CN102322908B - Differential pressure type oil-gas-water three-phase metering device - Google Patents

Differential pressure type oil-gas-water three-phase metering device Download PDF

Info

Publication number
CN102322908B
CN102322908B CN201110229611XA CN201110229611A CN102322908B CN 102322908 B CN102322908 B CN 102322908B CN 201110229611X A CN201110229611X A CN 201110229611XA CN 201110229611 A CN201110229611 A CN 201110229611A CN 102322908 B CN102322908 B CN 102322908B
Authority
CN
China
Prior art keywords
gas
oil
water
differential pressure
separator
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
CN201110229611XA
Other languages
Chinese (zh)
Other versions
CN102322908A (en
Inventor
邰九龙
许文革
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.)
NANTONG FEIYU OIL SCIENCE AND TECHNOLOGY EXPLOITATION Co Ltd
Original Assignee
NANTONG FEIYU OIL SCIENCE AND TECHNOLOGY EXPLOITATION Co Ltd
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 NANTONG FEIYU OIL SCIENCE AND TECHNOLOGY EXPLOITATION Co Ltd filed Critical NANTONG FEIYU OIL SCIENCE AND TECHNOLOGY EXPLOITATION Co Ltd
Priority to CN201110229611XA priority Critical patent/CN102322908B/en
Publication of CN102322908A publication Critical patent/CN102322908A/en
Application granted granted Critical
Publication of CN102322908B publication Critical patent/CN102322908B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Measuring Volume Flow (AREA)

Abstract

The invention provides a differential pressure type oil-gas-water three-phase metering device, which comprises a constant temperature box, a gas and liquid separator, an oil and water separator and a computer collection control processing system, wherein a pressure return valve, a gas flow rate meter and a differential pressure sensor are connected onto the gas and liquid separator, a differential pressure sensor, an electromagnetic valve and a balance are connected onto the oil and water separator, and the gas and liquid separator is connected with the oil and water separator. The differential pressure type oil-gas-water three-phase metering device has the following technical effects that the oil and water emulsification and the gas generation do not need to be worried, the real-time effect is good, and the precision is high.

