Page 223 - Introduction to Computational Fluid Dynamics
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                           CB908/Date
                                        0 521 85326 5
            0521853265c06
                     202
                                                                2D CONVECTION – COMPLEX DOMAINS
                                                      FUEL MASS FRACTION           May 25, 2005  11:10
                                      0.1
                                        0.2



                                                        VARIABLE Ψ
                                          0.9           0.3                   0.1
                                                                                       0.2
                                                                 0.5
                                          0.8

                                          0.7                                          0.6

                                                        TEMPERATURE
                                                      0.3
                                        0.9                                  0.1
                                                                                      0.2
                                                               0.5

                                           0.8                                        0.6
                                                    0.7

                            Figure 6.22. Scalar variables for a gas-turbine combustion chamber.



                            geometry of injection holes to achieve high levels of mixing, for determining exact
                            location of injection ports to minimize NO x formation, to achieve uniformity of
                            exit temperatures, and to take account of liquid-fuel injection from burners and
                            consequent fuel breakup into droplets.



                            Laminar Natural Convection in an Eccentric Annulus
                            Kuehn and Goldstein [37] measured heat transfer in horizontal eccentric cylinders
                            (radius ratio R o /R i = 2) containing nitrogen (Pr = 0.706). The inner cylinder is
                            maintained hot at temperature T h and the outer cylinder is maintained at colder
                            temperature T c . The positive vertical eccentricity  /L = 0.652, where L = R o −
                            R i . This problem has been computed by employing curvilinear grids by Karki and
                            Patankar [32] and Ray and Date [58] among many others. Here, the problem is
                            computed employing triangular (1,340 cells) as well as quadrilateral (1,320 cells)
                            meshes as shown in Figure 6.23. The symmetry about the vertical axis is exploited.
                            Corresponding to experimental conditions, the Rayleigh number Ra = g β (T h −
                                                 4
                                3
                            T c )L /(να) = 4.8 × 10 is chosen. At this value of Ra, the flow remains laminar
                            in all regions of the cavity between the cylinders.
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