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  1. Home
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  4. /Orifice Flow Calculator

Orifice Flow Calculator

Last updated: March 28, 2026

Calculator

Results

Flow Rate (Q)

0.0062

m³/s

Flow Rate

372

L/min

Ideal Velocity

10

m/s

Actual Velocity

6.2

m/s

Ideal Flow Rate

0.01

m³/s

Results

Flow Rate (Q)

0.0062

m³/s

Flow Rate

372

L/min

Ideal Velocity

10

m/s

Actual Velocity

6.2

m/s

Ideal Flow Rate

0.01

m³/s

The Orifice Flow Calculator determines the volumetric flow rate of a fluid passing through an orifice plate, nozzle, or sharp-edged opening. Orifice plates are one of the most widely used flow measurement devices in industry, found in water treatment plants, oil refineries, chemical plants, and natural gas pipelines.

The calculator applies the orifice equation with a discharge coefficient to account for real-world losses from flow contraction and turbulence.

Visual Analysis

How It Works

The flow rate through an orifice is derived from Bernoulli's equation with a correction factor:

$$Q = C_d \cdot A \cdot \sqrt{\frac{2 \Delta P}{\rho}}$$

where:

  • Q — volumetric flow rate (m³/s)
  • C_d — discharge coefficient (dimensionless)
  • A — orifice area (m²)
  • ΔP — pressure difference across the orifice (Pa)
  • ρ — fluid density (kg/m³)

The ideal velocity through the orifice (without losses) comes from Torricelli's theorem:

$$v_{ideal} = \sqrt{\frac{2 \Delta P}{\rho}}$$

The discharge coefficient C_d accounts for two effects:

  • Velocity coefficient (Cv): friction losses reduce actual velocity below ideal
  • Contraction coefficient (Cc): the jet contracts to an area smaller than the orifice (vena contracta)

$$C_d = C_v \times C_c$$

Typical discharge coefficients:

  • Sharp-edged orifice: C_d ≈ 0.60–0.65
  • Well-rounded nozzle: C_d ≈ 0.95–0.99
  • Short tube (L/D ≈ 2–3): C_d ≈ 0.80–0.85
  • Borda (re-entrant) inlet: C_d ≈ 0.51

For precise metering applications, C_d is determined by calibration or from standards (ISO 5167) based on the beta ratio (orifice diameter / pipe diameter), Reynolds number, and tap location.

Understanding Your Results

The actual flow rate is the product of the discharge coefficient and ideal flow rate. The difference between ideal and actual values represents energy lost to flow contraction and turbulence at the orifice. A higher C_d means a more efficient orifice design with less energy loss. The calculator shows both ideal and actual velocities so you can assess the orifice efficiency.

Worked Examples

Water through a sharp orifice plate

Inputs

cd0.62
area0.000314
delta p20000
rho1000

Results

q m3s0.001231
q lmin73.86
v ideal6.3246
v actual3.9212
q ideal0.001986

A 20 mm diameter sharp-edged orifice (A = π×0.01² ≈ 0.000314 m²) with 20 kPa differential: ~74 L/min flow.

Tank drain through a rounded nozzle

Inputs

cd0.97
area0.002
delta p49050
rho1000

Results

q m3s0.019216
q lmin1152.96
v ideal9.9045
v actual9.6074
q ideal0.019809

A well-rounded nozzle (Cd = 0.97) draining a tank with 5 m head (ΔP ≈ 49 kPa) through 0.002 m² opening.

Frequently Asked Questions

For a standard sharp-edged orifice plate, use Cd ≈ 0.60–0.65. For a well-rounded nozzle (like an ISA 1932 nozzle), Cd ≈ 0.95–0.99. For critical applications, calibrate the orifice or use ISO 5167 calculations based on your specific geometry and Reynolds number.

An orifice plate creates a pressure drop proportional to the square of the flow rate. By measuring the differential pressure across the plate and knowing Cd, A, and ρ, you can calculate Q. Pressure taps are placed upstream and downstream (flange taps, corner taps, or D-D/2 taps).

The vena contracta is the point of minimum jet diameter downstream of an orifice, where the streamlines are most constricted. For a sharp-edged orifice, the vena contracta occurs about half a diameter downstream. The contraction coefficient Cc = A_vena/A_orifice ≈ 0.61–0.65.

For low-pressure-ratio gas flows (ΔP/P < 0.1), this incompressible equation gives reasonable results. For higher pressure ratios, compressible flow equations with an expansion factor (Y) must be used: Q = Cd·Y·A·√(2ΔP/ρ).

This comes from Bernoulli's equation where kinetic energy (½ρv²) equals pressure energy (ΔP). Solving for v gives v ∝ √ΔP, and since Q = Av, flow rate is also proportional to √ΔP. This square-root relationship is why orifice meters have limited rangeability (typically 3:1 to 5:1).

The beta ratio β = d/D is the orifice bore diameter divided by the pipe internal diameter. Typical values range from 0.2 to 0.75. Lower beta ratios give larger pressure drops and more accurate measurements but higher permanent pressure loss. Beta > 0.75 is generally avoided.

Sources & Methodology

ISO 5167-2:2003. Measurement of fluid flow by means of pressure differential devices — Orifice plates. Miller, R.W. (1996). Flow Measurement Engineering Handbook, 3rd Edition. McGraw-Hill.
R

Roboculator Team

The Roboculator Team explains calculations, planning tools, and practical formulas in clear language for real-life situations.

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