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Orifice Plate Flow Calculator (ISO 5167-2)

Calculate liquid flow through a concentric orifice plate from the measured DP. The workbook iterates the Reader Harris/Gallagher discharge coefficient and Reynolds number, and checks the ISO 5167-2 limits.

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  • Calculator sheet with a worked example
  • How to Use sheet with steps
  • 44 built in formulas, no macros
  • Yellow input cells, grey results
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  • Excel, Google Sheets and LibreOffice

Worked Example

These are the results of the example already filled in the workbook. Replace the yellow cells with your own data.

Pipe inside diameter D (mm)102.26
Orifice bore d (mm)63
Differential pressure (mbar)250
Density ρ (kg/m³)998.2
Viscosity μ (cP = mPa·s)1.002
Pressure tappingsFlange
Beta ratio β = d ÷ D0.6161
Velocity of approach factor E1.0809
L1 (upstream tap ÷ D)0.2484
L2' (downstream tap ÷ D)0.2484
M2' = 2 L2' ÷ (1 − β)1.2939

Iteration of discharge coefficient C and Reynolds number

IterationRe (assumed)Discharge coefficient CMass flow (kg/s)Re (calculated)
11,000,0000.6062614.4311179,323
2179,3230.6095914.5105180,309
3180,3090.6095814.5101180,305
4180,3050.6095814.5101180,305
5180,3050.6095814.5101180,305
6180,3050.6095814.5101180,305
7180,3050.6095814.5101180,305
8180,3050.6095814.5101180,305
Discharge coefficient C:0.60958  ·  Mass flow (kg/h):52,236.4  ·  Volume flow (m³/h):52.331  ·  Pipe Reynolds number:180,305  ·  Pipe velocity (m/s):1.770  ·  Permanent pressure loss (mbar):152.4  ·  ISO 5167-2 limits (β 0.1 to 0.75, D 50 to 1000 mm, d ≥ 12.5 mm, Re):OK
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About this Calculator

The orifice plate is still the most widely used flowmeter in process plants. Its discharge coefficient depends on Reynolds number, which depends on the flow you are trying to find, so the calculation must be iterated. This workbook does the iteration visibly, row by row, so the result can be checked and audited.

Basis: ISO 5167-2:2003 Reader Harris/Gallagher equation for C and permanent pressure loss; liquid service (ε = 1).

How to use

  1. Enter the measured pipe inside diameter and the orifice bore at operating temperature.
  2. Enter the DP in mbar and the liquid density and viscosity at flowing conditions.
  3. Choose the tapping arrangement; L1 and L2' follow automatically.
  4. The iteration table refines C and Re; the last row gives the result.
  5. Check that the ISO 5167-2 limits row shows OK.

Formulas used

  • β = d ÷ D, E = 1 ÷ √(1 − β⁴).
  • C from the Reader Harris/Gallagher equation (ISO 5167-2).
  • qm = C × E × (π ÷ 4) × d² × √(2 × ΔP × ρ).
  • Re = 4 qm ÷ (π μ D), fed back into C until it converges.

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Frequently Asked Questions

What is the Reader Harris/Gallagher equation?

The empirical equation in ISO 5167-2 that gives the discharge coefficient C of an orifice plate as a function of β, Reynolds number and tapping position.

Why does the orifice calculation need iteration?

C depends on Reynolds number, and Reynolds number depends on the flow being calculated. A few passes converge on the answer.

What are flange taps?

Pressure tappings 25.4 mm (1 inch) upstream and downstream of the plate faces, the most common arrangement.

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