0.0062
m³/s
372
L/min
10
m/s
6.2
m/s
0.01
m³/s
0.0062
m³/s
372
L/min
10
m/s
6.2
m/s
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.
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:
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:
$$C_d = C_v \times C_c$$
Typical discharge coefficients:
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.
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.
Inputs
Results
A 20 mm diameter sharp-edged orifice (A = π×0.01² ≈ 0.000314 m²) with 20 kPa differential: ~74 L/min flow.
Inputs
Results
A well-rounded nozzle (Cd = 0.97) draining a tank with 5 m head (ΔP ≈ 49 kPa) through 0.002 m² opening.
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.
Roboculator Team
The Roboculator Team explains calculations, planning tools, and practical formulas in clear language for real-life situations.
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