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1

Spencer, E. A. Study of edge sharpness effects measured during the EEC orifice plate cofficient programme. Commission of the European Communities, 1987.

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2

Martin, C. N. B. Effects of upstream bends and valves on orifice plate pressure distributions and discharge coefficients. National Engineering Laboratory, 1986.

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3

Reader-Harris, Michael. Orifice Plates and Venturi Tubes. Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-16880-7.

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4

Kinghorn, F. C. The expansibility correction for orifice plates: EEC data. Commission of the European Communities, 1986.

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5

A, Spencer E., ed. The analysis of coefficient data relating to the EEC 100mm orifice plates. Commission of theEuropean Communities, 1986.

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6

Smith, D. J. M. The effects of flow straighteners on orifice plates in good flow conditions. Commission of the European Communities, 1986.

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7

Fietz, T. R. An aid to the design of orifice plates according to ISO code 5167. University of New South Wales, Water Research Laboratory, 1988.

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8

B, Gloss Blair, and United States. National Aeronautics and Space Administration., eds. Orifice-induced pressure error studies in Langley 7- by 10-foot high-speed tunnel. National Aeronautics and Space Administration, Scientific and Technical Infomraton Branch, 1986.

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9

Plentovich, Elizabeth B. Orifice-induced pressure error studies in Langley 7- by 10-foot High-Speed Tunnel. NASA, 1986.

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10

B, Gloss Blair, and United States. National Aeronautics and Space Administration., eds. Orifice-induced pressure error studies in Langley 7- by 10-foot high-speed tunnel. National Aeronautics and Space Administration, Scientific and Technical Infomraton Branch, 1986.

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11

Clark, W. J. Flow Measurement: By Square-Edged Orifice Plate Using Corner Tappings. Elsevier Science & Technology Books, 2016.

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12

Escudier, Marcel. Engineering applications of Bernoulli’s equation. Oxford University Press, 2018. http://dx.doi.org/10.1093/oso/9780198719878.003.0008.

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In this chapter it is shown how Bernoulli’s equation can be applied to practical fluid-flow problems. In the case of internal flows, such as that through a Venturi tube, it is also necessary to use the continuity equation to relate changes in cross-sectional area to changes in flow velocity. For liquid flows it is shown that for sufficiently high flowspeeds the static pressure could fall below the saturated vapour pressure and lead to cavitation. The designs of various flow-measuring devices, including the orifice-plate flowmeter, the Venturi-tube flowmeter, and the Pitot tube, are based on Bernoulli’s equation. The changes in flow velocity occurring in flow through a wind-tunnel contraction are explained by Bernoulli’s equation.
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13

Reader-Harris, Michael. Orifice Plates and Venturi Tubes. Springer, 2016.

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14

Reader-Harris, Michael. Orifice Plates and Venturi Tubes. Springer, 2015.

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15

Reader-Harris, Michael. Orifice Plates and Venturi Tubes. Springer, 2015.

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16

Casado, Emilio. Design Guide for Restriction Orifice Plates with 1 Central Hole: Guide Nº 1. Independently Published, 2021.

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17

Martin, C. N. B. Effects of upstream bends and valves on oriface plate pressure distributions and discharge coefficients. National Engineering Laboratory, 1986.

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