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Governing equations of fluid mechanics  83

          Eqn  (2.46) to simplify Eqn  (2.58a,b), Eqns (2.62) and (2.63) apply equally well  to
          compressible flow. In order to show this to be true, it is necessary to allow density to
          vary in the derivation of Term (i) and to simplify it using the compressible form of the
          continuity Eqn (2.45).

          2.6.1  The Euler equations

          For some applications in  aerodynamics it can be an acceptable approximation to
          neglect the viscous stresses. In this case Eqns (2.66) simplify to
                                 (Z  ;:  ;;)
                                p  -++-+v-        =pg,--   aP              (2.68a)
                                                         ax
                                   dv   dv               dP
                                                  -pg
                                p  -++-+v-    dv)-    Y  ay                (2.68 b)
                                                       --
                                 ( at   ax    ay
          These  equations  are  known  as  the  Euler  equations.  In  principle,  Eqns  (2.68a,b),
          together with the continuity Eqn (2.46), can be solved to give the velocity components
          u and v and pressurep. However, in general, this is difficult because Eqns (2.68a,b) can
          be regarded as the governing equations for u and v, but p does not appear explicitly in
          the continuity equation. Except for special cases, solution of the Euler equations can
          only be  achieved  numerically using a  computer. A  very  special and  comparatively
          simple case is irrotational flow (see Section 2.7.6). For ths case the Euler equations
          reduce to a single simpler equation - the Laplace equation. This equation is much more
          amenable to analytical solution and this is the subject of Chapter 3.

            2.7  Rates of strain, rotational flow and vorticity


          As they stand, the momentum Eqns (2.66) (or 2.67), together with the continuity Eqn
          (2.46) (or 2.47) cannot be solved, even in principle, for the flow velocity and pressure.
          Before this is possible it is necessary to link the viscous stresses to the velocity field
          through a constitutive equation. Air, and all other homogeneous gases and liquids,
          are closely approximated by the Newtonian fluid model. This means that the viscous
          stress is proportional to the rate of strain. Below we consider the distortion experi-
          enced by an infinitesimal fluid element as it travels through the flow field. In this way
          we can derive the rate of strain in terms of velocity gradients. The important  flow
          properties, vorticity and circulation will also emerge as part of this process.

          2.7.1  Distortion of fluid element in flow field
          Figure 2.24 shows how a  fluid element is transformed  as it moves through a flow
          field. In general the transformation  comprises the following operations:
           (i)  Translation - movement from one position to another.
          (ii)  DilationlCompression ~  the shape remains invariant, but volume reduces or increases.
              For incompressible flow the volume remains invariant from one position to another.
          (iii)  Distortion - change of shape keeping the volume invariant.
              Distortion  can  be  decomposed  into  anticlockwise  rotation  through  angle
              (a - p)/2 and a shear of angle (a + /3)/2.

          The angles a and p are the shear strains.
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