Skip to main content

Introduction and History

  • Chapter
  • First Online:
Orifice Plates and Venturi Tubes

Part of the book series: Experimental Fluid Mechanics ((FLUID))

  • 4374 Accesses

Abstract

Differential-pressure flowmeters (called differential-pressure meters) remain the most common type of meter for large and medium flowrates: their demise has often been predicted, and yet large numbers of them are still both used and bought. The reasons for their continued popularity are considered: their advantages and disadvantages are listed. The theory (Bernoulli’s Theorem) for incompressible and compressible flow is considered, and both the basic equation for flow through differential-pressure meters and the expansibility-factor equation for Venturi tubes are derived. An introduction to Reynolds number and velocity profile, pipe roughness and pressure loss is provided. The essential requirements for differential-pressure flow measurement are described and discussed, and the location of material in other chapters required to meet these requirements is given. The history of flow measurement by Venturi tubes and orifice plates is described, with particular reference to Clemens Herschel in the main text and an Appendix on Sextus Julius Frontinus.

This is a preview of subscription content, log in via an institution to check access.

Access this chapter

Chapter
USD 29.95
Price excludes VAT (USA)
  • Available as PDF
  • Read on any device
  • Instant download
  • Own it forever
eBook
USD 99.00
Price excludes VAT (USA)
  • Available as EPUB and PDF
  • Read on any device
  • Instant download
  • Own it forever
Hardcover Book
USD 199.99
Price excludes VAT (USA)
  • Durable hardcover edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info

Tax calculation will be finalised at checkout

Purchases are for personal use only

Institutional subscriptions

Notes

  1. 1.

    In summa moduli sunt XX quinque. Omnes consentiunt et rationi et commentariis, exceptis his quattuor, quos aquarii novaverunt. Omnia autem quae mensura continentur, certa et immobilia congruere sibi debent; ita enim universitati ratio constabit. Et quemadmodum verbi gratia sextarii ratio ad cyathos, modii vero et ad sextarios et ad cyathos respondet; ita et quinariarum multiplicatio in amplioribus modulis servare consequentiae suae regulam debet. Alioqui cum in erogatorio modulo minus invenitur, in acceptorio plus, apparet non errorem esse sed fraudem (34).

  2. 2.

    An offtake (or intake) tube, here effectively a water meter.

  3. 3.

    ‘consistent’ might be better.

  4. 4.

    The Roman pint (about 0.55 l), close to an imperial pint.

  5. 5.

    1/12th of a sextarius (about 45 ml), about 1.6 fl oz.

  6. 6.

    The Roman peck: 16 sextarii (about 8.8 l), close to an imperial peck.

  7. 7.

    Sed et calicis positio habet momentum. In rectum et ad libram conlocatus modum servat, ad cursum aquae oppositus et devexus amplius rapit, ad latus praetereuntis aquae conversus et supinus, id est ad haustum pronior, segniter et exiguum sumit. Est autem calix modulus aeneus, qui rivo vel castello induitur; huic fistulae applicantur. Longitudo eius habere debet digitos non minus duodecim, lumen capacitatem quanta imperata fuerit (36).

  8. 8.

    This translation makes good sense but is not an obvious rendering of the Latin.

  9. 9.

    The translation may be assuming that ‘induitur’ should be ‘inditur’.

  10. 10.

    Interior area.

  11. 11.

    Circa conlocandos quoque calices observari oportet ut ad lineam ordinentur nec alterius inferior calix, alterius superior ponatur. Inferior plus trahit; superior, quia cursus aquae ab inferiore rapitur, minus ducit (113).

  12. 12.

    here calices.

  13. 13.

    In quibusdam, cum calices legitimae mensurae signati essent, statim amplioris moduli fistulae subiectae fuerunt, unde acciderat ut aqua non per legitimum spatium coercita, sed per brevis angustias expressa facile laxiorem in proximo fistulam inpleret. Ideoque illud adhuc, quotiens signatur calix, diligentiae adiciendum est, ut fistulae quoque proximae per spatium, quod S. C. comprehensum diximus, signentur (112).

  14. 14.

    here calices.

  15. 15.

    i.e. 50 feet: see below.

  16. 16.

    here calix.

  17. 17.

