Coefficient of Discharge Calculator

Calculate coefficient of discharge (Cd), theoretical and actual flow rates for orifices, nozzles, weirs, and Venturi meters.

Calculate the coefficient of discharge (Cd), theoretical and actual flow rates for orifices, nozzles, weirs, and other flow devices.

m
kg/m³
Cd (Coefficient of Discharge)
0.610
Standard value for Sharp-edged orifice
Theoretical Velocity
9.905 m/s
v = √(2gH) = √(2 × 9.81 × 5)
Theoretical Flow Rate
9.905e-3 m³/s
Q_theo = A × v = 9.905 L/s
Actual Flow Rate
6.042e-3 m³/s
Q_actual = Cd × Q_theo = 6.042 L/s
Mass Flow Rate
6.030 kg/s
ṁ = ρ × Q = 998.00 × 6.042e-3
Reynolds Number
214,725
Re = ρvD/µ — Turbulent flow
Coefficient Breakdown: Cd = Cv × Cc
Cv (velocity coeff.)
0.629
Cc (contraction coeff.)
0.970
Cd (discharge coeff.)
0.610

Standard Discharge Coefficients

DeviceCdDescription
Sharp-edged orifice0.61Standard thin plate with sharp upstream edge
Well-rounded orifice0.98Smooth bell-mouth entrance
Short tube (L=2.5D)0.82Short pipe section, re-entrant
Borda (re-entrant)0.51Inward-projecting tube, vena contracta inside
Nozzle (converging)0.95Smooth converging nozzle
Venturi meter0.975Gradual contraction and expansion
Sluice gate0.61Vertical gate in open channel
V-notch weir (90°)0.58Triangular weir, 90° included angle
Rectangular weir0.62Rectangular notch, no end contractions
Planning notes, formulas, and examples

About the Coefficient of Discharge Calculator

The coefficient of discharge (Cd) is the ratio of actual flow rate to theoretical flow rate through an orifice or flow device. It accounts for energy losses from friction, turbulence, and flow contraction at the vena contracta that reduce the actual flow below the ideal prediction.

Torricelli's theorem gives the theoretical velocity through an orifice: v = √(2gH), where H is the head of fluid. The theoretical flow rate Q_theo = A × v. In practice, Cd ranges from about 0.51 (Borda re-entrant orifice) to 0.98 (well-rounded nozzle). A standard sharp-edged orifice has Cd ≈ 0.61.

This calculator computes flow rates from known Cd values or determines Cd from measured flow data. It includes a database of standard discharge coefficients for common flow devices, Reynolds number estimation, and coefficient breakdown into velocity (Cv) and contraction (Cc) components. Use the device table to compare sharp-edged orifices, nozzles, weirs, and Venturi meters when choosing a flow measurement setup.

When This Page Helps

Flow rate calculations for orifices and other devices require knowing Cd, which varies by geometry, Reynolds number, and installation conditions. Standard references list Cd for various devices, but applying them with correct units and determining theoretical flow requires multiple steps.

It gives both forward (Cd → flow rate) and inverse (measured flow → Cd) calculations, with a built-in database of standard coefficients. It is useful for hydraulic engineers, students, and anyone designing or calibrating flow measurement devices.

How to Use the Inputs

  1. Select the mode: calculate flow rate from known Cd, or find Cd from measured flow.
  2. Select the orifice or flow device type.
  3. Enter the orifice area and unit.
  4. Enter the fluid head (pressure head in meters of fluid).
  5. Optionally enter fluid density for mass flow calculations.
  6. For finding Cd, enter the measured volumetric flow rate.
Formula used
Q_actual = Cd × A × √(2gH). Cd = Q_actual / Q_theoretical. Cd = Cv × Cc. Torricelli: v = √(2gH). Re = ρvD/µ.

Example Calculation

Result: 6.04 × 10⁻³ m³/s actual flow (6.04 L/s)

v_theo = √(2 × 9.81 × 5) = 9.90 m/s. Q_theo = 0.001 × 9.90 = 9.90 × 10⁻³ m³/s. Q_actual = 0.61 × 9.90 × 10⁻³ = 6.04 × 10⁻³ m³/s = 6.04 L/s.

Tips & Best Practices

  • For flow measurement, use a Venturi meter (Cd ≈ 0.975) for lowest pressure loss, or an orifice plate (Cd ≈ 0.61) for lowest cost.
  • The upstream edge must be truly sharp for standard orifice Cd — any rounding increases Cd and causes measurement error.
  • In open channel flow, weir Cd values depend on the ratio of head to weir width (H/P ratio).
  • For compressible fluids (gases), an expansion factor Y must be applied: Q = Cd × Y × A × √(2ΔP/ρ).
  • Orifice Cd is remarkably stable over a wide range of Reynolds numbers (>10,000), making orifice plates popular flow meters.

Theory of Flow Through Orifices

Torricelli's theorem (1643) states that the velocity of fluid through an orifice is v = √(2gH), identical to the velocity of a body falling freely from height H. This assumes inviscid, incompressible flow — a good approximation for water at moderate pressures.

The actual flow is less than the theoretical value because: (1) the flow contracts at the vena contracta, reducing the effective area; (2) friction along the orifice walls dissipates some kinetic energy; (3) turbulence creates additional losses. The coefficient of discharge captures all three effects in a single empirical number.

Common Flow Measurement Devices

**Orifice plates** are thin plates with precisely machined holes, installed in pipelines. They are cheap but cause significant pressure loss (60-80% of differential pressure is not recovered). ISO 5167 provides detailed specifications for orifice flow measurement.

**Venturi meters** have a gradual contraction and expansion that minimizes losses. Cd ≈ 0.975 with only 10-20% unrecovered pressure loss. Used where permanent pressure loss must be minimized.

**Weirs** measure open channel flow. V-notch weirs are accurate for low flows; rectangular weirs handle higher flows. The Francis formula gives Q = 1.84 × L × H^1.5 for rectangular weirs.

Experimental Determination of Cd

To measure Cd experimentally, set up the orifice in a constant-head tank or pipeline with known area and head. Collect the discharged fluid in a graduated vessel over a measured time. Calculate Q_actual = Volume/Time, then Cd = Q_actual / (A × √(2gH)). Repeat at several head values to establish Cd vs Re behavior.

Sources & Methodology

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Frequently Asked Questions

  • Cd is the ratio of actual flow to theoretical flow through an opening. It accounts for losses due to friction, turbulence, and vena contracta (flow contraction). Cd = Q_actual / Q_theoretical, and it is always ≤ 1.