Engineering-Stream - Software for Engineering Applications
Home
Online Calculators
Downloads
Shop
About
Orifice Plate Sizing - Gas/Vapour
Pipe Nominal Size and Schedule
Selected Pipe Outside Diameter, Do
in
Selected Pipe Nominal Wall Thickness, Tn
in
Selected Pipe Inside Diameter, D
in
Pressure Upstream of Orifice, P1
psia
Pressure Downstream of Orifice, P2
psia
Temperature Upstream of Orifice, T1
deg.F
Molecular mass of Gas/Vapour, MW
lb/lbmol
Compressibility factor of Gas/Vapour U/S of Orifice, Z1
Density of Gas/Vapour U/S of Orifice, rho1
lbm/ft3
Viscosity of the fluid at inlet, mu1_cP
cP
Isentropic Coefficient, k
Mass flow rate through the orifice, qm
lbm/s
Type of Orifice Tap, OrificeTapType
Select orifice Tap Type
Corner Taps
D and D/2 Taps
Flange Taps
Relative Pressure Tap Spacing, L1, L2 (L = l/D)
Pipe Reynolds Number, RD
Expansibility Factor, Y
Calculated Orifice Plate Discharge Coefficient, C
Calculated Orifice Diameter, d
in
Beta Ratio, BR
Pressure Loss, h
lbf/in2
Design Verification1
Design Verification2
Design Verification3
Design Verification4
Design Verification5
Design Verification6
Submit
Help
General Notes:
Note: Refer to the "Terms and Conditions" in the 'About' section before using the software.
1) Orifice Plate Sizing is a software program that can be used to determine the bore (d in inches) of measurement orifice plates.
2) The available pipe sizes vary from 2 in to 36 in.
3) The procedure is based on ASME MFC-3M 2004 Ed / 2007 Addenda.
4) Equations used :-
qm = 0.09970190 * C * Y * d^2 * SQRT ((hw * rho1) / (1 - beta^4)).
C = 0.5961 + 0.0261 * BR^2 - 0.216 * BR^8 + 0.000521 * (10^6 * BR / RD) ^ 0.7 + (0.0188 + 0.0063*A) * BR^3.5
* (10^6/RD)^0.3 + (0.043 + 0.080 * e^(-10*L1) - 0.123*e^(-7*L1)) * (1- 0.11*A) * (BR^4/(1-BR^4)
- 0.031 * (M2' - 0.8 * M2'^1.1) * BR^1.3
When D < 71.12 mm (2.8 in), the following term shall be added to the above equation.
+ 0.011 * (0.75 - BR) * (2.8 - D) [ D - Pipe ID, D in inches, D/25.4 in place of D if D is in mm (SI units) ]
BR = d/D; RD - Pipe Reynolds Number; L1 = l1/D; L2' = l2'/D; M2' = (2 * L2')/(1-BR); A = (19000 * BR / RD)^0.8;
a) for Corner Taps: L1 = L2' = 0; b) for D and D21 taps: L1 = 1; L2' = 0.47; c) for Flange taps: L1 = L2' = 1/D; [D, in or D/25.4, mm]
Expansibility Factor, Y = 1 - (0.351 + 0.256*BR^4 + 0.93*BR^8) * [1 - (P2/P1)^(1/k)];
Pressure Loss, h = (NUM/DENOM) * (0.03606 * hw) ; hw - Differential pressure (in of H2O)
NUM = SQRT[ 1 - BR^4 * (1 - C^2)] - C * BR^2 ; DENOM = SQRT[ 1 - BR^4 * (1 - C^2)] + C * BR^2 ;
Limits of Use. Standard orifice plates shall only be used in accordance with the code clause under the following conditions:
(a) For orifice plates with corner or with D and D/2 pressure taps
(1) d >= 12.5 mm (0.5 in.)
(2) 50 mm (2 in.) <= D <= 1000 mm (40 in.)
(3) 0.10 <= BR <= 0.75;
(4) RD >= 5000 for 0.10 <= BR <= 0.56
(5) RD >= 16000 * BR^2 for BR > 0.56
(b) For orifice plates with flange taps
(1) d >= 12.5 mm (0.5 in.)
(2) 50 mm (2 in.) <= D <= 1000 mm (40 in.)
(3) 0.10 <= BR <= 0.75
(4) RD >= 5000 and RD >= 170 * BR^2 * D, (D, mm)
(5) RD >= 5000 and RD >= 4318 * BR^2 * D, (D, in.)
5) If you notice any error, please let us know, so that can be rectified.
6) Contact us with any comments / questions : engineeringstream11@gmail.com
7) Visit us for more software programs at https://engineering-stream.com