    Procurator calicem eius moduli, qui fuerit impetratus, adhibitis libratoribus signari cogitet, diligenter intendat mensurarum quas supra diximus modum et positionis notitiam habeat, ne sit in arbitrio libratorum, interdum maioris luminis, interdum minoris pro gratia personarum calicem probare. Sed nec statim ab hoc liberum subiciendi qualemcumque plumbeam fistulam permittatur arbitrium, verum eiusdem luminis quo calix signatus est per pedes quinquaginta, sicut senatus consulto quod subiectum est cavetur (105).

  18. 18.

    surveyors.

  19. 19.

    diligently.

  20. 20.

    here measures (i.e. meters).

  21. 21.

    a pronoun that refers to the calix.

  22. 22.

    here calix.

  23. 23.

    Ita demum enim vilicus cum scierit non aliter quam signatas conlocari debere, omni carebit excusatione (112—immediately following previous extract from 112).

  24. 24.

    Tot aquarum tam multis necessariis molibus pyramidas videlicet otiosas compares aut cetera inertia sed fama celebrata opera Graecorum (16).

References

  • AGA (1951) Investigation of orifice meter installation requirements. American Gas Association, Washington

    Google Scholar 

  • AGA (1954a) Investigation of orifice meter installation requirements. American Gas Association, Washington

    Google Scholar 

  • AGA (1954b) Large diameter orifice meter tube tests. Final report of supervising committee. Research project NX-4. American Gas Association, Washington

    Google Scholar 

  • AGA-ASME (1935) History of orifice meters and the calibration, construction and operation of orifices for metering. Report of the joint AGA—ASME committee on orifice coefficients

    Google Scholar 

  • Agarwal NK (1994) Mean separation and reattachment in turbulent pipe flow due to an orifice plate. J Fluids Eng 115:373–376

    Google Scholar 

  • API (1985) Manual of petroleum measurement standards, chapter 14—natural gas fluids measurement, section 3—orifice metering of natural gas and other related hydrocarbon fluids, 2nd edn. ANSI/API 2530

    Google Scholar 

  • API (1990) Manual of petroleum measurement standards, chapter 14—natural gas fluids measurement, section 3—concentric, square-edged orifice meters, part 1—general equations and uncertainty guidelines. MPMS chapter 14, section 3, part 1, 3rd edn. American Petroleum Institute, Washington DC

    Google Scholar 

  • Batchelor GK (1967) An introduction to fluid dynamics. Cambridge University Press, Cambridge

    Google Scholar 

  • Bates CJ (1981) Laser Doppler anemometry measurements of the flow through an orifice plate. Flow 81 its measurement and control in science and industry 2. Instrument Society of America, Pittsburgh, pp 59–68

    Google Scholar 

  • Bean HS, Benesh ME, Buckingham E (1931) Experiments on the metering of large volumes of air. Bur Stand J Res 7:93–145 (Research paper no 335)

    Article  Google Scholar 

  • Bean HS, Buckingham E, Murphy PS (1929) Discharge coefficients of square-edged orifices for measuring the flow of air. Bur Stand J Res 2:561–658 (Research paper no 49)

    Article  Google Scholar 

  • Beitler SR (1935) The flow of water through orifices. A study in 1-in., 1½-in., 2-in., 3-in., 6-in., 10-in, and 14-in. lines. Engineering experiment station bulletin no 89. Ohio State University

    Google Scholar 

  • Bernoulli D (1738) Hydrodynamica, sive de viribus et motibus fluidorum commentarii. Strasbourg

    Google Scholar 

  • Bernoulli J (1743) Hydraulica nunc primum detecta ac demonstrata directe ex fundamentis pure mechanicis, Anno 1732. Opera Omnia, vol 4, Lausanne and Geneva

    Google Scholar 

  • Buckingham E (1932) Notes on the orifice meter: the expansion factor for gases. Bur Stand J Res 9 (Research paper no 459)

    Google Scholar 

  • Chisholm D (1967) Flow of incompressible two-phase mixtures through sharp-edged orifices. J Mech Eng Sci 9(1):72–78

    Google Scholar 

  • Chisholm D (1977) Research note: two-phase flow through sharp-edged orifices. J Mech Eng Sci 19(3):128–130

    Google Scholar 

  • Cousins T (1975) An experimental investigation into the design parameters of the Dall tube. Fluid flow measurement in the mid-1970s, 2: paper J-2, National Engineering Laboratory

    Google Scholar 

  • Curle N, Davies HJ (1968) Modern fluid dynamics. Incompressible flow, vol 1. van Nostrand Reinhold, London