Description

Differential pressure type oil-gas-water three-phase metering device
Technical field
The present invention relates to a kind of WT-MSR, specifically, relate to a kind of differential pressure type oil-gas-water three-phase metering device.
Background technology
Oil, gas, water three phase metering device are used to measure displacement test endpiece oil gas aquatic products output, thereby confirm that the oil gas water is to the profit saturation value in the permeability test.Many weeks, oil, gas, water three phase metering are worldwide difficult problems, its metering method comprises optoelectronic scanning method, electric-resistivity method, density difference, bulking value method, capacitance method and differential pressure method etc.Every kind of method all has relative merits separately, and the optoelectronic scanning method is afraid of that oil pollutes transparent window and influences the real-time conversion of photosignal, when seriously polluted even can not work; Lose conducting function after the same greasy dirt with the optoelectronic scanning method of electric-resistivity method sticks electrode gradually, electrode can't be measured, hysteresis phenomenon is serious, fails the problem of fine solution oil-water emulsion; Density difference, bulking value method, real-time are good; Though be not afraid of oil-water emulsion; But influence profit density when gas occurring, density difference, bulking value method all adopt flexibility to hang the title method: promptly measuring container is hung on peaceful bottom through flexible rope, and the profit outlet is connected on the measuring container; Along with the increase gradually of profit weight, container is hung and is produced the value that distortion power influences balance between rope and the outlet connecting pipe.More than three kinds of methods all can not accurately measure, have only capacitance method and differential pressure method not only not to be afraid of oil-water emulsion but also be not afraid of generation gas, real-time is good.
Summary of the invention
The objective of the invention is to overcome the weak point of prior art, a kind of differential pressure type oil-gas-water three-phase metering device is provided.
Differential pressure type oil-gas-water three-phase metering device of the present invention; Comprise constant temperature oven, gas-liquid separator, oil-water separator and computer acquisition control processing system; Be connected with check valve, gas meter and No. 2 differential pressure pick-ups on the said gas-liquid separator; Be connected with differential pressure pick-up, solenoid valve and balance on the oil-water separator No. 1, gas-liquid separator links to each other with oil-water separator.
Preferably,
Said gas-liquid separator upper end is provided with positive umbrella shape device, and the lower end is provided with the device of falling the umbrella shape.
Said oil-water separator is the ring pipe structure, and the left side of separation vessel is output liquid and emulsion end, and the right side is a test lead.
Differential pressure method oil-gas-water three-phase metering device of the present invention has following technique effect: not only be not afraid of oil-water emulsion but also be not afraid of generation gas, real-time is good, precision is high.
Description of drawings
Fig. 1 is the structural representation of differential pressure type oil-gas-water three-phase metering device of the present invention;
Fig. 2 is the structural representation of the gas-liquid separator of differential pressure type oil-gas-water three-phase metering device of the present invention;
Fig. 3 is the structural representation of the oil-water separator of differential pressure type oil-gas-water three-phase metering device of the present invention;
Fig. 4 is the software interface figure of differential pressure type oil-gas-water three-phase metering device of the present invention.
Embodiment
As shown in Figure 1; Differential pressure type oil-gas-water three-phase metering device of the present invention comprises constant temperature oven, gas-liquid separator, oil-water separator and computer acquisition control processing system; Be connected with check valve, gas meter and No. 2 differential pressure pick-ups on the said gas-liquid separator; Be connected with differential pressure pick-up, solenoid valve and balance on the oil-water separator No. 1, gas-liquid separator links to each other with oil-water separator.
As shown in Figure 2, gas-liquid separator employing transparent material is processed and is convenient to observe, and a positive umbrella shape device is adorned in the upper end, and the lower end is the device of falling the umbrella shape.When gas and liquid mixture when inlet end gets into separation vessel; Liquid flows to the lower end of separation vessel through umbrella shape device appearance; Gas shows to get into gas meter in the umbrella shape device, make gas-liquid separation more thoroughly gas measure by flowmeter, through the RS232 interface by computer data acquisition.
As shown in Figure 3, oil-water separator adopts ring pipe version, and clear glass is processed, and selects the oil-water separator of different volumes according to the volume of output liquid, and the separation vessel of the different ranges of system configuration supplies experimental selection, 50mL; 80mL; 120mL; 150mL; 200mL; 300mL; Each 5 of 500mL.The left side of separation vessel is output liquid and emulsion end, and the right side is a test lead.Before experiment, must demarcate the pairing volume of promptly different differential pressure value to oil-water separator.
Differential pressure pick-up has two, adopts the U.S. STD924 of Honeywell company product; Range is respectively 0-2KPa; 0-5KPa, precision is 0.1%.Power supply 9-36V, output 0-5V is through the communication of A/D change-over panel and computing machine.Differential pressure value is respectively through the secondary instrument demonstration and through RS-232 communication interface and computing machine communication.Electronic balance adopts German Sai Duodesi import balance, range 1200g; Precision 1%.Data acquisition system (DAS) comprises the instant numerical value of gathering 7 groups of pressure, temperature, balance flow and constant-flux pump pressure etc.
For guaranteeing the reliability of measuring accuracy and control, adopt C168H digital collection control card, thereby realize the digital collection transmission.Software moves under the Windows2000/XP environment, adopts the Delphi programming.The instrument workflow is presented on the interface, can realize man-machine conversation, after operating personnel configure parameter; Just can unmanned; Computing machine can be gathered all pressure, flow automatically, the treated raw data form that generates of the data of computer acquisition, analytical statement and curve map; Generate the database file form simultaneously so that user flexibility is used, as shown in Figure 4.
The important technological parameters of differential pressure type oil-gas-water three-phase metering device of the present invention: constant temperature oven operating room size: 600 * 600 * 1000; Working temperature: 100 ℃ of maximum temperatures; Temperature measurement precision: ± 0.5 ℃; Pressure measurement scope: ⊿ P 10-2KPa ⊿ P 20-5Kpa; Pressure measurement precision: 1 ‰; Gas dosing precision: 2ml; Oil gas metering precision: 0.1g; Check valve controlled pressure: 2-60Mpa; Back pressure control accuracy≤0.02; Supply voltage: AC220V; Dissipated power: 3.5KW.
The workflow of differential pressure type oil-gas-water three-phase metering device of the present invention is following:
Oil, gas, water three-phase get into from separator inlet, because oil, water and emulsion density have nothing in common with each other, oil rises to the oil-water separator upper end, and emulsion rests on the centre of gauge line left side oil and water.The liquid-column height that differential pressure pick-up 1 records in the fine pipeline is a liquid measure, and when surpassing the upper end liquid level, computing machine is opened through D/O input/output board enabled instruction solenoid valve, and water flows on the electronic balance through solenoid valve in the bottom.No matter come in from gas-liquid separator is water or oil, and overflowing through solenoid valve all is water, and promptly metering is water.What differential pressure pick-up 2 measured is that oily increment is an oil mass, the BVO that the ring pipe volume requirement is displaced greater than model.Before doing experiment, to carefully demarcate the volume of ring pipe, promptly at the volume of differing heights.
High precision differential pressure pick-up 2 is measured oil, water termination and accurate position, can record the volume of oil and water in the separation vessel exactly through this potential difference.When separator inlet is come in water; Oil, water termination rise, and computing machine becomes big through the value of the differential pressure pick-up that the A/D change-over panel collects, and computing machine sends instruction and opens motorized valve through the D/O input/output board; Make its oil, water termination get back to initial interface, close motorized valve automatically.At this moment, the value that balance increased is exactly the volume that flows into profit from separator inlet.

