CN2699248Y - Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter - Google Patents

Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter Download PDF

Info

Publication number
CN2699248Y
CN2699248Y CN 200420022873 CN200420022873U CN2699248Y CN 2699248 Y CN2699248 Y CN 2699248Y CN 200420022873 CN200420022873 CN 200420022873 CN 200420022873 U CN200420022873 U CN 200420022873U CN 2699248 Y CN2699248 Y CN 2699248Y
Authority
CN
China
Prior art keywords
flow meter
oil
phase
venturi tube
flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 200420022873
Other languages
Chinese (zh)
Inventor
黄志尧
王微微
王保良
冀海峰
李海青
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang University ZJU
Original Assignee
Zhejiang University ZJU
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhejiang University ZJU filed Critical Zhejiang University ZJU
Priority to CN 200420022873 priority Critical patent/CN2699248Y/en
Application granted granted Critical
Publication of CN2699248Y publication Critical patent/CN2699248Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Measuring Volume Flow (AREA)

Abstract

The utility model relates to an oil-water double phase flow measuring apparatus based on a standard venturi pipe and a turbine flow meter, comprising a metering pipeline, a flow mixer which is arranged at the front end of the metering pipeline, a turbine flow meter with high viscosity and a temperature sensor which are arranged at the rear end of the metering pipeline, a standard venturi pipe which is arranged at the middle portion of the metering pipeline, a differential pressure transducer which is connected with the venturi pipe, an A/D transition card and a computer. Each sensor is connected with the computer by the A/D transition card in a clamping way. The utility model has the advantages of small size, simple structure, convenient installation, low pressing loss, wide scope of application, a plurality of metering parameters which can be obtained, high flow capacity checking precision, etc., and is suitable for metering oil-liquid two-phase flow of chemical industry solvent extraction, etc.