    Google Scholar 

  • de Leeuw H (1994) Wet-gas flow measurement by means of a Venturi meter and a tracer technique. In: Proceedings of the 12th North Sea Flow Meas Workshop, Peebles. National Engineering Laboratory Executive Agency, East Kilbride, Glasgow

    Google Scholar 

  • de Leeuw H (1997) Liquid correction of Venturi meter readings in wet-gas flow. In: Proceedings of the 15th North Sea Flow Meas Workshop, paper 21, Norway

    Google Scholar 

  • DeOtte RE, Morrison GL, Panak DL, Nail GH (1991) 3-D laser Doppler anemometry measurements of the axisymmetric flow field near an orifice plate. Flow Meas Instrum 2(2):115–123

    Article  Google Scholar 

  • Eujen E (1969) Die Durchfluβmessung mit Drosselgeräten bei laminarer Rohrströmung. Brennst-Wärme-Kraft 21(12):628–630

    Google Scholar 

  • Frontinus SJ (c. 97–98) De aquis urbis Romae

    Google Scholar 

  • Hall GW (1959) Application of boundary layer theory to explain some nozzle and Venturi flow peculiarities. Proc Inst Mech Eng 173(36):837–870

    Article  Google Scholar 

  • Halmi D (1973a) Metering performance investigation and substantiation of the “Universal Venturi Tube” (U.V.T.). Part 1—hydraulic shape and discharge coefficient. ASME paper 73-WA/FM-3

    Google Scholar 

  • Halmi D (1973b) Metering performance investigation and substantiation of the “Universal Venturi Tube” (U.V.T.). Part 2—installation effect, compressible flow and head loss. ASME paper 73-WA/FM-4

    Google Scholar 

  • Halmi D (1973c) Practical guide to the evaluation of the metering performance of differential producers. J Fluids Eng:127–141 (March 1973)

    Google Scholar 

  • Herschel C (1887) The Venturi water meter: an instrument making use of a new method of gauging water; applicable to the cases of very large tubes, and of a small value only, of the liquid to be gauged. Trans Am Soc Civ Eng 17:228–258

    Google Scholar 

  • Herschel C (1895) The Venturi meter patented by Clemens Herschel hydraulic engineer and by Builders Iron Foundry, made by Builders Iron Foundry, founders and machinists. Livermore and Knight Co., Providence

    Google Scholar 

  • Hickstein EO (1915) The flow of air through thin-plate orifices. Trans ASME 37:765–793

    Google Scholar 

  • Ho YS, Leung TP (1985) Performance of conical entrance orifice plates at low Reynolds numbers. Int J Heat Fluid Flow 6(2):122–125

    Article  Google Scholar 

  • Hodgson JL (1917) The commercial metering of air, gas and steam. Minutes Proc Inst Civ Eng CCIV 108–193

    Google Scholar 

  • ISO (1967) Measurement of fluid flow by means of orifice plates and nozzles. International Organization for Standardization, Geneva. ISO/R 541:1967

    Google Scholar 

  • ISO (1980) Measurement of fluid flow by means of orifice plates, nozzles and Venturi tubes inserted in circular cross-section conduits running full. International Organization for Standardization, Geneva. ISO 5167:1980

    Google Scholar 

  • ISO (1991) Measurement of fluid flow by means of pressure differential devices—part 1: orifice plates, nozzles and Venturi tubes inserted in circular cross-section conduits running full. International Organization for Standardization, Geneva. ISO 5167-1:1991

    Google Scholar 

  • ISO (1998) Measurement of fluid flow in closed conduits—guidelines on the effects of flow pulsations on flow measurement instruments. International Organization for Standardization, Geneva. ISO/TR 3313:1998

    Google Scholar 

  • ISO (2003a) Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full—part 1: general principles and requirements. International Organization for Standardization, Geneva. ISO 5167-1:2003

    Google Scholar 

  • ISO (2003b) Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full—part 2: orifice plates. International Organization for Standardization, Geneva. ISO 5167-2:2003

    Google Scholar 

  • ISO (2003c) Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full—part 3: nozzles and Venturi nozzles. International Organization for Standardization, Geneva. ISO 5167-3:2003

    Google Scholar 

  • ISO (2003d) Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full—part 4: Venturi tubes. International Organization for Standardization, Geneva. ISO 5167-4:2003

