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area for a poppet needle valve. (a) Entire popper valve. (b) Eetail on the throat flow area. (c) ISO symbol.

      The same abovementioned references collected empirical formulas for the orifice coefficient for various geometries and sizes. In many cases, it can be simply assumed that Ω1 ≫ ΩO: hence, the effects of velocity of approach are negligible and the value of Cf can be approximated with the coefficient of discharge Cd.

      For any specific geometric case, the orifice coefficient should be determined experimentally. Several authors report the theoretical evaluation of such a coefficient for different geometries, under the assumptions of frictionless, incompressible and irrotational flow. For example, Von Mises [40] provided the analytical results for the flow coefficient for several different orifice geometries. A comparison between Von Mises' results and experimental data is also extensively discussed in [36].

      As shown in [2, 32, 36], typical values for Cf are in the range of 0.6–0.8. In particular, 0.611 is the von Mises' theoretical value for a circular sharp edge orifice (Figure 4.1).

      The value of the Cf coefficient can be considered constant only for high Reynolds numbers (turbulent flow conditions). In case of laminar flow, the flow through an orifice can be solved analytically from Navier‐Stokes equations. In the case of a circular sharp edge orifice, the relationship becomes [41]

normal upper Delta p equals upper R Subscript italic turb Baseline dot upper Q squared

      Therefore,

      A fixed orifice is a hydraulic element characterized by a specific throat area ΩO; in a variable orifice, the area ΩO can vary according to the instantaneous geometric configuration.

      It is important to remark the square root dependence between Δp and Q highlighted in Figure 4.4. Because of this dependence, in order to double the flow across the orifice, it is necessary to increase the pressure by four times.

      The valve symbol includes different details when compared to the representation with basic orifices. For instance, in Figure 4.5, the information about the closed configuration (all ports completely closed ΩO = 0) is not provided by the basic orifice symbols.

      As explained in Chapter 3, the product Q · Δp represents hydraulic power. For the case of an orifice, this product represents the power dissipation introduced by the orifice itself:

      This power dissipation mostly goes into heat generation within the fluid. In most cases, the portion of heat exchange with the external environment (through the solid walls of the components in the system, including the orifice) is minimal and negligible. The temperature increase of the fluid can be calculated from the energy balance: