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Exterior noise: Assessment and control     C HAPTER 22.1

           drawn back into the cylinder) particularly at low engine  where T is the temperature, s is specific entropy, h is
           speeds and this is important for stable idle. Combustion  specific enthalpy and v is specific volume. This can be
           instability manifests itself as a cylinder-to-cylinder  re-written as
           variation in IMEP. Low valve overlap is beneficial for
           low-speed torque. Twenty degree overlap is a typical  T  ds  ¼  dh     1 dp                (22.1.22)
           compromise for producting gasoline engines.            dx   dx   r dx
                                                              Substituting equation (22.1.22) into equation (22.1.19)
           22.1.3.10.3 On the flow through the intake valve    gives
           Knowledge of the gas dynamics at the intake valve is
                                                                         2
                                                                vu   v u
           useful to the refinement engineer. A non-conservative  vt  þ  vx 2  ¼ Tds   dh              (22.1.23)
           form of the conservation of momentum equation for
           a fluid in three dimensions is (Hirsch, 1988)
                                                              Now the total (or stagnation) enthalpy H is given as
              du                                                        u 2

             r   ¼ VpI þ V,s þ rf e               (22.1.17)     H ¼ h þ                               (22.1.24)
              dt                                                         2
           where                                              and substituting the differential of equation (22.1.24)
                                                              into equation (22.1.23)
                           vp   vp    vp
             grad p ¼ Vp ¼   i þ   j þ   k
                           vx   vy    vz                        vu  ¼ Tds   dH                        (22.1.25)
                                                                vt
             i; j; k are unit vectors
                                                              Now for the assumption of homentropic flow, equation
             I is the unit tensor
                                                              (22.1.25) reduces to:
             s is the viscous shear stress tensor
             f e is the external force vector                   vu
             p is pressure                                      vt  þ dH ¼ 0                          (22.1.26)
             r is density
             u is the velocity vector                         Now along a streamline the stagnation enthalpy is con-
             The total inertial term on the left-hand side of equa-  stant, so
           tion (22.1.17) can be re-written as the sum of linear,  vu
           kinetic and rotational forces:                          þ H ¼ H 0 ¼ constant               (22.1.27)
                                                                vt

              du      vu     u 2                              A scalar potential function f can be declared so that
             r   ¼ r    þ V        u   x          (22.1.18)
              dt      vt     2
                                                                u ¼ Vf                                (22.1.28)
           where x is known as the vorticity vector.                vf
             Simplifying the analysis to consider only one di-  u ¼  vx  in a 1-D model               (22.1.29)
           mension x, and neglecting viscosity effects, external
           forces and vorticity, equation (22.1.17) reduces to the  and thereby create what is known as a potential flow
           familiar non-linear inviscid Euler equation (see Appendix  model given by:
           21.1G for a derivation):
                                                                vf
                                                                   þ H ¼ H 0 ¼ constant               (22.1.30)
                                                                vt
             vu   v u 2      1 vp
               þ         ¼                        (22.1.19)                                                 1
             vt  vx 2        r vx                             For an ideal gas, where a is the speed of sound (m s )
                                                              and g is the ratio of specific heats c p /c v
             From the second law of thermodynamics (for instance       2
           Zemansky and Dittman (1997)):                        h ¼   a                               (22.1.31)
                                                                    g   1
             Tds ¼ dh   vdp                       (22.1.20)
                                                              and so using equation (22.1.24), equation (22.1.30) can
           or                                                 be written for flow along a streamline (or a Fanno line) as:

               ds   dh    dp                                    vf    a 2   u 2   a 2 0
             T   ¼      v                         (22.1.21)        þ      þ    ¼                      (22.1.32)
              dx    dx    dx                                    vt   g   1  2    g   1


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