Orifice, Nozzle, Venturi:

In general flow coefficient, K, is given as

where Cc º Avena contracta/Athroat and Cv = V2 actual/V2 ideal

For nozzles and venturi meters, the section of minimum flow area is located at the throat.  There is no vena contracta and Cc = 1.  For these cases

where β is given as

The factor 1/(1 - β4)1/2 is called the "velocity of approach" factor.

Some of the pressure is recovered in the diverging section.  An expansion factor Y is introduced to give a better representation of the velocity.

For liquids, expansion factor (Y) is 1. 

For gases, expansion factor (Y), can be obtained using Figure 4.1 (Crane Fig. A-20).  Figure 4.1 presents Y for various values of (1 - r)/k and β2, where r is defined as

This equation can be rearranged to the following form:

Nozzles:  If the flow of a gas is occurring under critical conditions, then pressure ratio (r) values for compressible flow through nozzles and venturi tubes is given in Figure 4.2 (Crane A-21).  Pressure ratio r is plotted as a function of k and b.  Now values of r and β can be utilized in Figure 4.1 (Crane A-20) to obtain expansion factor (Y).

Orifice Meters:  The velocity through an orifice can be computed knowing the value of orifice coefficient CV, which is a function or Reynolds number.  The expansion factor for liquids is 1.0, whereas for gases it is found from the following equation.

Module:

h (Manometer reading, in)
Pi (Inlet pressure, psi)
delta_P (Pressure drop, psi)
ρ (Density, lb per ft3)
μ (Viscosity, cP)
d1 (Diameter of flow meter, in)
d2 (Pipe diameter, in)
C_v (Velocity coefficient)
Y (Expansion coefficient)
T (Temperature, deg F)
Flow Meter Orifice Nozzle Venturi

Fluid Liquid Gas