Description

Oil-water two-phase flow measurement mechanism based on standard Venturi tube and turbo flow meter
Technical field
The utility model relates to a kind of oil-water two-phase flow measurement mechanism based on standard Venturi tube and turbo flow meter.
Background technology
Oil-water two-phase flow is prevalent in the petroleum industry.The complicacy of oil-water two-phase flow system brings a lot of difficulties for the measurement of flow and density.Current measuring methods mainly is to carry out profit two earlier to be separated, and measures single-phase flow then respectively.But because oil-water separation is subjected to influence of various factors easily, profit two-phase separating difficulty is bigger, and separating effect is bad, thereby causes measuring accuracy not high; And because profit two is separated and needs the regular hour, when flow was very big, two are separated need be chronic, makes that the metering time of profit two-phase is elongated, is unfavorable for that the real-time of measurement parameter detects.
Another kind of metering method commonly used is oil-water two-phase flow to be mixed become homogeneous flow, utilizes single-phase flowmeter such as restriction flowmeter, volumeter to wait and obtains flow.But the flow that obtains is a profit two-phase total volumetric flow rate, can't obtain each minute phase content and separate phase flow rate data.Though densitometer can solve the individual phase measurement problem in conjunction with single-phase flowmeter, measuring accuracy is not ideal enough during still actual the use, and cost is also very high.Vibrating tube densimeter commonly used is very responsive to field conditions such as the temperature of medium, pressure.And there is safety problem in gamma ray density meter, operating conditions is required high.Also can still there be shortcomings such as cost height, service condition harshness, installation and maintenance inconvenience in the coriolis mass flowmeters of Chu Xianing with solving profit individual phase measurement problem in recent years.
Summary of the invention
The purpose of this utility model provides a kind of profit two-phase measurement mechanism based on standard Venturi tube and turbo flow meter.
It has the metering pipeline, on the metering pipeline, be provided with mixed flow device, standard Venturi tube, wide viscosity type turbo flow meter, temperature sensor successively, the supporting differential pressure pick-up that is equipped with of standard Venturi tube, wide viscosity type turbo flow meter, differential pressure pick-up, temperature sensor link to each other with the A/D transition card, and the A/D transition card links to each other with computing machine.
Advantage of the present utility model is as follows:
1) do not carrying out under the situation that profit two is separated, utilizing Venturi tube and turbo flow meter the branch phase content and the flow of test fluid density and profit two-phase simultaneously, improving precision and real-time that the oil-water two-phase flow amount detects.
2) selected turbine flow is counted wide viscosity type turbo flow meter, it is the measuring accuracy height not only, easy for installation, be difficult for stopping up, be suitable for high-tension measurement, can be used for various bores, especially small-bore, and compare with the flowmeter that positive displacement etc. can be used for the profit two-phase flow measurement, it is little that turbo flow meter has a volume, easy for installation, advantage such as flow range is bigger.In addition, wide viscosity type turbo flow meter is owing to the viscosity compensation is arranged, so be particularly suitable for the measurement of high viscosity fluid flows such as profit two-phase.
3) the utility model can be used for the measurement of the oil-water two-phase flow system in the petroleum industry, and with respect to existing multiple measuring method, characteristics of the present utility model are to solve the engineering survey problem with the ingenious combination of traditional single-phase flow measurement instrument.Use the combination of Venturi tube and turbo flow meter and measure oil-water two-phase flow total volumetric flow rate, hybrid density, branch phase content, phase-splitting volumetric flow rate and phase-splitting mass rate simultaneously.Measurement is reliable, stable, precision is high, applied widely, easy for installation, volume is little.
Description of drawings
Accompanying drawing is based on the oil-water two-phase flow measurement mechanism structural representation of standard Venturi tube and turbo flow meter.
Embodiment
Restricting element selection standard Venturi tube in the utility model.After oil-water two-phase flow to be measured entered metering pipeline 1, by mixed flow device 2, oil-water two-phase flow is mixed became homogeneous flow earlier.Differential pressure pick-up 5 and the 3 supporting installations of standard Venturi tube.Differential pressure signal changes the standard electric signal into sends into computing machine 8 through A/D transition card 7.Turbo flow meter 4 obtains the profit total volumetric flow rate of whole pipeline and changes flow signal into the standard electric signal sends into computing machine 8 through A/D transition card 7.Temperature sensor 6 is used for detecting the oil-water two-phase flow temperature T and changes temperature signal into the standard electric signal sends into computing machine 8 through A/D transition card 7.In computing machine 8, be provided with memory module, store density and the data such as coefficient of flow of restricting element, perforated area of profit two-phase under different temperatures.Computing machine 8 is handled in real time, obtains the oil-water two-phase flow hybrid density, divides phase content and separate phase flow rate.
Realization profit two-phase measuring method for measuring is undertaken by following concrete steps:
(1) utilize turbo flow meter to obtain the profit two-phase total volumetric flow rate q of pipeline v, computing formula is as follows:
q v=ξf (1)
In the formula:
ξ is the coefficient of flow of turbo flow meter.Generally speaking, in specified flow range and in certain liquid viscosity scope, ξ and fluid viscosity are irrelevant, are constants.Because the viscosity of profit two-phase mixture is very high, so turbo flow meter is selected wide viscosity type turbo flow meter for use, to eliminate the influence of viscosity.F is the pulse output number of turbo flow meter.q vBe the oil-water two-phase flow total volumetric flow rate.
(2) the utility model adopts the standard knot fluid element, and measuring principle satisfies shellfish and makes great efforts equation and continuity equation, therefore according to Throttle Principle:
q v = α A 0 2 Δp ρ - - - ( 2 )
It is as follows to obtain profit two-phase hybrid density ρ computing formula:
ρ = 2 α 2 A 0 2 Δp q v 2 - - - ( 3 )
In the formula:
q vObtained by turbo flow meter, the differential pressure Δ p of restricting element place sampling pipe is obtained by differential pressure pick-up.α is a standard Venturi tube coefficient of flow, when fluid Reynolds number during greater than critical Reynolds number, is a constant, and concrete numerical value is by experimental calibration.A 0Be the restricting element perforated area.ρ is the oil-water two-phase flow hybrid density of restricting element of flowing through.
(3) owing to the oil-water two-phase flow hybrid density be:
ρ=x 1ρ 1+(1-x 12 (4)
Obtaining the profit two-phase by formula (4) divides phase content and separate phase flow rate computing formula as follows:
The rate that contains of oil is x 1 = ρ - ρ 2 ρ 1 - ρ 2
The rate that contains of water is x 2=1-x 1
The volumetric flow rate of oil is q V1msm=x 1q v
The volumetric flow rate of water is q V2msm=x 2q v
The mass rate of oil is q M11q V1msm
The mass rate of water is q M22q V2msm
In the formula:
ρ 1, ρ 2Be respectively the density of temperature be T time oil and water.Temperature T is obtained by temperature sensor.x 1, x 2Be respectively the rate that contains of oil and water.q V1msm, q V2msmBe respectively the volumetric flow rate of oil and water.q M1, q M2Be respectively the mass rate of oil and water.

Claims (3)

1. profit two-phase measurement mechanism based on standard Venturi tube and turbo flow meter, it is characterized in that it has metering pipeline (1), on metering pipeline (1), be provided with mixed flow device (2), standard Venturi tube (3), turbo flow meter (4), temperature sensor (6) successively, the supporting differential pressure pick-up (5) that is equipped with of standard Venturi tube (3), differential pressure pick-up (5), temperature sensor (6), turbo flow meter (4) link to each other with A/D transition card (7), and A/D transition card (7) links to each other with computing machine (8).
2. the described a kind of oil-water two-phase flow measurement mechanism based on standard Venturi tube and turbo flow meter of claim 1 is characterized in that said turbo flow meter adopts wide viscosity type turbo flow meter.
3. the described a kind of oil-water two-phase flow measurement mechanism based on standard Venturi tube and turbo flow meter of claim 1 is characterized in that said mixed flow device adopts single helical-ribbon type oar or two helical-ribbon type oar liquid liquid phase stirrer.
CN 200420022873 2004-05-15 2004-05-15 Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter Expired - Fee Related CN2699248Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200420022873 CN2699248Y (en) 2004-05-15 2004-05-15 Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200420022873 CN2699248Y (en) 2004-05-15 2004-05-15 Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter

