ГОСТ 8.586.2-2005 Государственная система обеспечения единства измерений (ГСИ). Измерение расхода и количества жидкостей и газов с помощью стандартных сужающих устройств. Часть 2. Диафрагмы. Технические требования (с Поправкой)

[1]

Международный стандарт ИСО 5167-1:2003

Измерение расхода среды с помощью устройств переменного перепада давления, помещенных в заполненные трубопроводы круглого сечения. Часть 1. Общие принципы и требования

(International Standard ISO 5167-1:2003)

(Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full - Part 1: General principles and requirements)

[2]

Международный стандарт ИСО 5167-2:2003

Измерение расхода среды с помощью устройств переменного перепада давления, помещенных в заполненные трубопроводы круглого сечения. Часть 2. Диафрагмы

(International Standard ISO 5167-2:2003)

(Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full - Part 2: Orifice plates)

[3]

Международный стандарт ИСО 5167-3:2003

Измерение расхода среды с помощью устройств переменного перепада давления, помещенных в заполненные трубопроводы круглого сечения. Часть 3. Сопла и сопла Вентури

(International Standard ISO 5167-3:2003)

(Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full - Part 3: Nozzles and Venturi nozzles)

[4]

Международный стандарт ИСО 5167-4:2003

Измерение расхода среды с помощью устройств переменного перепада давления, помещенных в заполненные трубопроводы круглого сечения. Часть 4. Трубы Вентури

(International Standard ISO 5167-4:2003)

(Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full - Part 4: Venturi tubes)

[5]

Отчет ИСО 9464:1998 (ISO/TR 9464:1998)

Руководство по применению ИСО 5167-1:1991 (Guidelines for the use of ISO 5167-1:1991)

[6]

Hobbs, J.M and Humphreys, J.S. The effect of orifice plate geometry upon discharge coefficient. Flow Measurement and Instrumentation, 1, April 1990, pp.133-140

[7]

Reader-Harris, M.J. and Sattary, J.A. The orifice plate discharge coefficient equation - the equation for ISO 5 167-1. In Proc. Of 14th North Sea Flow Measurement Workshop, Peebles, Scotland, East Kilbride, Glasgow, National Engineering Laboratory, October 1996, p.24

[8]

Reader-Harris, M.J. The equation for the expansibility factor for orifice plates. In Proc. Of FLOMEKO 98, Lund, Sweden, June 1998, pp.209-214

[9]

Reader-Harris, M.J. Pipe roughness and Reynolds number limits for the orifice plate discharge coefficient equation. In Proc. of 2nd Int. Symp. on Fluid Flow Measurement, Calgary, Canada, Arlington, Virginia: American Gas Association, June 1990, pp.29-43

[10]

Reader-Harris, M.J., Sattary, J.A. and Spearman, E.P. The orifice plate discharge coefficient equation. Progress Report No PR14: EUEC/17 (EEC005). East Kilbride, Glasgow: National Engineering Laboratory Executive Agency, May 1992

[11]

Morrow, T.B. and Morrison, G.L. Effect of meter tube roughness on orifice C. In Proc. of 4th Int. Symp. on Fluid Flow Measurement, Denver, Colorado, June 1999

[12]

Urner, G. Pressure loss of orifice plates according to ISO 5167. Flow Measurement and Instrumentation, 8, March 1997, pp.39-41

[13]

Studzinski, W., Karnik, U., Lanasa, P., Morrow, Т., Goodson, D., Husain, Z. and Gallagher, J. White paper on Orifice Meter Installation Configurations with and without Flow Conditiners, Washington D.C., American Petroleum Institute, 1997

[14]

Studzinski, W., Weiss, M., Attia, J. And Geerligs, J. Effects of reducers, expanders, a gate valve, and two elbows in perpendicular planes on orifice meter performance, In Proc. of Flow Measurement 2001 International Conference, Peebles, Scotland, May 2001, ppr 3.1, East Kilbride, Glasgow, National Engineering Laboratory

[15]

Weiss, M., Studzinski, W. and Attia, J. Performance evaluation of orifice meter standards for selected T-junction and elbow installations. In Proc. 5th Int. Symp. on Fluid Flow Measurement, Washington, D.C., April 2002

[16]

ГОСТ 8.563.1-97

Государственная система обеспечения единства измерений. Измерение расхода и количества жидкостей и газов методом переменного перепада давления. Диафрагмы, сопла ИСА 1932 и трубы Вентури, установленные в заполненных трубопроводах круглого сечения. Технические условия

[17]

Zanker, K.J. and Goodson, D. Qualification of a flow conditioning device according to the new API 14.3 procedure. Flow Measurement and Instrumentation, 11, June 2000, pp.79-87

[18]

Reader-Harris, M.J. and Brunton, W.C. The effect of diameter steps in upstream pipework on orifice plate discharge coefficients. In Proc. 5th Int. Symp. on Fluid Flow Measurement, Washington, D. C., April 2002

[19]

Morrow, T.B. Metering Research Facility Program Orifice Meter Installation Effects: Ten-inch sliding flow conditioner tests. Technical Memorandum GRI Report No. GRI-96/0391. San Antonio, Texas: Southwest Research Institute, November 1996

[20]

Karnik, U. A compact orifice meter/flow conditioner package. In Proc. of 3rd Int. Symp. on Fluid Flow Measurement, San Antonio, Texas, March 1995

[21]

Karnik, U., Studzinski, W., Geerligs, J and Kowch, R. Scale up tests on the NOVA Flow Conditioner for orifice meter applications. In Proc. of 4th Int. Symp. on Fluid Flow Measurement, Denver, Colorado, June 1999