
Good water management requires that flow rates be accurately measured. A simple but economical and accurate device for the measurement of flow rates from pipes discharging to the atmosphere is the orifice meter. The orifice meter is sometimes called a pipe orifice, an end-cap orifice, or more descriptively, a circular orifice weir.
Orifice meters are usually circular orifices placed at the end of a horizontal discharge pipe as illustrated in Figure 1 . Flow rates are calculated from the orifice characteristics and a measure of the pressure behind the orifice. The head (or pressure) on the orifice is measured with a water manometer to obtain a high degree of accuracy (Typically within 2% of true values).
Because of the simplicity of design and the few components of the orifice meter, it can readily be constructed by individuals with only average mechanical skills. An orifice meter can be constructed from a pipe end-cap which has been properly drilled, if the discharge pipe is threaded to allow the end cap to be added for flow measurements or removed after its use.
The cost of the orifice meter is minimal when self-constructed. The orifice meter is very accurate because of the sensitivity of the water manometer, and, because of the absence of moving parts or the need for calibration, it is often used as a means of calibrating other flow-measuring devices.
Details of construction are illustrated in Figure 2 . The orifice consists of a perfectly round hole in the center of a circular steel plate. The orifice must be cut with clean, square edges. The plate must be 1/16-inch thick around the circumference of the hole. The plate is fastened against the outer end of a level discharge pipe so that the orifice is centered on the pipe. The end of the pipe must be cut square so that the plate will be vertical. A properly machined pipe end-cap may be used as the orifice plate.
The bore of the pipe should be smooth and free of any obstruction that might cause excessive turbulence. This includes ensuring that there are no elbows, valves or other fittings closer than 6 feet upstream from the orifice. This approach must also be straight and level.
To measure pressure head on the orifice with sufficient accuracy, a glass tube manometer should be used. Exactly 24 inches from the orifice plate, the pipe wall is tapped mid-way between the top and bottom with a 1/8-1/4 inch diameter hole. Burrs inside the pipe caused by the drilling or tapping should be filed to ensure a smooth surface. The glass tube is connected with a short piece of flexible tubing to a pipe nipple threaded into the tapped hole. The glass tube is mounted vertically with a scale set to measure the height of water in the tube above the centertine of the pipe. When water is pumped through the orifice so that it is flowing full, the height of the water in the tube is the pressure head on the orifice.
For any given size of orifice discharge pipe, the rate of flow varies in a known manner with the pressure head as measured with the glass tube manometer. Standard tables, such as Table 1 , give the flow in gallons per minute (gpm) for various combinations of orifice diameter and pipe diameter
Discharge through the orifice is computed from equation 1 .
whereQ = orifice discharge (gpm),
C = coefficient which varies with the ratio of the orifice diameter to the pipe diameter, as well as with all of the other factors affecting flows in orifices of this construction (from Figure 3 ),
A = cross sectional area of the orifice (in 2 ), and
h = head on the orifice measured above its centerline (in).
The value of its coefficient, C, varies with the ratio of the orifice diameter to pipe diameter because of changes in streamlines is flow converges through orifices of various sizes. The value of C is also a function of friction losses through the orifice. Therefore, the values of C given in Figure 3 are only applicable when the orifice meter is constructed as previously described.
The use of Equation 1 is illustrated by an example. The following data apply:
Orifice constructed as previously described
Orifice diameter = 4 in
Discharge pipe inside diameter = 8 in
Pressure head, h = 30 in
Calculations are performed in 4 steps:
1.Ratio of orifice diameter to pipe diameter = 4 in / 8 in = 0.5
2.From Figure 3, C = 0. 587
3.Cross sectional area of orifice = pi d 2 /4 = (3.14)(4 in) 2 /4 = 12.56 in 2
4.Q = 8.02 CA h
Q = 8.02 (0.587) (12.56 in2) 30in
Q = 324 gpm
Comparing this result with that shown in Table 1 (325 gpm) shows the utility of Equation 1 . The discrepancies between values in Table 1 and those calculated result from inaccuracies in interpolating C values from Figure 3 .
The orifice meter provides the capability of measuring flow rates with accuracies within 2% of the actual rates if it is properly constructed and operated. Besides constructing the parts accurately and setting up the device correctly in the field, additional precautions must be taken to obtain accurate results. First, the diameter of the orifice should be less than 0.8 and greater than 0.4 of the inside diameter of the discharge pipe. The value of C changes rapidly as the ratio of diameters increases. Therefore, to ensure greatest accuracy, the ratio should be less than 0.7.
Second, the manometer tube must be completely free of obstruction and air bubbles when measurements of pressure head are made. Air bubbles can be eliminated by lowering the manometer tube to allow water to flow through it.
Finally, the orifice must flow completely full for Equation 1 or the data in Table 1 to apply. One method of ensuring this is to select an orifice diameter such that the manometer water level is above the top of the discharge pipe.
Orifice meters are easily constructed and economical flow-measuring devices for irrigation pump discharges. Accuracies within 2% of actual flow rates are obtainable if construction and operational practices outlined in this paper are followed. Because of the absence of moving parts or the need for calibration, the orifice meter is often used as a means of calibrating other flow measuring devices.
Briggs, G. F. and A. G. Fielder, eds. 1966. Ground Water and Wells. Johnson Division, Universal Oil Products. 440 pp.