    Google Scholar 

  • ISO (2007a) Measurement of fluid flow by means of pressure differential devices—guidelines for the specification of orifice plates, nozzles and Venturi tubes beyond the scope of ISO 5167. International Organization for Standardization, Geneva. ISO/TR 15377:2007

    Google Scholar 

  • ISO (2007b) Measurement of fluid flow by means of pressure differential devices—guidelines on the effect of departure from the specifications and operating conditions given in ISO 5167. International Organization for Standardization, Geneva. ISO/TR 12767:2007

    Google Scholar 

  • ISO (2008) Guidelines for the use of ISO 5167:2003. International Organization for Standardization, Geneva. ISO/TR 9464:2008

    Google Scholar 

  • Ito H, Watanabe Y, Shoji Y (1985) A long-radius inlet nozzle for flow measurement. J Phys E Sci Instrum 18:88–91

    Article  Google Scholar 

  • Jaumotte AL, Onockx L (1985) Sur les valeurs du coefficient d’épaisseur d’un ajustage de Borda. Bulletin de la Classe des Sciences, 5e série, tome 71:138–146. Académie royale des Sciences, des Lettres et des Beaux-Arts, Bruxelles

    Google Scholar 

  • Kastner LJ, McVeigh JC (1965–1966) A reassessment of metering orifices for low Reynolds numbers. Proc I Mech E 180(1): 331–345

    Google Scholar 

  • Kent WG (1912) An appreciation of two great workers in hydraulics; Giovanni Battista Venturi…Clemens Herschel. Privately printed, London

    Google Scholar 

  • Kinghorn FC, McHugh A (1978) The performance characteristics of Borda inlet air flowmeters. J Phys E: Sci Instrum 11:87–93

    Article  Google Scholar 

  • Kinghorn FC, McHugh A, Crawford DA (1975) Effect of cross-wind on three types of differential pressure inlet flowmeter. NEL report no 605. National Engineering Laboratory, East Kilbride

    Google Scholar 

  • Lake WT (1999) Guidelines for choosing, installing, maintaining offshore metering: dealing with the “construction gorillas”. Offshore 152, 153, 198. September 1999

    Google Scholar 

  • Lindley D (1966) Venturimeters and boundary layer effects. Ph.D. thesis, Dept. of Mech. Eng, Univ. Coll. of South Wales and Monmouthshire, Cardiff

    Google Scholar 

  • Martin CNB (1986) Effects of upstream bends and valves on orifice plate pressure distributions and discharge coefficients. NEL report no 702. National Engineering Laboratory, East Kilbride

    Google Scholar 

  • Mattingly GE, Davis RW (1977) Numerical solutions for laminar orifice flow. ASME paper 77-WA/FE-13, American Society of Mechanical Engineers, New York

    Google Scholar 

  • McKeon BJ, Li J, Jiang W, Morrison JF, Smits AJ (2004) Further observations on the mean velocity distribution in fully developed pipe flow. J Fluid Mech 501:135–147

    Article  MATH  Google Scholar 

  • McVeigh JC (1974) The effect of installation conditions on the discharge coefficient of the conical entrance orifice plate at low Reynolds numbers. In: Dowdell R (ed) Flow its measurement and control in science and industry, vol 1, no 2. Instrument Society of America, Pittsburgh, pp 533–537 (conference was in May 1971)

    Google Scholar 

  • Mills RD (1968) Numerical solutions of viscous flow through a pipe orifice at low Reynolds numbers. J Mech Eng Sci 10(2):133–140

    Article  Google Scholar 

  • Morrison GL (1990) 3-D laser anemometer study of compressible flow through orifice plates. Part 1. GRI report no GRI-90/0036. Gas Research Institute, Chicago

    Google Scholar 

  • Morrison GL (1993) 3-D laser anemometer study of compressible fluid flow through orifice plates. Final report to Gas Research Institute (September 1986–December 1992). GRI report no GRI-93/0314. Gas Research Institute, Chicago

    Google Scholar 

  • Morrison GL, DeOtte RE, Beam EJ (1992a) Installation effects upon orifice flow meters. 71st Annual Gas Processors Association convention, Anaheim, California

    Google Scholar 

  • Morrison GL, DeOtte RE, Nail GH, Panak DL (1992b) Mean velocity and turbulence fields inside a β = 0.50 orifice flow meter. AIChE 1992 spring national meeting, New Orleans, paper no 100G

