A new procedure for estimating area and capital cost targets of constrained heat exchanger networks is presented. The method allows for match constrained networks and exchangers with more than one tube pass. The procedure is based on modelling the problem as a non-linear formulation where the forbidden exchanger matches are included as constraints and the temperature difference correction due to multipass exchangers is included in the model. The difficulty of converging to a solution due to the additional non-linear constraints imposed by the multipass exchangers required the use of a two-level approach: at the inner level, the area targets for simple pass exchangers are obtained, and at the outer level the temperature difference required for multipass exchangers are computed and fed back to the inner level. The procedure 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 final heat exchanger design shows a very good agreement.
[1]
Ignacio E. Grossmann,et al.
A structural optimization approach in process synthesis. II: Heat recovery networks
,
1983
.
[2]
Manfred Morari,et al.
Area and capital cost targets for heat exchanger network synthesis with constrained matches and unequal heat transfer coefficients
,
1990
.
[3]
G. L. Shires,et al.
Process Heat Transfer
,
1994
.
[4]
B. Linnhoff,et al.
Design of Multipass Heat Exchangers: An Alternative Approach
,
1988
.
[5]
B. Linnhoff,et al.
Supertargeting; Different process structures for different economics
,
1989
.
[6]
R. Smith,et al.
Targets and design for minimum number of shells in heat exchanger networks
,
1989
.