MachineCalcs

Orifice Flow Rate Calculator

Estimate incompressible liquid flow through an orifice from diameter, pressure drop, discharge coefficient and fluid density, with velocity and mass-flow output.

Calculator

Actual orifice bore diameter.

mm

Pressure difference across the orifice.

bar

Accounts for contraction and losses. Sharp-edged liquid orifices are often near 0.60-0.65.

Density at operating temperature.

kg/m³

Results

Default result
Edit inputs
Orifice flow rate(Q)
41.36L/min

Q = Cd x A x sqrt(2dp/rho).

Also computed

Effective jet velocity(Cd*v_ideal)8.777m/s

Ideal velocity(sqrt(2dp/rho))14.16m/s

Orifice area(A)78.54mm²

Mass flow(m_dot)0.688kg/s

Method notes 2 notes
  • Liquid orifice flow uses Q = Cd*A*sqrt(2*dp/rho). Cd must match the orifice geometry and Reynolds-number range.
  • This incompressible screen is not for choked gas flow, two-phase flow, cavitating restrictions, control-valve sizing or calibrated custody-transfer metering.

Liquid orifice flow uses Q = Cd*A*sqrt(2*dp/rho), where A = pi*d²/4, dp is pressure drop, rho is fluid density and Cd accounts for contraction and loss. This calculator returns volumetric flow, effective jet velocity, ideal velocity, orifice area and mass flow for incompressible liquid restrictions. It is not a choked gas, cavitation or control-valve sizing model.

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How to use this calculator

  1. Enter orifice diameter. Use the actual bore diameter of the restriction.
  2. Enter pressure drop. Use the differential pressure across the orifice.
  3. Set Cd and density. Use a discharge coefficient and liquid density that match the installation.
  4. Review flow and velocity. Check volumetric flow, mass flow and jet velocity for the restriction.

How it works

Area comes from the orifice diameter:

A = pi x d^2 / 4

For an incompressible liquid, ideal velocity comes from Bernoulli:

v_ideal = sqrt(2 x dp / rho)

The discharge coefficient derates that ideal flow:

Q = Cd x A x sqrt(2 x dp / rho)

If the restriction is part of a pipe system, pair this with the pipe flow pressure drop calculator and pump NPSH calculator.

Worked example

Verified against the live calculator

A 10 mm orifice with 1 bar pressure drop, Cd = 0.62 and water density near 998 kg/m^3 flows about 41.4 L/min, or about 10.9 gpm.

Frequently asked questions

How is orifice flow rate calculated?

For incompressible liquid flow, Q = Cd x A x sqrt(2 x pressure drop / density). The discharge coefficient accounts for losses and contraction.

What discharge coefficient should I use?

A sharp-edged liquid orifice is often around 0.60 to 0.65, but the correct value depends on geometry, Reynolds number and calibration data.

Can I use this for air or gas flow?

No. Compressible gas flow can choke and needs a gas-specific equation, pressure ratio, temperature and gas properties.

Is this a control valve sizing calculator?

No. It is a fixed-orifice liquid screen. Control valves need valve Cv/Kv data, cavitation/flashing checks and manufacturer sizing rules.

Method & assumptions

  • Uses incompressible liquid flow with a user-entered discharge coefficient.
  • Pressure drop is the differential across the orifice, not the total pump discharge pressure.
  • Does not handle choked gas flow, steam, two-phase flow, cavitation, flashing, very low Reynolds number correction or custody-transfer metering.
  • Use calibrated or manufacturer data for safety-critical restrictors, hydraulic controls and flow measurement.
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