    Google Scholar 

  • Morrison GL, Hall KR, Holste JC, Macek M L, Ihfe LM, DeOtte RE, Terracina DP (1993) Slotted orifice flow meter/conditioner. Flow measurement for the utilities, Amsterdam, the Netherlands

    Google Scholar 

  • Morrison GL, Hall KR, Holste JC, Macek ML, Ihfe LM, DeOtte RE, Terracina DP (1994) Comparison of orifice and slotted plate flowmeters. Flow Meas Instrum 5(2):71–77

    Article  Google Scholar 

  • Morrow TB (2005) Metering research facility program: additional studies of orifice meter installation effects and expansion factor. GRI report GRI-04/0246 on SwRI project no 18.10315. Gas Research Institute, Chicago

    Google Scholar 

  • Murdock JW, Foltz CJ (1953) Experimental evaluation of expansion factors for steam. Trans ASME 75(5): 953–959

    Google Scholar 

  • Panak DL, Morrison GL, DeOtte RE, Nail, GH (1992) Triple velocity correlations and other turbulence quantities from 3-D LDV measurements of the flow in an orifice meter. In: 6th International Symposium Application Laser Techniques to Fluid Mechanics. Lisbon, Portugal

    Google Scholar 

  • Pearsall IS (1962) Calibration of three conical inlet nozzles. NEL report no 39. National Engineering Laboratory, East Kilbride

    Google Scholar 

  • Ramamurthi K, Nandakumar K (1999) Characteristics of flow through small sharp-edged cylindrical orifices. Flow Meas Instrum 10(3):133–143

    Article  Google Scholar 

  • Reader-Harris MJ (2007) ISO flow measurement standards—report on the ISO/TC 30 meeting in November 2006. Flow Meas Instrum 18(3–4):114–120

    Article  Google Scholar 

  • Sattary JA (1991) EEC orifice plate programme—installation effects. Flow Meas Instrum 2(1): 21–33

    Google Scholar 

  • Sattary JA, Reader-Harris MJ (1997) Computation of flow through Venturi meters. In: Proceedings of the 15th North Sea Flow Meas Workshop, Norway

    Google Scholar 

  • Schlichting H (1960) Boundary layer theory. McGraw-Hill, New York

    MATH  Google Scholar 

  • Spearman EP, Sattary JA, Reader-Harris MJ (1996) Comparison of velocity and turbulence profiles downstream of perforated plate flow conditioners. Flow Meas Instrum 7 (3/4): 181–199

    Google Scholar 

  • Spearman EP, Sattary JA, Reader-Harris MJ, Rhodes FS (1995) The effect of upstream installations on orifice meter discharge coefficients. Flow measurement memo FL/445. National Engineering Laboratory Executive Agency, East Kilbride

    Google Scholar 

  • Stoll HW, Zientara D (1974) The conical entrance orifice plate, an investigation of its performance characteristics. In: Dowdell R (ed) Flow its measurement and control in science and industry, vol 1, no 2. Instrument Society of America, Pittsburgh, pp 517–522 (conference was in May 1971)

    Google Scholar 

  • Stolz J (1978) A universal equation for the calculation of discharge coefficients of orifice plates. In: Dijstelbergen HH, Spencer EA (eds) Flow measurement of fluids. North Holland Publishing Company, Netherlands, pp 519–534

    Google Scholar 

  • Studzinski W, Karnik U, LaNasa P, Morrow T, Goodson D, Husain Z, Gallagher J (2001) White paper on orifice meter installation configurations with and without flow conditioners. White paper prepared for API 14.3 Part 2. GRI report GRI 99/0262, Gas Research Institute, Chicago

    Google Scholar 

  • Studzinski W, Weiss M, Attia J (2000) Effect of reducers, expanders and a gate valve on orifice meter performance. NRTC report # 01426, Nova Research and Technology Corporation, Calgary

    Google Scholar 

  • Turton RK (1975) A note on flow through conical entrance orifice plates. In National Engineering Laboratory: Fluid Flow Measurement in the mid-1970s 1: paper A-3

    Google Scholar 

  • Vasy GS, Kastner LJ, McVeigh JC (1968–1969) Profiles for low Reynolds number flows. Proc I Mech E 183(1):591–602

    Google Scholar 

  • Venturi GB (1797) Recherches expérimentales sur le principe de la communication latérale du mouvement dans les fluides, appliqué à l’explication de différents phénomènes hydrauliques, Paris

