Page 56 - Introduction to Computational Fluid Dynamics
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                        2.7 DEALING WITH NONLINEARITIES
                        Comparing Equations 2.56 and 2.57, leads to                May 25, 2005  10:49  35
                                                                                 −1
                                                      x i+1/2 − x i  x i+1 − x i+1/2
                                     k i+1/2 =  x i+1/2          +                 .       (2.58)
                                                          k i          k i+1
                        If the cell face were midway between the nodes then this equation would read as
                                                                     −1
                                                            1    1

                                                k i+1/2 = 2   +         .                  (2.59)
                                                           k i  k i+1
                           These equations suggest that the conductivity at a cell face should be eval-
                        uated by a harmonic mean to accord with the physics of conductance. We shall
                        regard this as a general practise and extend it to the case when thermal conduc-
                        tivity varies with temperature. Thus, instead of using either Equation 2.52 or 2.53,
                        Equation 2.58 will be used with k i and k i+1 evaluated in terms of temperatures
                        T i and T i+1 , respectively. Further, note that if conductivity is constant, k i+1/2 =
                        k i = k i+1 .



                        2.7.3 Boundary Conditions
                        In practical problems, three types of boundary conditions are encountered:

                        1. Boundary temperatures T 1 and/or T N are specified.
                        2. Boundary heat fluxes q 1 and/or q N are specified.
                        3. Boundary heat transfer coefficients h 1 and/or h N are specified.

                           Our interest in this section lies in prescribing these boundary conditions by
                        employing Su and Sp for the near-boundary nodes.



                        Boundary Temperature Specified
                        For the purpose of illustration, consider the i = 2 node, where T 1 is specified. Then,
                        Equation 2.43 will read as

                                     (AP 2 + Sp 2 ) T l+1  = AE 2 T l+1  + AW 2 T  l+1  + Su 2 ,  (2.60)
                                                  2           3          1

                        where Su 2 and Sp 2 are already updated to account for any source term. Equation
                        2.60 can be left as it is but we alter it via a three-step procedure in which we set
                                                   Su 2 = Su 2 + AW 2 T 1 ,

                                                   Sp 2 = Sp 2 + AW 2 ,

                                                  AW 2 = 0.0.                              (2.61)
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