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Orifice Plate Flow Calculator (ISO 5167)

Calculate flow through a concentric square edged orifice plate from the measured differential pressure. The discharge coefficient is calculated with the Reader Harris/Gallagher equation from ISO 5167-2, iterated on Reynolds number.

ISO 5167-2Liquid and gasFlange, corner, D and D/2 tapsMass and volume flow
Mass flow32,680 kg/h
Volume flow (actual)32.739 m³/h
Volume flow144.14 US gpm
Beta ratio β0.5000
Discharge coefficient C0.6059
Expansibility ε1.0000
Pipe Reynolds number112,800
Pipe velocity1.107 m/s
How this result was calculated
  1. β = d ÷ D = 51.13 ÷ 102.26 = 0.5000
  2. C from the Reader Harris/Gallagher equation, iterated with Re = 112,800: 0.6059
  3. qm = C ÷ √(1 − β⁴) × ε × π/4 × d² × √(2 ΔP ρ) = 9.0777 kg/s
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The ISO 5167 Orifice Equation

ISO 5167-2 gives the mass flow through an orifice plate from the measured differential pressure and the geometry of the plate and pipe:

qm = C ÷ √(1 − β⁴) × ε × (π/4) × d² × √(2 × ΔP × ρ1)

Where qm is mass flow (kg/s), C is the discharge coefficient, β = d/D is the diameter ratio, ε is the expansibility factor (1 for liquids), d is the bore (m), ΔP is the differential pressure (Pa) and ρ1 is the upstream density (kg/m³).

C depends on β, the tapping arrangement and the Reynolds number, which itself depends on the flow. The calculator solves this loop by iteration, exactly as flow computers do.

Worked example

Water at 20 °C (998.2 kg/m³, 1.002 cP) flows in a 4 inch Sch 40 pipe (ID 102.26 mm) through a 51.13 mm bore (β = 0.5) with flange taps. At 250 mbar the calculator gives C = 0.606, a mass flow of about 32,700 kg/h and a volume flow of 32.7 m³/h (1.1 m/s in the pipe).

Key insight: because flow follows √ΔP, a quarter of the DP means half the flow. Size the DP range so normal flow sits around 70 % of maximum flow, which keeps accuracy good at low flow.
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Frequently Asked Questions

What is a typical orifice discharge coefficient?

For a sharp edged concentric orifice in turbulent flow C is close to 0.6, typically 0.598 to 0.61 depending on β, tappings and Reynolds number.

What beta ratio should I use?

ISO 5167-2 allows 0.1 to 0.75. Values of 0.4 to 0.65 are a good compromise between permanent pressure loss and required straight pipe length.

Does this calculator work for gas and steam?

Yes. Select Gas or steam and enter the absolute upstream pressure and isentropic exponent; the expansibility factor ε is then applied. Use density at flowing conditions.

How accurate is an orifice flow measurement?

With ISO 5167 geometry and installation, the uncertainty of C is about 0.5 % for most β ratios. Total installed uncertainty, including the DP transmitter and density, is typically 1 to 2 % of rate.

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