Large Diameter Orifice for Gas Flow calculation is mobiledevicefriendly as of February 3, 2015
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Units in large bore orifice flow meter for gas flow calculation: C=degrees Celsius, cm=centimeter, cP=centipoise,
cSt=centistoke, F=degrees Fahrenheit, cfm=cubic feet per minute, cfs=cubic feet per
second, ft=foot, g=gram, hr=hour, in=inch, K=degrees Kelvin, kg=kilogram, lb=pound,
m=meters, mbar=millibar, min=minute, mm=millimeter, N=Newton, Pa=Pascal, psi=pound per
square inch, R=degrees Rankine, s=second, scfm=standard cfm, std=standard.
Types of Pressure Taps for Orifices
Topics: Introduction Equations
Discharge Coefficient Variables
Validity and Discussion Error Messages References
Introduction
Orifice flow meters are used to determine a liquid or gas flow rate by measuring the
differential pressure (P_{1}  P_{2}) across the orifice plate.
Orifice meters are typically less expensive to install and manufacture than the other
commonly used differential pressure flow meters; however, nozzle
and venturi flow meters have the advantage of lower pressure
drops. Equations for orifice meters have the advantage of no Reynolds Number upper
limit for validity.
An orifice flow meter is typically installed between flanges connecting two pipe
sections (flanges are not shown in the above drawings). The three standard pressure
tapping arrangements are shown in the drawings; the location of the pressure taps affects
the discharge coefficient somewhat. Flange pressure taps penetrate the flange and
are at a standard distance of 1 inch (2.54 cm) from either side of the orifice. For
corner taps or D and D/2 taps, the pressure tap locations are as shown.
Orifices are typically less than 0.05D thick. For exact geometry and
specifications for orifices, see ISO (1991) or ASME (1971).
The ASME and ISO have been working on guidelines for orifices since the early 1900s.
The organizations have the most confidence in orifice accuracy when the Reynolds number
exceeds 10^{5}, though Reynolds numbers as low as 4x10^{3} are valid for
certain d/D ratios as discussed below. The calculation above is for flow of gases.
For liquid flow through orifices, please visit our orifice calculations for
liquids: Pipe diameter < 5 cm or pipe diameter > 5 cm. Gas flow calculations include an
expansibility factor (e), which is not present in the liquid calculation. The
expansibility factor accounts for the effect of pressure change on gas density as gas
flows through the orifice. LMNO Engineering also has an orifice calculation for gas flow in pipes less than 5 cm
diameter.
Equations
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The calculations on this page are for orifices carrying a gas as described in ISO (1991 and 1998).
Discharge Coefficient (ISO, 1998)
Corner Pressure Taps: L_{1} = L'_{2} = 0
D and D/2 Pressure Taps: L_{1} = 1 and L'_{2} = 0.47
Flange Pressure Taps: L_{1} = L'_{2} = 0.0254/D where D is in
meters
Variables
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Dimensions: F=Force, L=Length, M=Mass, T=Time, t=temperature
Validity and Discussion
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Discharge Coefficient:
For all types of pressure taps: d ≥ 1.25 cm, 5 cm ≤ D ≤ 1
m, 0.1 ≤ d/D ≤ 0.75
For Corner Pressure Taps or D and D/2 Pressure Taps:
Re_{D} ≥ 4000 for 0.1 ≤ d/D ≤
0.5 and Re_{D} ≥ 16,000(d/D )^{2} for
d/D>0.5
For Flange Pressure Taps: Re_{D} ≥ 4000 and Re_{D}
≥ 170,000 D (d/D )^{2} where D is in meters
The calculation does not provide results if these values are out of range.
Expansibility:
The equation shown above for expansibility, e, is valid for P_{2}/P_{1}
≥ 0.75. Our calculation gives a warning message if P_{2}/P_{1}
< 0.75, but still computes answers.
Builtin Properties for Certain Gases:
To provide ease of use, our calculation has properties of some gases builtin to the
calculation. The user can select Air, Carbon dioxide, Hydrogen, Methane (natural
gas), Nitrogen, or Oxygen. The density is automatically computed using the ideal gas
law based on the upstream pressure and temperature entered. The dynamic viscosity is
a function of temperature and uses the methodology shown on our Gas
Viscosity page. The isentropic exponent, K, is based on the specific
heat ratio. For methane, the dynamic viscosity value shown in the calculation is
valid for 0^{ o}F < T < 1000^{ o}F. If T<0^{
o}F, then the viscosity value shown and used in the computation is the viscosity at 0
^{o}F. If T>1000^{ o}F, then the viscosity value shown and used
in the computation is the viscosity at 1000 ^{o}F (0^{ o}F is 17.8 ^{o}C
and 1000 ^{o}F is 537.8 ^{o}C). For all other gases shown in the
dropdown menu, there is no temperature limitation on the validity of the viscosity.
Dynamic viscosity is essentially independent of pressure.
If you know that your density, viscosity, or isentropic exponent is significantly
different than the value shown in the calculation, then you can select "User enters P_{1},
density, viscosity, K" and enter these values manually. Also, if the gas is not
listed in our dropdown menu, then you can select "User enters P_{1},
density, viscosity, K" and enter these values manually. K must be >
1. Additionally, values for K can be found in Weast (1985,
p. F11), Perry and Green (1984, p. 3144), and other sources.
Note that our calculation prior to February 2003 included helium as a gas in the
dropdown gas menu, and the viscosities for the gases were set at 20 ^{o}C.
Now, the viscosity variation with temperature is included, but helium was removed because
it doesn't have a simple viscosity relationship with temperature.