Israelsen, 0. W. and V. E. Hansen. 1962. Irrigation Principles and Practices. John Wiley and Sons. 447 pp.
SCS National Engineering Staff. 1964. Measurement of Irrigation Water. Section 15, Chapter 9. SCS National Engineering Handbook. SCS. USDA. 72 pp.
| Table 1. Discharge from circular pipe orifices. | ||||||||||
| Head (inches) | 3-in. orifice | 4-in. orifice | 5-in. orifice | 6-in. orifice | 7-in. orifice | 8-in. orifice | ||||
| 4-in. Pipe | 6-in. Pipe | 6-in. Pipe | 8-in. Pipe | 6-in. Pipe | 8-in. Pipe | 8-in. Pipe | 10-in. Pipe | 10-in. Pipe | 10-in. Pipe | |
| G.p.m. | G.p.m. | G.p.m. | G.p.m. | G.p.m. | G.p.m. | G.p.m. | G.p.m. | G.p.m. | G.p.m. | |
| 6 | 108 | 82 | 160 | 150 | 305 | 240 | 408 | 345 | ||
| 8 | 122 | 94 | 185 | 170 | 350 | 280 | 458 | 395 | 600 | 935 |
| 10 | 133 | 104 | 205 | 190 | 393 | 316 | 508 | 445 | 666 | 1040 |
| 12 | 146 | 114 | 225 | 208 | 430 | 346 | 556 | 490 | 728 | 1120 |
| 14 | 157 | 123 | 243 | 224 | 465 | 376 | 599 | 530 | 785 | 1194 |
| 16 | 167 | 132 | 257 | 238 | 495 | 402 | 636 | 568 | 838 | 1266 |
| 18 | 178 | 140 | 271 | 252 | 524 | 426 | 672 | 604 | 887 | 1336 |
| 20 | 187 | 148 | 285 | 266 | 548 | 449 | 708 | 636 | 933 | 1404 |
| 22 | 197 | 156 | 299 | 279 | 572 | 470 | 744 | 664 | 979 | 1471 |
| 24 | 205 | 164 | 310 | 291 | 596 | 488 | 776 | 692 | 1022 | 1529 |
| 26 | 214 | 171 | 323 | 303 | 620 | 504 | 805 | 720 | 1064 | 1585 |
| 28 | 222 | 177 | 335 | 314 | 644 | 520 | 831 | 747 | 1104 | 1641 |
| 30 | 230 | 183 | 346 | 325 | 668 | 536 | 857 | 773 | 1143 | 1697 |
| 32 | 239 | 189 | 357 | 335 | 692 | 552 | 882 | 799 | 1181 | 1753 |
| 34 | 246 | 195 | 369 | 345 | 715 | 568 | 907 | 824 | 1218 | 1809 |
| 36 | 254 | 200 | 380 | 354 | 737 | 584 | 931 | 847 | 1251 | 1865 |
| 38 | 260 | 205 | 390 | 363 | 759 | 600 | 955 | 867 | 1281 | |
| 40 | 266 | 210 | 401 | 371 | 781 | 616 | 979 | 887 | 1311 | |
| 42 | 272 | 214 | 411 | 380 | 800 | 631 | 1001 | 906 | 1341 | |
| 44 | 278 | 219 | 420 | 388 | 820 | 645 | 1023 | 925 | 1371 | |
| 46 | 284 | 224 | 429 | 396 | 837 | 659 | 1045 | 944 | 1401 | |
| 48 | 290 | 229 | 440 | 405 | 855 | 672 | 1067 | 963 | 1431 | |
| 50 | 296 | 234 | 448 | 413 | 872 | 686 | 1089 | 982 | 1461 | |
| 52 | 302 | 238 | 457 | 421 | 888 | 700 | 1110 | 100 | 1491 | |
| 54 | 307 | 243 | 465 | 429 | 904 | 714 | 1130 | 1018 | 1520 | |
| 56 | 313 | 248 | 472 | 437 | 919 | 727 | 1150 | 1036 | 1548 | |
| 58 | 317 | 252 | 480 | 445 | 934 | 739 | 1170 | 1052 | 1574 | |
| 60 | 323 | 257 | 489 | 453 | 948 | 751 | 1190 | 1068 | 1598 | |
| 62 | 328 | 262 | 496 | 461 | 961 | 763 | 1209 | 1084 | ||
| 64 | 333 | 266 | 504 | 469 | 974 | 775 | 1227 | 1099 | ||
| 66 | 338 | 271 | 513 | 475 | 988 | 787 | 1245 | 1113 | ||
| 68 | 343 | 275 | 520 | 483 | 1002 | 799 | 1263 | 1127 | ||
| 70 | 349 | 280 | 525 | 491 | 1016 | 811 | 1280 | 1140 | ||
This document is AE22, one of a series of the Agricultural and Biological Engineering Department, Florida Cooperative Extension Service, Institute of Food and Agricultural Sciences, University of Florida. Original publication date July, 1987. Reviewed July, 2002. Visit the EDIS Web Site at http://edis.ifas.ufl.edu.
Allen G. Smajstrla, assistant professor; and Dalton S. Harrison, professor, Cooperative Extension Service, Institute of Food and Agricultural Sciences, University of Florida, Gainesville, 32611.
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