Page 291 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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SOME EXAMPLES OF FLUID FLOW AND HEAT TRANSFER PROBLEMS
                                           2.5 3  Re = 100                                    283
                                                Re = 200
                                          Local Nusselt number  1.5 1
                                                Re = 300
                                                Re = 500
                                            2

                                           0.5
                                            0
                                              5   10   15   20   25  30   35   40
                                                         Horizontal distance

                        Figure 9.23 Forced convection heat transfer downstream of a backward-facing step. Local
                        Nusselt number distribution on the hot wall for different Reynolds numbers


                           Figure 9.22 shows the temperature contours for all the different Reynolds numbers
                        considered. Previous studies indicate that the maximum heat transfer occurred close to
                        the reattachment length. The incompressible flow is attached to the wall from the inlet
                        until it reaches the step. The flow is detached from the bottom wall and recirculation
                        develops downstream of the step as shown previously for the non-isothermal case. The
                        flow reattaches itself to the bottom wall after the recirculation in the downstream portion
                        of the step. The location at which the reattachment takes place varies with the Reynolds
                        number. The higher the Reynolds number, the farther will be the reattachment point from
                        the step. The reattachment distances from the step are given in Figure 9.22. These values
                        are in close agreement with reported results (Kondoh et al. 1993).
                           The thermal action predominantly takes place downstream of the step in the bottom
                        portion of the channel. It may be observed that as the flow approaches the reattachment
                        point, the thermal boundary layer shrinks indicating a stronger temperature gradient in the
                        vicinity of the reattachment point and thus a higher heat transfer rate taking place close to
                        this point. This is clearly demonstrated in Figure 9.23 in which the local Nusselt number
                        is plotted along the hot wall downstream of the step. The local Nusselt number starts with
                        an almost zero value at the corner close to the step and increases smoothly to a maximum
                        value close to the reattachment point and then drops. It appears that the peak Nusselt
                        number value is calculated close to, but just after, the reattachment point. After reaching
                        the peak value, the local Nusselt number drops as the flow approaches the exit.



                        9.4 Thermal Conduction in an Electronic Package

                        Electronic packages (EP) are the integrated circuit (IC) carriers called components that are
                        used in the boards of all electronic systems. EP protect IC chips from a hostile environment,
                        communicate with other circuit boards and enhance the heat dissipation during operation.
                           In this section, an investigation has been carried out to find the thermal performance
                        of an electronic package, which is represented normally by the thermal resistance between
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