Page 194 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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CONVECTION HEAT TRANSFER
                        186


                                            Hot, vertical plate  Fluid circulation


                                                                            g








                                                               x 2





                                                                           x 1
                                   Figure 7.7  Natural convective flow near a hot, vertical plate


                           On introducing the above non-dimensional scales into the governing equations, we
                        obtain the non-dimensional form of the equations as follows:

                        Continuity equation
                                                      ∂u ∗  ∂u ∗
                                                        1     2
                                                          +     = 0                         (7.64)
                                                      ∂x ∗  ∂x ∗
                                                        1     2
                        x 1 momentum equation
                                                                                  !
                                                                               2 ∗
                                                                        2 ∗
                                     ∂u ∗    ∂u ∗    ∂u ∗    ∂p  ∗     ∂ u    ∂ u
                                       1  + u ∗  1  + u ∗  1  =−  + Pr    1  +   1          (7.65)
                                     ∂t  ∗  1  ∂x  ∗  2  ∂x  ∗  ∂x  ∗  ∂x ∗2  ∂x ∗2
                                               1       2       1         1      2
                        x 2 momentum equation
                                                                           !
                                                                 2 ∗
                                                                        2 ∗
                              ∂u ∗    ∂u ∗    ∂u ∗   ∂p ∗       ∂ u   ∂ u
                                2  + u ∗  2  + u ∗  2  =−  + Pr    2  +  2  + GrP r T  ∗    (7.66)
                                                                                   2
                              ∂t  ∗  1  ∂x ∗  2  ∂x  ∗  ∂x  ∗   ∂x ∗2  ∂x ∗2
                                        1       2      2          1      2
                        Energy equation
                                                                              !
                                                                          2
                                                                   2
                                          ∂T  ∗   ∂T  ∗   ∂T  ∗   ∂ T  ∗  ∂ T  ∗
                                              + u ∗ 1  + u ∗ 2  =      +                    (7.67)
                                          ∂t  ∗   ∂x ∗    ∂x  ∗   ∂x ∗2   ∂x ∗2
                                                    1       2       1       2
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