Page 143 - Design and Operation of Heat Exchangers and their Networks
P. 143

Steady-state characteristics of heat exchangers  131


              in which V is a (M+M M ) (M+M M ) matrix, whose nonzero elements are
                                  r j x
                            v ij ¼ h ij e ð i ¼ 1, 2, …, M; j ¼ 1, 2, …, MÞ  (3.316)
                                   ð
                             v ii ¼ 1 i ¼ M +1, M +2, …, M + M M Þ      (3.317)
                 The flow arrangement is defined by three matching matrices as follows:
                 Interchannel matching matrix G:Itis a (M+M M ) (M+M M ) matrix whose
              elements g ij are defined as the ratio of the thermal capacity rate flowing from
              channel j into channel i to that flowing through channel i.
                 Entrance matching matrix G :Itisa(M+M M ) N f matrix whose elements
                                       0
                0
              g ik are defined as the ratio of the thermal capacity rate flowing from the
              entrance of stream k to channel i to that flowing through channel i.
                                   00                                        00
                 Exit matching matrix G :Itisan N f  (M+M M ) matrix whose elements g ki
              are defined as the ratio of the thermal capacity rate flowing from channel i to
              the exit of stream k to that flowing out of the exit of stream k.
                 The energy balance at the entrances of M+M M channels yields
                                        M + M
                           N f           X M
                           X
                  _    0       _              _     00

                  C i tx ¼    C k i t in,k +  C j i t i x  ð i ¼ 1, 2, …, M + M M Þ
                       i                            i
                           k¼1           i¼1
                                                                        (3.318)
                                       _
                 Dividing Eq. (3.318) by C i , we obtain
                                   M + M
                         N f         X M
                        X

                     0       0                00
                  tx ¼      g t in,k +   g ij t i x  ð i ¼ 1, 2, …, M + M M Þ  (3.319)
                     i       ik               i
                         k¼1         i¼1
              or in the matrix form as
                                       0    0          00
                                   Θ x ðÞ ¼ G T in + GΘ xðÞ             (3.320)
                                                 T
                                                 ] is the inlet temperature vector
              in which T in ¼[t in, 1 , t in, 2 , …, t in, N f
                                                  0 T
                                                                           00 T
                               0
              of the exchanger; x ¼[x 1 , x 2 , …, x M ] and x ¼[x 1 , x 2 , …, x M ]
                                     0
                                         0
                                                               00
                                                                   00
                                                           00
              are the coordinate vectors of the channel inlets and outlets, respectively;
              Θ is the extended temperature vector;
                                                                     T
                    0
                                  0
                            0
                Θ x ðÞ ¼ t 1 x , t 2 x , ⋯, t M x 0                     (3.321)
                            1     2         M  , t M +1 , t M +2 , ⋯, t M + M M
                                                                      T
                   00
                                  00
                Θ x ðÞ ¼ t 1 x , t 2 x , ⋯, t M x 00                    (3.322)
                            00
                            1     2         M  , t M +1 , t M +2 , ⋯, t M + M M
                 0
              t i (x i ) is the temperature of the fluid stream at the inlet of the ith channel
                       00
               0
                                                         00
              x i ; and t i (x i ) is that at the outlet of the ith channel x i , which can be expressed
              from Eq. (3.312) as
                                      M
                                     X       0
                                 0         r j x
                                             i
                              t i x ¼    h ij e d j i ¼ 1, 2, …, MÞ     (3.323)
                                               ð
                                 i
                                      j¼1
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