Publications (1)

Publication Number Publication Date
CN2699248Y true CN2699248Y (en) 2005-05-11

Family

ID=34770537

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200420022873 Expired - Fee Related CN2699248Y (en) 2004-05-15 2004-05-15 Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter

Country Status (1)

Country Link
CN (1) CN2699248Y (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106092236A (en) * 2016-05-26 2016-11-09 深圳市联恒星科技有限公司 A kind of multiphase flow metering detecting system
CN106383069A (en) * 2016-10-12 2017-02-08 西安电子科技大学 Homogeneous gas-liquid mixed dielectric viscosity measuring device and method
CN107015551A (en) * 2016-01-06 2017-08-04 哈米尔顿森德斯特兰德公司 Save the intelligent Venturi tube of environmental control system (ECS)
CN117454063A (en) * 2023-12-26 2024-01-26 西南石油大学 Wellbore oil-gas-water multiphase flow state discrimination and water holdup calculation method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107015551A (en) * 2016-01-06 2017-08-04 哈米尔顿森德斯特兰德公司 Save the intelligent Venturi tube of environmental control system (ECS)
CN106092236A (en) * 2016-05-26 2016-11-09 深圳市联恒星科技有限公司 A kind of multiphase flow metering detecting system
CN106092236B (en) * 2016-05-26 2019-08-20 深圳市联恒星科技有限公司 A kind of multiphase flow metering detection system
CN106383069A (en) * 2016-10-12 2017-02-08 西安电子科技大学 Homogeneous gas-liquid mixed dielectric viscosity measuring device and method
CN106383069B (en) * 2016-10-12 2019-09-03 西安电子科技大学 A kind of homogeneity blending agent device for measuring viscosity and method
CN117454063A (en) * 2023-12-26 2024-01-26 西南石油大学 Wellbore oil-gas-water multiphase flow state discrimination and water holdup calculation method
CN117454063B (en) * 2023-12-26 2024-03-12 西南石油大学 Wellbore oil-gas-water multiphase flow state discrimination and water holdup calculation method

Similar Documents

Publication Publication Date Title
CN201818297U (en) Oil-gas-water three phase automatic metering device
US4236406A (en) Method and apparatus for sonic velocity type water cut measurement
US5608170A (en) Flow measurement system
CN101178347B (en) Narrow slit Venturi throttling set and gas-liquid two-phase flow measuring system
EP0523068A1 (en) Improvements to two and three-phase flow measurement.
GB2178174A (en) Method and apparatus for determining the amounts of petroleum and water in a crude oil outflow from a hydrocarbon well
CN101162165A (en) Low gas content gas-liquid two-phase flow measuring apparatus based on capacitance sensor and standard venturi tube
CN101666770A (en) Device and method for measuring crude oil with low air void
CN200979430Y (en) A flow measurement device for two-phase and three-media of gas-water-oil
CN201032457Y (en) Low gas content gas-liquid dual-phase flow measuring apparatus based on standard Venturi tube and vortex flowmeter
CN2699248Y (en) Oil-water double phase flow measuring apparatus based on standard Venturi tube and turbine flow meter
CN1746632A (en) Two-phase flow and dual parameter measurement with bent tube and flowmeter combination and system thereof
CN1259657A (en) measuring method of crude petroleum, natural gas and water multiphase flow and its measuring equipment
CN1247984C (en) Liquid-liquid two-phase flow measuring method and device
CN1673690A (en) Correlation measuring method and system for synchronous measuring two-phase flow rate and content of elbow
CN2699247Y (en) Liquid-liquid double phase flow measuring apparatus based on long throat neck Venturi tube and turbine flow meter
CN2731409Y (en) Two-phase flow measurer based on long throat venturi tube and elliptic gear flowmeter
CN2697601Y (en) Oil and water two-phase measurer based no Venturi tube and spring scraper flow meter
CN2342371Y (en) Automatic detector for core physical property
CN201032456Y (en) Low gas content gas-liquid dual-phase flow measuring apparatus based on capacity transducer and standard Venturi tube
CN103674139B (en) Based on the two-phase flow measurement method of mass flowmeter parametric statistics feature
CN2394225Y (en) Automatic oil metering and gas testing device for single well
CN2394226Y (en) Automatic oil metering and gas testing device for single well
CN102587885A (en) Device and method for metering crude oil output of wellhead
CN100587411C (en) Method for measuring liquid-liquid diphasic flow using dominant phase arbiter

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee