Orifice Plate Sizing Calculator

Professional ISO 5167 flow measurement and restriction orifice design tool. Calculate beta ratio, discharge coefficient (Cd), expansibility factor, and permanent pressure loss for liquid, gas, and steam systems.

This advanced engineering calculator sizes concentric, sharp-edged orifice plates per ISO 5167-1:2003 methodology. It features the Reader-Harris/Gallagher discharge coefficient correlation, iterative convergence solving, and comprehensive validation checks for choked flow, cavitation, and Reynolds number limits.

ISO 5167 Orifice Sizing

At flowing (upstream) conditions
Measured at operating temperature
Absolute pressure upstream of orifice
Absolute pressure downstream of orifice
At upstream conditions (P1, T)
1 cP = 0.001 Pa·s. Water @ 20°C ≈ 1.0 cP
Air: 1.4, Steam: 1.3
Z=1 for ideal gas
For cavitation check (liquid only)
Recommended: ≥10D (flange), ≥20D (corner)
Engineering Disclaimer: Results are for preliminary sizing and educational purposes. Final design must be validated against certified software and project standards per ISO 5167.
Orifice Bore Diameter (d)
mm
Beta Ratio (β = d/D)
Discharge Coeff. (Cd)
Expansibility Factor (ε)
Reynolds Number (Re)
Permanent Pressure Loss
bar
Estimated Uncertainty
View Iteration Convergence
Iter β Cd Qcalc Error %

Engineering Equations (ISO 5167-1:2003)

Orifice Flow Equation:

\[ q_m = \frac{C_d}{\sqrt{1-\beta^4}} \epsilon \frac{\pi}{4} d^2 \sqrt{2 \Delta P \rho} \]

Reader-Harris/Gallagher Cd (Flange Taps):

\[ C_d = 0.5961 + 0.0261\beta^2 - 0.216\beta^8 + 0.000521\left(\frac{10^6\beta}{Re}\right)^{0.7} + (0.0188 + 0.0063A)\beta^{3.5}\left(\frac{10^6}{Re}\right)^{0.3} \]

Where \( A = \left(\frac{19000\beta}{Re}\right)^{0.8} \). Tap-specific adjustments applied per ISO 5167-2.

Expansibility Factor (ε) for Compressible Flow:

\[ \epsilon = 1 - (0.351 + 0.256\beta^4 + 0.93\beta^8) \left[1 - \left(\frac{P_2}{P_1}\right)^{1/k}\right] \]

Permanent Pressure Loss (Crane TP-410):

\[ \Delta P_{perm} = \Delta P \times (1 - \beta^{1.9}) \]

Step-by-Step Engineering Calculation Methodology

  1. Unit Conversion & Validation: Convert all inputs to SI base units (m³/s, m, Pa, kg/m³, Pa·s). Verify positive, non-zero values.
  2. Initial Beta Estimate: Assume β = 0.5 (mid-range) to calculate initial orifice diameter: d = β × D.
  3. Reynolds Number: Calculate Re = ρVD/μ. ISO 5167 requires fully developed turbulent flow (Re ≥ 5000).
  4. Discharge Coefficient (Cd): Compute using the Reader-Harris/Gallagher equation with tap-specific adjustments.
  5. Expansibility Factor (ε): For gases/steam, correct for density change across the orifice. For liquids, ε = 1.0.
  6. Iterative Solving: Solve the orifice equation iteratively. Adjust d until |Qcalc - Q| < 0.001%.
  7. Validation Checks: Verify 0.1 ≤ β ≤ 0.75, check for choked flow (gas), cavitation (liquid), and sufficient upstream straight pipe length.

ISO 5167 Validity Limits for Orifice Plates

Parameter Minimum Maximum Preferred Range
Beta Ratio (β = d/D)0.100.750.20 – 0.60
Reynolds Number (Re)5,00010&sup7;> 20,000 (for β > 0.6)
Pipe Diameter D50 mm (2")No limit100 mm – 600 mm
Straight Length (Upstream)10D40D (depends on fittings)≥ 20D

⚠ Outside these limits: Measurement uncertainty increases significantly. Orifice plates are not recommended for β < 0.10 or > 0.75.

Engineering References & Standards

  • ISO 5167-1:2003 & ISO 5167-2:2003 — Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full.
  • Reader-Harris, M.J. & Gallagher, J.T. (1998). "New equation for the discharge coefficient of orifice plates." Flow Measurement and Instrumentation.
  • Crane Technical Paper No. 410 (latest ed.) — Flow of Fluids Through Valves, Fittings, and Pipe.
  • AGA Report No. 3 — Orifice Metering of Natural Gas (based on Reader-Harris/Gallagher).

Frequently Asked Questions

Why is iterative solving required for orifice sizing?

The discharge coefficient (Cd) depends on both the beta ratio (β) and Reynolds number (Re), which themselves depend on the unknown orifice diameter (d). Therefore, the orifice equation must be solved iteratively until convergence is achieved.

What is the Reader-Harris/Gallagher equation?

It is the internationally accepted correlation for orifice plate discharge coefficient, adopted by ISO 5167 and AGA Report No. 3. It provides an uncertainty of ±0.5% for β ≤ 0.6 and Re ≥ 10,000.

What is the difference between metered ΔP and permanent pressure loss?

Metered ΔP is the differential pressure measured at the tap locations (e.g., flange taps). Permanent pressure loss is the unrecovered pressure drop downstream, typically 60-80% of the metered ΔP depending on β. This is critical for pump and compressor sizing.

Can this calculator be used for custody transfer?

No. Custody transfer requires certified flow computers, strict adherence to installation standards, and calibration. This tool is designed for preliminary engineering sizing and educational purposes only.