A new procedure for estimating area and capital cost targets of constrained
heat exchanger networks is presented. The method allows for match constrai
ned networks and exchangers with more than one tube pass. The procedure is
based on modelling the problem as a non-linear formulation where the forbid
den exchanger matches are included as constraints and the temperature diffe
rence correction due to multipass exchangers is included in the model. The
difficulty of converging to a solution due to the additional non-linear con
straints imposed by the multipass exchangers required the use of a two-leve
l approach: at the inner level, the area targets for simple pass exchangers
are obtained, and at the outer level the temperature difference required f
or multipass exchangers are computed and fed back to the inner level. The p
rocedure is repeated until an appropriate tolerance between two iterations
was achieved. A comparison between the estimated exchanger areas and costs
estimated by the new procedure and the area and costs obtained from the fin
al heat exchanger design shows a very good agreement.