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CHAPTER 6

              Optimal design of heat exchanger

              networks


                             a
                                       b
              Wilfried Roetzel , Xing Luo , Dezhen Chen c
              a
              Institute of Thermodynamics, Helmut Schmidt University/University of the Federal Armed Forces Hamburg,
              Hamburg, Germany
              b
              Institute of Thermodynamics, Gottfried Wilhelm Leibniz University Hannover, Hannover, Germany
              c
              Institute of Thermal Energy and Environmental Engineering, Tongji University, Shanghai, China

              In many industrial processes, heat exchanger networks are used to transfer
              heat among more than two process streams, in which the cold streams are
              heated by the hot streams that need to be cooled and vice versa. In this
              way, a large amount of heat energy can be recovered from the process
              streams, and therefore, the heating and cooling loads from external
              sources (hot and cold utilities) can be dramatically reduced. However,
              the use of heat exchangers for heat recovery also increases the investment
              costs. Therefore, a balance between the utility costs and investment costs
              should be established. The optimal design of a heat exchanger network is
              to configure a heat recovery system or retrofit an existing network capable
              of performing the prescribed tasks at the minimum total annual costs that
              are mainly determined by the utility costs and investment costs (Masso
              and Rudd, 1969). Because of its structural characteristics, it is also named
              as synthesis of heat exchanger networks. The optimal design also deals
              with the optimal retrofit design of an existing heat exchanger network
              by rematching the process streams; changing the heat exchanger area;
              and adding or removing some heat exchangers, heaters, and coolers, so
              that the sum of the annual utility costs and retrofitting costs reaches
              the minimum.
                 The available optimization design and synthesis methods can be classified
              into three categories: (1) thermodynamic analysis methods with pinch
              technology (Linnhoff and Flower, 1978a; Linnhoff et al., 1979); (2) math-
              ematical programming methods (Grossmann and Sargent, 1978); and
              (3) stochastic or heuristic algorithms such as genetic algorithm (Lewin,
              1998), simulated annealing algorithm (Dolan et al., 1989) and particle swarm


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