Page 189 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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CONVECTION HEAT TRANSFER
                        in the x 1 direction and
                                                                          2
                                                                                2

                                       ∂u 2    ∂u 2    ∂u 2     ∂p        ∂ u 2  ∂ u 2        181
                                    ρ      + u 1   + u 2    =−     + µ       +              (7.33)
                                        ∂t     ∂x 1    ∂x 2     ∂x 2     ∂x 2   ∂x 2
                                                                           1      2
                        in the x 2 direction. In vector notation, the momentum equations can be written as
                                              ∂u

                                            ρ    +∇.(u   ×   u) = ∇.[−pI + τ]               (7.34)
                                               ∂t
                        or, in indicial form
                                                                            !
                                                                         2
                                              ∂u i    ∂u i     ∂p       ∂ u i
                                           ρ      + u j    =−      + µ                      (7.35)
                                               ∂t     ∂x j     ∂x i     ∂x 2 i
                        Note that the above equation is applicable in any dimension.
                        7.2.3 Energy equation

                        The energy equation can be derived by following a procedure similar to the momen-
                        tum equation derivation. However, the difference here is that the temperature, or energy
                        equation, is a scalar equation. In order to derive this equation, let us consider the control
                        volume as shown in Figure 7.6. The energy convected into the control volume in the x 1
                        direction is

                                                       ρc p u 1 T x 2                       (7.36)
                           Similarly, the energy convected into the control volume in the x 2 direction is

                                                       ρc p u 2 T x 1                       (7.37)


                                                               ∂q 2
                                                        q +∆x 2   +  ....
                                                         2
                                                               ∂x 2
                                             ∂[rc u T]
                                                p 2
                                    rc u T +∆x 2     +  ....
                                     p 2
                                               ∂x
                                                 2
                                                                           ∂q 1
                                         q 1                         q +∆x 1  +  ....
                                                                     1
                                                                           ∂x 1
                                                          ∆x 2
                                                                          ∂[rc u T]
                                                                             p 1
                                         rc u T       ∆x          ru T +∆x 1      +  ....
                                          p 1
                                                                    1
                                                        1
                                                                             ∂x
                                                                              1
                                                  rc u T
                                                    p 2
                                                          q 2
                        Figure 7.6 Infinitesimal control volume in a flow field. Derivation of conservation of
                        energy
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