Page 124 - Design and Operation of Heat Exchangers and their Networks
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112   Design and operation of heat exchangers and their networks


          3.4.1 Mathematical model
          The thermal calculation of spiral heat exchangers has been analyzed theoret-
          ically, experimentally, and numerically by many researchers (Baird et al.,
          1958; Chowdhury et al., 1985; Picon-Nunez et al., 2007; Rajavel and
          Saravanan, 2008; Sathiyan et al., 2010; Kaman et al., 2017). A systematic
          theoretical work has been contributed by Bes (1978, 2001) and Bes and
          Roetzel (1992a, 1992b, 1993, 1998) and is introduced as follows.
             Bes and Roetzel (1992a) treated the spiral heat exchanger with the spi-
          ral of Archimedes. A spiral heat exchanger can usually be divided into
          three regions: the innermost region where heat is transferred only through
          one wall; the middle region (referred to as bulk part) with turns, which
          usually occupies the main space of the exchanger and performs the main
          duty of the exchanger; and the outmost region, where heat is transported
          again through one wall only (i.e., the outside wall of the spiral heat
          exchanger is insulated). For a counterflow spiral heat exchanger shown
          in Fig. 3.9, the energy equations of the three parts can be expressed as
          follows:
             The innermost region,0<θ<2π:

                           _  dt h θðÞ
                          C h      + khrφ rðÞ t h θðÞ t c θðÞ½  Š ¼ 0  (3.208)
                               dθ
                  _  dt c θðÞ
                 C c     + khrφ rðÞ t h θðÞ t c θðÞ½  Š
                     dθ                                              (3.209)
                                    ð
                             ð
                         + kh r + s c Þφ r + s c Þ t h θ +2πð½  Þ t c θðފ ¼ 0





                                                         .
                                                     t h,out , C h
                                                         .
                                          r           t c,in , C c
                                  s       q
                                         r 0
                                         t h,in
                                                        t c,out




          Fig. 3.9 Flow arrangement in a spiral heat exchanger, turns n¼3.
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