Page 175 - Introduction to Computational Fluid Dynamics
P. 175

P1: IWV
                                        0 521 85326 5
                                                                                   May 20, 2005
                                                                                                12:28
                           CB908/Date
            0521853265c05
                     154
                                                                                  ζ
                                                         L       2D CONVECTION – CARTESIAN GRIDS




                                   T = 0                                         L



                             η                  U




                             T =  1  Y0

                                                           T = 0
                                          X0
                                        T =  1
                            Figure 5.24. Estimating false diffusion.


                                velocity u in (as shown) and temperature T in . The chamber walls and the lip
                                separating the inflow and outflow are adiabatic. Allow for the presence of a
                                buoyancy effect,

                                (a) Write the appropriate differential equations and the boundary conditions
                                   for all relevant variables.
                                (b) Carry out any necessary node tagging, defining clearly the convention
                                   used. For example, along AB, NTAGW (2, J) = 14 (say) to indicate the
                                   west adiabatic wall boundary.

                            12. Solve the problem of false diffusion discussed in the text for the case of θ = 45
                                degrees in which the boundary conditions are as shown in Figure 5.24. Take L =
                                100 and y 0 = x 0 = 2 S, where  S =  X =  Y. The situation is therefore
                                akin to that of a temperature source convected by U. Now, define orthogonal
                                coordinates ξ and η as shown. Use UDS. Obviously, the maximum temperature
                                T max will occur at η = 0 for each ξ. Now, locate the value of η 1/2 corresponding
                                to T/T max = 0.5. Hence, plot the computed results as T/T max versus η/η 1/2 for
                                different values of ξ/ S > 50. Show that the profies collapse on a single curve
                                                                              2
                                                    T                    η
                                                        = exp −ln(2)            ,
                                                   T max                η 1/2
                                                       0.5
                                where η 1/2 / S = (ξ/ S) . This equation is similar to the solution to the
   170   171   172   173   174   175   176   177   178   179   180