Xg. Zhao et al., HEAT INTEGRATION FOR BATCH PROCESSES - PART 2 - HEAT-EXCHANGER NETWORK DESIGN, Chemical engineering research & design, 76(A6), 1998, pp. 700-710
A three-step design procedure is proposed for the design of heat excha
nger networks (HENs) for batch/semi-continuous processes. This consist
s of the initial individual design, the rematching design and the fina
l overall design. Firstly, for every time interval, the conventional m
ethods for continuous processes can be used directly to develop the in
itial individual designs. Based on the information provided by this de
sign, the second individual designs are then performed by focusing on
the optimal rematching of streams for maximum use of the common exchan
gers. Finally, the overall design is obtained through some adjustments
of area, energy exchanged and configuration of the HEN for further op
timization of the whole system. The information on rematching is obtai
ned by solving an MILP model-the transshipment model developed specifi
cally for batch/semi-continuous processes. A case study is provided to
demonstrate the design procedure and its effectiveness.