    Google Scholar 

  • Wilson MP, Teyssandier RG (1975) The paradox of the vena contracta. Trans ASME J Fluids Eng 97(3):366–371

    Google Scholar 

  • Witte R (1931) Die Strömung durch Düsen und Blenden. Forschung auf dem Gebiet des Ingenieurwesens 2: 245 and 291 (two issues)

    Google Scholar 

  • Witte R (1951) Neue Arbeiten zur Durchfluβmessung. Brennst-Wärme-Kraft 3(11):378–380

    Google Scholar 

  • Zagarola MV, Smits AJ (1998) Mean flow scaling in turbulent pipe flow. J Fluid Mech 373:33–79

    Article  MATH  Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Michael Reader-Harris .

Appendix 1.A: Sextus Julius Frontinus

Appendix 1.A: Sextus Julius Frontinus

Probably the first person to describe flow measurement in closed pipes using a method whose descendant is that codified in modern differential-pressure standards was Sextus Julius Frontinus. He was born about 35 AD and was Provincial Governor of Britain about 76 AD, where he subdued the Silures (a tribe in Wales) and constructed the Via Julia. After his return to Rome he wrote Strategemata (his work on the art of war) about 90 AD. He then became Water Commissioner in Rome: he might have regarded this as a sinecure, but instead he was an outstanding public servant and wrote a treatise De Aquis (Frontinus c 97–98) around 97–98 AD on the Aqueducts of Rome (quotations below from De Aquis are from the Loeb edition with a translation by Charles E Bennett, a revision of that by Clemens Herschel). He describes how the aqueduct system of ancient Rome (depicted in Figs. 1.A.1 and 1.A.2) operated, and places particular emphasis on the flow measurement aspects. His book is a remarkable achievement for one who came to flow measurement so late in life.

Fig. 1.A.1
figure 12

Aqua Claudia in the Parco degli Acquedotti: August 2008 taken by Agricmarketing (talk) Wikipedia under Parco degli Acquedotti

Fig. 1.A.2
figure 13

Porta Maggiore, Rome, formed by a supporting arch of the Aqua Claudia and Rome’s highest elevated aqueduct Aqua Anio Novus, integrated into Aurelian Wall as a gate 271 AD. From Wikipedia under Roman aqueduct: it was taken by Diana

Standardized pipes

The system contained standardized pipes for offtakes and intakes from and to the main aqueducts. Frontinus described the permissible pipe sizes showing how they were constructed: the basic unit was the quinaria (or 5-pipe), a pipe with a diameter of 5 quarters of a digit, where a digit is 1/16 Roman foot (the Roman foot was equal to 0.967 imperial foot; the Roman foot could alternatively be divided into 12 inches). The senaria (or 6-pipe) had a diameter of 6 quarters of a digit and so up to the vicenaria (or 20-pipe) with a diameter of 20 quarters of a digit (i.e. 5 digits). Above that size the system was different and based on area not diameter: the vicenum quinum (or 25-pipe) had an area of 25 square digits, the tricenaria (30-pipe) of 30 square digits and so up to the centenum vicenum (120-pipe). If the second definition based on area had been used for the vicenaria (or 20-pipe) then the difference from the definition based on diameter would have been very small (less than 2 per cent on area). So there was little problem at the changeover between systems.

Frontinus discovered that in four pipe sizes (duodenaria (12-pipe), vicenaria (20-pipe), centenaria (100-pipe) and centenum vicenum (120-pipe)) the common usage was different from the systematic method described above. Although for the first of these the error was small, for the second, which was commonly used for delivery, the common usage was 20 % smaller than it should have been, the third and fourth were 13 and 68 % larger, respectively, than they should have been. He sums this up as follows:

In all there are 25 ajutages.Footnote 1 , Footnote 2 They all conform to their computed and recorded capacities, barring these four which the water-men have altered. But everything embraced under the head of mensuration ought to be fixed, unchanged, and constant.Footnote 3 For only so will any special computation accord with general principles. Just as a sextarius,Footnote 4 for example, has a regular ratio to a cyathus,Footnote 5 and similarly a modius Footnote 6 to both a cyathus and sextarius, so also the multiplication of the quinariae in case of the larger ajutages must follow a regular progression. However, when less is found in the delivery ajutages and more in the receiving ajutages, it is obvious that there is not error, but fraud.

