste
am consumption 16% smaller than a similar previous study. From energy and c
apital costs, it is shown that the integrated evaporator exhibits a total c
ost 14% smaller than the non-integrated configuration.