Summary

The discharge coefficient is a dimensionless number used to characterise the flow and pressure loss behaviour of nozzles and orifices in fluid systems. Orifices and nozzles are typically used to deliberately reduce pressure, restrict flow or to measure flow rate. This article gives typical values of the discharge coefficient for common orifice and nozzle designs.

Definitions

CdC_{d}:Discharge Coefficient
Cd,∞C_{d,\infty}:Discharge Coefficient at infinite Reynolds number
D1D_{1}:Full pipe diameter
D0D_{0}:Constricted diameter (mm)
KK:Resistance Coefficient
ReRe:Reynolds Number (measured at full pipe diameter and velocity)
β\beta:Area Ratio ( Do/D1D_{o}/D_{1} )

Introduction

There are two distinct uses for nozzles and orifice plates. The first is to restrict flow where high accuracy is generally not important and the second is flow measurement where calculation accuracy is critical.

For the purpose of flow restriction an orifice plate is typically used and it is generally acceptable to use typical values of the discharge coefficient as presented in this article for the orifice sizing calculation.

Orifice Plate Dimensions

For the purpose of flow measurement either an orifice or nozzle may be used and the accuracy of the discharge coefficient has greater importance. For orifice plate installation the discharge coefficient will vary depending on the location of the pressure tappings. Common arrangements are:

  • Corner tappings: Tapping points are at the flange.
  • Flange tappings: Tapping points are 1" upstream and downstream of orifice plate in the flanges.
  • 2.5D and 8D tappings: Tapping points are 2.5 pipe diameters upstream and 8 pipe diameters downstream.
  • D and 1/2 D tappings: Tapping points are 1 pipe diameter upstream and half a pipe diameter downstream.

Corner and Flange Orifice Tappings

Downstream and Upstream Orifice Tappings

Other devices with high accuracy and greater pressure recovery exist such as ASME, ISA, Venturi Nozzles and Lo Loss Tubes. When using these devices the vendor should be consulted for the exact discharge coefficient.

Discharge Coefficient Values

Relationship to Resistance coefficient KK

The discharge coefficient may be directly related to the resistance coefficient via the follow equation:

K=1Cd2 K = \frac{1}{C_{d}^{2}}

Typical Values for Discharge Coefficient CdC_{d}

For simple pressure loss or flow rate calculations where high accuracy is not critical the following typical values may be used:

Equipment Typeβ\beta minβ\beta maxCdC_{d}
Orifice Plate, Thin sharp edged--0.61
Venturi Nozzle, Machined0.40.750.995
Venturi Nozzle, Rough Welded Sheet Metal0.40.700.985
Venturi Nozzle, Rough Cast0.30.770.984

Precise Relationships for Discharge Coefficient

Where a higher degree of accuracy is required, such as for flow rate measurement, the relationships below may be used.

Cd=C∞+bRen C_{d}=C_{\infty}+\frac{b}{Re^{n}}

Values for C∞C_{\infty} , bb and nn are presented below. Dimensions in millimeters.

DeviceCd,∞C_{d,\infty}bbnn
Venturi Nozzle, Machined Inlet0.9950.9950000
Venturi Nozzle, Cast Inlet0.9840.9840000
Venturi Nozzle, Welded Sheet Metal0.9850.9850000
Lo-Loss Tube1.005−0.471β+0.564β2−0.514β31.005-0.471\beta+0.564\beta^{2}-0.514\beta^{3}0000
Nozzle, ASME Long Radius0.99750.9975−6.53β0.5-6.53\beta^{0.5}0.50.5
Nozzle, ISA 19320.9900−0.2262β4.10.9900-0.2262\beta^{4.1}(−0.00175+0.0033β4.15)×106.9(-0.00175+0.0033\beta^{4.15})\times10^{6.9}1.151.15
Orifice, Corner Taps0.5959+0.0312β2.1−0.184β80.5959+0.0312\beta^{2.1}-0.184\beta^{8}91.71β2.591.71\beta^{2.5}0.750.75
Orifice, Flange Taps ( 50.8≤D1≤58.450.8\leq D_{1} \leq58.4 )0.5959+0.0312β2.1−0.184β8+0.039β41−β4−0.856β3Do0.5959+0.0312\beta^{2.1}-0.184\beta^{8}+0.039\frac{\beta^{4}}{1-\beta^{4}}-0.856\frac{\beta^{3}}{D_{o}}91.71β2.591.71\beta^{2.5}0.750.75
Orifice, Flange Taps ( D1≥58.4D_{1}\geq58.4 )0.5959+0.0312β2.1−0.184β8+2.286β4Do(1−β4)−0.856β3Do0.5959+0.0312\beta^{2.1}-0.184\beta^{8}+2.286\frac{\beta^{4}}{D_{o}(1-\beta^{4})}-0.856\frac{\beta^{3}}{D_{o}}91.71β2.591.71\beta^{2.5}0.750.75
D1D_{1} and D1/2D_{1}/2 taps0.5959+0.0312β2.1−0.184β8+0.039β41−β4−0.015840.5959+0.0312\beta^{2.1}-0.184\beta^{8}+0.039\frac{\beta^{4}}{1-\beta^{4}}-0.0158491.71β2.591.71\beta^{2.5}0.750.75
2.5D12.5D_{1} and 8D18D_{1} taps0.5959+0.461β2.1−0.48β8+0.039β41−β40.5959+0.461\beta^{2.1}-0.48\beta^{8}+0.039\frac{\beta^{4}}{1-\beta^{4}}91.71β2.591.71\beta^{2.5}0.750.75

Further Reading