Page 310 - Design and Operation of Heat Exchangers and their Networks
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296   Design and operation of heat exchangers and their networks



             Example H5C5—cont’d
                                                    Total annual cost ($/yr)

            Solutions in the literature          Reported    Revised
            Pettersson (2008)                     43,331     43,314
            Toffolo (2009)                        43,314
            Lin and Miller (2004)                 43,329     43,321
            Wei (2003), Wei et al. (2004a) a      43,777     43,329
            Gupta and Ghosh (2010)                43,342     43,342
            Huang and Karimi (2013)               43,359     43,359
            Floudas and Ciric (1989) a            43,830 b   43,376
            Linnhoff et al. (1979)  a,c           43,857
            Athier et al. (1997) a,c              43,856     43,393
            He and Cui (2013) c                   43,392
            Yee et al. (1990) a                   43,878     43,407
            Peng and Cui (2015) c                 43,411     43,411
            Huo et al. (2012)                     43,431     43,429
                            c
            Pariyani et al. (2006)                43,439     43,440
            Linnhoff and Flower (1978b) c         43,934     43,469
                            a,c
            Nishida et al. (1977)                 43,984     43,523
            Bergamini et al. (2007) c             43,220     43,590
            Escobar and Trierweiler (2013, Fig. A5)  43,570  43,627
            Nu ´n ˜ez-Serna and Zamora (2016, Fig. 8)  43,646  43,646
            Myankooh and Shafiei (2015)           43,718     43,649
            Yu et al. (2000) a,c                  43,176     43,688
            Chen and Cui (2016) c                 43,656     43,692
            Pho and Lapidus (1973) a,c            44,158     43,698
            Nu ´n ˜ez-Serna and Zamora (2016, Fig. 7) c  43,733  43,733
                           c
            Lewin et al. (1998)                   43,452     43,751
            Chakraborty and Ghosh (1999) c        44,214
                                            c
            Papoulias and Grossmann (1983a, Fig. 9)  –       43,803
            Su and Motard (1984) c                44,124     44,074
            a
            Using English units.
            b
             This value is obtained according to Fig. 9 of Floudas and Ciric (1989). The reported value of TAC
            was obviously a mistake.
            c
            No stream split.
             configurations, we have revised all the available results by the use of the
             problem data in SI, as is listed in Table 6.28. It shows that the effort for
             finding its global optimal design is just like an Olympic game. The best
             network configuration so far was obtained by Pettersson (2008), which
             has three independent variables for the three stream splits, as is shown
             in Fig. 6.28. According to his reported TAC of 43,331$/yr, the
             isothermal mixing of the splitting streams might be used. The local
             minimal TAC of 43,314$/yr was obtained by Toffolo (2009).
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