Page 327 - Design and Operation of Heat Exchangers and their Networks
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312   Design and operation of heat exchangers and their networks



             Example H22C17—cont’d

             monogenetic algorithm (Fieg et al., 2009) to solve this problem and
             obtained the best heat exchanger network shown in Fig. 6.35, which
             consists of 16 subnetworks. The largest subnetwork comprises four hot
             streams and two cold streams. There are totally eight independent
             variables, which yields the minimum TAC of 1,897,159$/yr.




          References
          Adjiman, C.S., Androulakis, I.P., Floudas, C.A., 2000. Global optimization of mixed-integer
             nonlinear problems. AIChE J. 46 (9), 1769–1797.
          Ahmad, S., 1985. Heat Exchanger Networks: Cost Tradeoffs in Energy and Capital (Ph.D.
             thesis). University of Manchester, Institute of Science and Technology.
          Ahmad, S., Linnhoff, B., Smith, R., 1990. Cost optimum heat exchanger networks—2. Tar-
             gets and design for detailed capital cost models. Comput. Chem. Eng. 14 (7), 751–767.
          Athier, G., Floquet, P., Pibouleau, L., Domenech, S., 1997. Synthesis of heat-exchanger net-
             work by simulated annealing and NLP procedures. AIChE J. 43 (11), 3007–3020.
          Azeez, O.S., Isafiade, A.J., Fraser, D.M., 2012. Supply and target based superstructure
             synthesis of heat and mass exchanger networks. Chem. Eng. Res. Des. 90 (2),
             266–287.
          Azeez, O.S., Isafiade, A.J., Fraser, D.M., 2013. Supply-based superstructure synthesis of heat
             and mass exchange networks. Comput. Chem. Eng. 56, 184–201.
          Bagajewicz, M.J., Pham, R., Manousiouthakis, V., 1998. On the state space approach to
             mass-heat exchanger network design. Chem. Eng. Sci. 53 (14), 2595–2621.
          Bergamini, M.L., Scenna, N.J., Aguirre, P.A., 2007. Global optimal structures of heat
             exchanger networks by piecewise relaxation. Ind. Eng. Chem. Res. 46 (6), 1752–1763.
          Biegler, L.T., Grossmann, I.E., Westerberg, A.W., 1997. Systematic Methods of Chemical
             Process Design. Prentice Hall PTR.
          Bjork, K.-M., Pettersson, F., 2003. Optimization of large-scale heat exchanger network syn-
             thesis problems. In: Proceedings of the IASTED International Conference on Modelling
             and Simulation, Hamza MH (Ed.), IASTED. ACTA Press.
          Bjork, K.M., Westerlund, T., 2002. Global optimization of heat exchanger network synthe-
             sis problems with and without the isothermal mixing assumption. Comput. Chem. Eng.
             26, 1581–1593.
          Bogataj, M., Kravanja, Z., 2012. An alternative strategy for global optimization of heat
             exchanger networks. Appl. Therm. Eng. 43, 75–90.
          Bohnenstaedt, T., Brandt, C., Fieg, G., Dietrich, W., 2014. Energy integration manager:
             a workflow for long term validity of total site analysis and heat recovery strategies.
             In: Klemes ˇ, J.J., Varbanov, P.S., Liew, P.Y. (Eds.), Proceedings of the 24th Euro-
             pean Symposium on Computer Aided Process Engineering, pp. 1819–1824.
          Brandt, C., Fieg, G., Luo, X., 2011. Efficient synthesis of heat exchanger networks
             combining heuristic approaches with a genetic algorithm. Heat Mass Transf.
             47, 1019–1026.
          Castillo, E.F., Acevedo, L., Reverberi, A.P., 1998. Cleaner production of nitric acid by heat
             transfer optimization: a case study. Chem. Biochem. Eng. Q. 12 (3), 157–163.
          Chakraborty, S., Ghosh, P., 1999. Heat exchanger network synthesis: the possibility of ran-
             domization. Chem. Eng. J. 72 (3), 209–216.
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