Frontinus was a faithful public servant, honest and conscientious, basing his conclusions on personal examination. For clarity he listed in detail the permissible 25 pipe sizes (those not actually in use are here in italics): 5, 6, 7, 8, 10, 12, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100 and 120. The problem with his system was that he assumed the flowrate would be proportional to the area alone. He made no direct allowance for velocity.

Meter installation

Frontinus knew that meter installation (in terms of the angle of the meter to the main flow) does make a difference:

Footnote 7But the position of the calix is also a factor. Placed at right angles and level, it maintains the normal quantity. Set against the current of the water, and sloping downward, it will take in more. If it slopes to one side, so that the water flows by, and if it is inclined with the current, that is, is less favourably placed for taking in water,Footnote 8 it will receive the water slowly and in scant quantity. The calix, now, is a bronze ajutage, insertedFootnote 9 into a conduit or reservoir, and to it the service pipes are attached. Its length ought not to be less than 12 digits, while its orificeFootnote 10 ought to have such capacity as is specified.

Calix is defined in the Oxford Latin Dictionary as ‘a short length of brass pipe of a specified diameter installed between a water main or reservoir and a private supply pipe to regulate the amount of water drawn off by the latter’.

Frontinus knew a little about the effect of pressure, but not enough to quantify the effect:

In setting ajutagesFootnote 11 , Footnote 12 also, care must be taken to set them on the level, and not place the one higher and the other lower down. The lower one will take in more; the higher one will suck in less, because the current of water is drawn in by the lower one.

Frontinus knew about the effect of unmatched upstream pipework:

In some of the reservoirs, though their ajutagesFootnote 13 , Footnote 14 were stamped in conformity with their lawful measurements, pipes of a greater diameter [than the ajutages] were at once attached to them. As a consequence, the water not being held together for the lawful distance,Footnote 15 and being on the contrary forced through the short restricted distance, easily filled the adjoining larger pipes. Care should therefore be taken, as often as an ajutageFootnote 16 is stamped, to stamp also the adjoining pipe over the length which we stated was prescribed by the resolution of the Senate.

Accreditation

Frontinus not only put forward a standard, but also an accreditation system based on standards and diligence:

The deputy must call in the levellersFootnote 17 , Footnote 18 and provide that the calix is stamped as conforming to the deeded quantity, and must studyFootnote 19 the size of the ajutagesFootnote 20 we have enumerated above, as well as have knowledge of their location, lest it rest with the caprice of the levellers to approve a calix of sometimes greater, or sometimes smaller, interior area, according as they interest themselves in the parties. Neither must the deputy permit the free option of connecting directly to the ajutagesFootnote 21 any sort of lead pipe, but there must rather be attached for a length of fifty feet one of the same interior area as that which the ajutageFootnote 22 has been certified to have, as has been ordained by a vote of the Senate which follows.

For then and then only can the overseer be held to his full responsibility, when he understands that none but stamped pipes must be set in place.Footnote 23

Frontinus’s Legacy

So Frontinus produced a standard for flow measurement, took account of installation effects, and aimed for consistency and fairness. He even achieved pleasure in such worthwhile engineering as the aqueducts:

With such an array of indispensable structures carrying so many waters,Footnote 24 compare, if you will, the idle Pyramids or the useless, though famous, works of the Greeks!

As is stated in the Loeb edition of Frontinus’s works ‘it is the personality of the writer that one loves to contemplate, his sturdy honesty, his conscientious devotion to the duties of his office, his patient attention to details, his loyal attachment to the sovereign whom he delighted to serve, his willing labours in behalf of the people whose convenience, comfort and safety he aimed to promote’.

Rights and permissions

Reprints and permissions

Copyright information

© 2015 Springer International Publishing Switzerland

About this chapter

Cite this chapter

Reader-Harris, M. (2015). Introduction and History. In: Orifice Plates and Venturi Tubes. Experimental Fluid Mechanics. Springer, Cham. https://doi.org/10.1007/978-3-319-16880-7_1

Download citation

  • DOI: https://doi.org/10.1007/978-3-319-16880-7_1

  • Published:

  • Publisher Name: Springer, Cham

  • Print ISBN: 978-3-319-16879-1

  • Online ISBN: 978-3-319-16880-7

  • eBook Packages: EngineeringEngineering (R0)

Publish with us

Policies and ethics