Page 354 - Design and Operation of Heat Exchangers and their Networks
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340   Design and operation of heat exchangers and their networks


          solution for a gas-to-gas exchanger with neither fluid mixed was developed.
          Romie (1983) and Gvozdenac (1986, 1991) obtained the transient responses
          of crossflow exchangers to inlet temperature step changes. Kabelac (1989)
          proposed a lumped parameter cell model to calculate the transient responses
          of the liquid and gas outlet temperatures of a finned crossflow heat
          exchanger. The model allows for inlet temperature and mass flow rate per-
          turbations. Luo (1998) developed a dynamic dispersive model to predict the
          transient responses to arbitrary inlet temperature variations.



          7.2 Solution methods for dynamic behavior of heat
          exchangers

          The methods suitable for solving governing equations to obtain transient
          responses of heat exchangers can be divided into analytical and numerical
          methods. The Laplace-transform method is usually adopted in analytical
          solutions if the dynamic problem can be regarded as linear, while the
          finite-difference method is frequently applied in numerical solution. Some-
          times, Laplace-transform and finite-difference methods can be combined to
          obtain solution for transient responses of complex heat exchangers.



          7.2.1 Direct solution
          For some simple or simplified problems, the easiest method is to obtain the
          direct analytical solution. For example, the governing equations of the
          lumped parameter model can be linearized so that they can be changed into
          the following linear differential equations with constant coefficients:

                                   dT
                                      ¼ AT + B τ ðÞ                   (7.92)
                                    dτ
                                    τ ¼ 0 : T ¼ T 0                   (7.93)
          where T is the temperature vector of M streams and pieces of solid wall, A is
          an M M coefficient matrix, and B is the heterogeneous term. The solution
          of Eqs. (7.92), (7.93) has been given in Chapter 2 as follows:
                                 τ
                                ð
                     Rτ   1         R τ τ Þ   1  0  0
                                         0
                                     ð
              T ¼ He H T 0 +      He      H B τðÞdτ           ð 2:140Þ, (7.94)
                                 0
                 Rτ        r 1 τ  r 2 τ  r M τ
          where e  ¼diag{e ,e ,…,e }, r i (i¼1, 2, …, M) are the eigenvalues of
          the coefficient matrix A, and H is an M M matrix whose columns are the
          eigenvectors of the corresponding eigenvalues.
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