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Orifice Plate Sizing Calculator (AS 2360.1.1 / ISO 5167)

Data Input

Process Conditions

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Orifice Sizing

Reynolds Number (ReD):-
Beta Ratio (β):-
Expansion Factor (ε₁):-
Discharge Coeff. (C):-
Calculated Orifice Diameter (d):-
Overall Pressure Loss (Δω):-

Range of Validity Checks

Pressure Ratio (τ ≥ 0.75):-
Orifice Diameter (d ≥ 12.5mm):-
Pipe Diameter (50-1000mm):-
Beta Ratio (0.2 ≤ β ≤ 0.75):-
Reynolds Number Limit:-
Flow is Subsonic:-

Technical Notes

Variable Definitions

  • D: pipe internal diameter (m) (computed from DN and schedule).
  • d: orifice bore diameter (m) (calculated).
  • β: beta ratio = d/D.
  • : mass flow rate (kg/s).
  • ρ: upstream density (kg/m³), μ: dynamic viscosity (Pa·s).
  • P₁: upstream absolute pressure (Pa), ΔP: differential pressure (Pa).
  • C: discharge coefficient (–) from ISO 5167-type correlation.
  • ε₁: expansibility (expansion) factor for gases (–).
  • ReD: Reynolds number based on pipe diameter.

Formulas / Logic

  • Reynolds number: ReD = 4ṁ / (π μ D).
  • Flow equation (orifice): rearranged to solve for d iteratively: ṁ = C ε₁ (π d²/4) √(2 ρ ΔP) / √(1−β⁴).
  • Discharge coefficient: ISO 5167-style correlation using β, ReD, and tap locations (L1, L2).
  • Gas expansibility: screening form: ε₁ = 1 − (0.41 + 0.35β⁴)·(ΔP/(k·P₁)) (bounded to ≥ 0).
  • Permanent pressure loss: estimated as a function of C, β, and ΔP (screening).
  • Sonic check (gas): a = √(k·P₁/ρ), compare with orifice velocity to flag subsonic flow.
This is a sizing / screening calculator. Final design should consider plate thickness, edge sharpness, vena contracta, tap details, installation straight lengths, and meter uncertainty per the standard.

Assumptions / Notes

  • Inputs are assumed at upstream flowing conditions. For gases, ensure absolute pressure and consistent density.
  • Validity limits shown are conservative checks. ISO 5167 validity depends on β, D, tapping, and Re and should be confirmed for the final selected geometry.
  • Multiphase flow, non-Newtonian fluids, pulsating flow, and significant compressibility effects beyond the expansibility factor are outside this tool’s scope.

Standards / References

  • ISO 5167 — Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full.
  • AS 2360.1.1 (where applicable) — orifice plate / differential pressure device practice.
  • Common engineering references: ISO 5167 supporting correlations (Reader-Harris/Gallagher), and DP metering handbooks.
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