A ratio between actual volumetric flowrate through the orifice and ideal theoretical estimation:
C_d = \frac{q_{\rm real}}{q_{\rm ideal}} |
where
q_{\rm ideal}=\frac{\pi d^2}{4} \cdot \sqrt{\frac{1 \cdot \Delta p}{\rho \cdot (1-\beta^4)}} |
and
pressure drop on the choke, | |
choke narrowing ratio | |
orifice diameter | |
pipe diameter |
The deviation from ideal estimation arise from fluid friction with choke elements and possible flow turbulence.
The discharge coefficient is a function of a choke narrowing ratio and Reynolds number :
C_d = C_d(\beta, {\rm Re}) |
It can be estimated for popular choke types or tabulated in laboratory.
The most popular engineering correlation covering all ISO 5167 tapping arrangements is given by Stolz:
C_d = \frac{d_D}{d} + 0.3167 \cdot \left( \frac{d}{d_D} \right)^{0.6} + 0.025 \cdot \big [ \log {\rm Re} - 4 \big ] |
Physics / Fluid Dynamics / Pipe Flow Dynamics / Pipe Flow Simulation (PFS) / Pipeline Choke @model
Pipeline Engineering / Pipeline / Choke
Reference
Stolz,J.,"A Universal Equation for the Calculation of Discharge Coefficient of Orifice Plates";, Proc. Flomeko 1918- FlowM easurement of Fluids,H. H. Dijstelbergenand E. A.Spencer(Eds), North-HollandPublishingCo.,Amsterdam(1918).pp 519-534