ISO Pipe Roughness Recommendation:
ISO recommends that in general k/D ≤ 3.8x10^{4} for
Corner Taps and k/D ≤ 10^{3} for Flange or D and D/2
pressure taps. k is the pipe roughness.
Our calculation does not check this.
Pressure Loss:
w is the static pressure loss occurring from a distance of approximately D
upstream of the orifice to a distance of approximately 6D downstream of the
orifice. It is not the same as differential pressure. Differential pressure is
measured at the exact locations specified in ISO (1991) (shown in the above figures).
Minor Loss Coefficient:
K_{m} is computed to allow you to design pipe systems with orifices and
incorporate their head loss. Head loss is computed as h=K_{m}V^{2}_{pipe}/2g.
Standard Volumetric Flow Rate:
Standard volumetric flow rate, Q_{s}, is the volumetric flow rate
computed at standard pressure and temperature, P_{std} and T_{std}
(shown above in variables). Actual flow rate, Q_{a},
is computed at the gas's actual pressure and temperature. Q_{s} is
useful to users who need to compute (or input) standard flow rate; often pump curves and
flow measurement devices provide standard, rather than actual, flow rate. The
advantage of using standard flow instead of actual flow is that the same device (or pump
curve) can be used for a gas at various temperatures and pressures without recalibrating
for an infinite range of actual pressures and temperatures. The user can easily
convert standard to actual flow rate if the actual temperature and pressure of the gas are
known; our calculation does this automatically.
Error Messages given by calculation
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"P_{2}/P_{1}<0.75. Out of range". The
equation for expansibility, e, is only valid for P_{2}/P_{1}≥0.75.
This is a just a warning message; all variables are computed.
For the following error messages, only some variables are computed. For example if
throat diameter (d) is to be computed, then pressure ratio, expansibility, pipe area, pipe
velocity, Re_{D}, and some other variables will be computed and shown.
However, if Re_{D} is out of range for C to be valid, then C and d (and anything
depending on d  such as throat area and throat velocity) will not be computed. If
an error message is shown and you think your input is correct, be sure to check that you
have selected the correct units for your entries.
"Infeasible input". While none of the inputs alone are out of
range, they collectively result in a physically infeasible situation.
"P_{1} and T (abs) must be >0". Absolute pressure or
absolute temperature was entered as zero or negative. If temperature was entered in
C or F, it was internally converted to absolute temperature.
"P_{1},D, T(abs), Dens, Visc must be >0". Pipe diameter,
density, viscosity, absolute pressure, and/or absolute temperature was entered as zero or
negative.
"K must be >1". Isentropic exponent was entered as ≤ 1.
"d/D must be <1". Orifice diameter cannot exceed pipe
diameter.
"M or Q, and d must be >0". Mass flow rate, volumetric flow
rates, and/or orifice diameter were entered as zero or negative.
"d, D, d/D, or Re_{D} out of range". At least one of
these variables is out of the range of validity for the discharge
coefficient.
"Δp and d must be >0". Cannot enter pressure difference or
d ≤0.
"Δp must be < P_{1}". Differential pressure cannot
exceed P_{1}; this would cause P_{2}(absolute) to be <0 which is
impossible.
"d/D out of range", "D out of range", "d
out of range" These must be in the range of validity
shown above.
"M or Q, and Δp must be >0". Mass flow rate, volumetric
flow rates, and/or differential pressure were entered as zero or negative.
"Re_{D} out of range". Re_{D} must be in range of validity shown above.
"Re_{D} will be too small", "Re_{D} will be
out of range", "d/D will be out of range", "d will
be <0.0125 m", "d/D will be < 0.1", "d/D will
be > 0.75". Input values result in variables that will be out of the range of validity.
• Try the simpler orifice calculation on our Bernoulli page if your parameters are out of range. It is
not as accurate, but won't give "parameter out of range" error messages.
References
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American Society of Mechanical Engineers (ASME). 1971. Fluid meters: Their
theory and application. Edited by H. S. Bean. 6ed. Report of ASME
Research Committee on Fluid Meters.
International Organization of Standards (ISO 51671). 1991. Measurement of
fluid flow by means of pressure differential devices, Part 1: Orifice plates, nozzles, and
venturi tubes inserted in circular crosssection conduits running full. Reference
number: ISO 51671:1991(E).
International Organization of Standards (ISO 51671) Amendment 1. 1998.
Measurement of fluid flow by means of pressure differential devices, Part 1: Orifice
plates, nozzles, and venturi tubes inserted in circular crosssection conduits running
full. Reference number: ISO 51671:1991/Amd.1:1998(E).
Perry, R. H. and D. W. Green (editors). 1984. Perry's Chemical Engineers'
Handbook. McGrawHill Book Co. 6th ed.
Weast, R. C. (editor). 1985. CRC Handbook of Chemistry and Physics.
Chemical Rubber Company. 65th ed.
© 20002015 LMNO Engineering, Research, and
Software, Ltd. All rights reserved.
Please contact us for consulting or other questions.
LMNO Engineering, Research, and Software, Ltd.
7860 Angel Ridge Rd. Athens, Ohio 45701 USA Phone and
fax: (740) 5921890
LMNO@LMNOeng.com http://www.LMNOeng.com
August 25, 2015: Made text fields narrower to show 8 significant figures rather than 16. Calculation still uses double precision internally.

To:
LMNO Engineering home page (more calculations)
Other Flow Meter Calculations using standard methodologies:
Orifice for gases (D<5 cm)
Orifice for liquids (D<5cm)
Orifice for liquids (D>5cm)
Nozzle for liquids
Venturi for liquids
Simpler orifice calculation (not as accurate but won't give "parameter out of
range" messages):
Bernoulli calculation
Unit Conversions
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