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alignment | left |
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q_{\rm ideal}= \epsilon \frac{\pi d^2}{4} \cdot \sqrt{\frac{1 \cdot \Delta p}{\rho \cdot (1-\beta^4)}} |
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The deviation from ideal estimation
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arise from fluid friction with choke elements and possible flow turbulence.
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The most popular engineering correlation covering all ISO 5167 tapping arrangements is given by Discharge coefficient @ model:
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C_d = C_{d, \infty}(\beta) + b(\beta) \cdot {\rm Re}^{-n} |
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Device | | | |
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Nozzle, ISA 1932 | 0.99 − 0.2262 · β4.1 | 1,708 − 8,936 · β + 19,779 · β4.7 | 1.15 |
Orifice, Corner Taps | 0.5959 + 0.0312 · β2.1 − 0.184 · β6 | 91.71 · β2.5 | 0.75 |
See also
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Physics / Fluid Dynamics / Pipe Flow Dynamics / Pipe Flow Simulation (PFS) / Pipeline Choke @model
Pipeline Engineering / Pipeline / Choke
Reference
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Stolz,J.,"A Universal Equation for the Calculation of Discharge Coefficient of Orifice Plates";, Proc. Flomeko 1978- Flow Measurement of Fluids,H. H. Dijstelbergenand E. A.Spencer(Eds), North-HollandPublishingCo.,Amsterdam(1978), pp 519-534
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