Claims (1)

1. differential pressure type oil-gas-water three-phase metering device is characterized in that, comprises constant temperature oven, gas-liquid separator, oil-water separator and computer acquisition control processing system; Be connected with check valve, gas meter and No. 2 differential pressure pick-ups on the said gas-liquid separator; Be connected with differential pressure pick-up, solenoid valve and balance on the oil-water separator No. 1, gas-liquid separator links to each other with oil-water separator, and said gas-liquid separator upper end is provided with positive umbrella shape device; The lower end is provided with the device of falling the umbrella shape; Said oil-water separator is the ring pipe structure, and the left side of separation vessel is output liquid and emulsion end, and the right side is a test lead.
CN201110229611XA 2011-08-11 2011-08-11 Differential pressure type oil-gas-water three-phase metering device Expired - Fee Related CN102322908B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201110229611XA CN102322908B (en) 2011-08-11 2011-08-11 Differential pressure type oil-gas-water three-phase metering device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201110229611XA CN102322908B (en) 2011-08-11 2011-08-11 Differential pressure type oil-gas-water three-phase metering device

Publications (2)

Publication Number Publication Date
CN102322908A CN102322908A (en) 2012-01-18
CN102322908B true CN102322908B (en) 2012-11-14

Family

ID=45450701

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201110229611XA Expired - Fee Related CN102322908B (en) 2011-08-11 2011-08-11 Differential pressure type oil-gas-water three-phase metering device

Country Status (1)

Country Link
CN (1) CN102322908B (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103292843B (en) * 2013-07-15 2015-05-20 钱如树 Oil and water two-phase metering device
CN103645302B (en) * 2013-12-17 2015-12-30 中国石油大学(北京) Realize CO 2displacement of reservoir oil dynamic monitoring and inverting dynamic simulation experimental device and method
CN103823045B (en) * 2014-02-26 2016-01-20 中国海洋石油总公司 Heavy crude heat extraction logistics organizations produced fluid is separated and gathers metering method and device
CN104089665A (en) * 2014-06-26 2014-10-08 卢玖庆 Single-pipe three-phase flowmeter
CN108017033B (en) * 2016-10-28 2021-06-11 株式会社龙野 Oil filling device
CN107144312B (en) * 2017-05-26 2019-10-18 苏州天大泰和自控仪表技术有限公司 Flow measuring apparatus and flow meter assembly
CN108342218A (en) * 2018-01-20 2018-07-31 盘锦北方沥青股份有限公司 A kind of petroleum substance automatic dehydration system
CN108412479A (en) * 2018-02-06 2018-08-17 常州大学 A kind of oil-water separation metering device and method for displacement test
CN108709842B (en) * 2018-04-26 2021-03-09 中国石油天然气股份有限公司 Oil-water separation metering method and device
CN108590626B (en) * 2018-04-27 2021-06-25 成都理工大学 Oil-gas-water three-phase trace automatic metering device and method
CN109752507A (en) * 2019-03-06 2019-05-14 重庆科技学院 A kind of rock core displacement test oil-gas-water metering device
CN113075110A (en) * 2021-04-06 2021-07-06 西南石油大学 Multifunctional accurate metering device for rock core displacement experiment

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4852395A (en) * 1988-12-08 1989-08-01 Atlantic Richfield Company Three phase fluid flow measuring system
CN2407331Y (en) * 2000-02-24 2000-11-22 王家禄 Accurate automatic oil-gas-water flowmeter
CN2537960Y (en) * 2002-04-28 2003-02-26 西安朗森科技有限责任公司 High precision oil gas and water three phase flow automatic meter
CN2574019Y (en) * 2002-09-30 2003-09-17 刘宝和 Automatic oil-gas-water meter
CN1696619A (en) * 2004-05-14 2005-11-16 寿焕根 Device for automatic measuring oil and gas
CN2783275Y (en) * 2005-04-15 2006-05-24 浙江大学 Three-phase flow continuous metering system for oil, gas and water with high water content
CN101042304A (en) * 2007-04-24 2007-09-26 胜利油田胜利工程设计咨询有限责任公司 Oil gas and water mixed flow phase-splitting contimuous measuring equipment
CN200984473Y (en) * 2006-12-21 2007-12-05 吴培森 Full-automatic air, liquid and oil three-phase separation apparatus

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7707897B2 (en) * 2008-05-27 2010-05-04 Baker Hughes Incorporated Method of measuring multiphase flow using a multi-stage flow meter

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4852395A (en) * 1988-12-08 1989-08-01 Atlantic Richfield Company Three phase fluid flow measuring system
CN2407331Y (en) * 2000-02-24 2000-11-22 王家禄 Accurate automatic oil-gas-water flowmeter
CN2537960Y (en) * 2002-04-28 2003-02-26 西安朗森科技有限责任公司 High precision oil gas and water three phase flow automatic meter
CN2574019Y (en) * 2002-09-30 2003-09-17 刘宝和 Automatic oil-gas-water meter
CN1696619A (en) * 2004-05-14 2005-11-16 寿焕根 Device for automatic measuring oil and gas
CN2783275Y (en) * 2005-04-15 2006-05-24 浙江大学 Three-phase flow continuous metering system for oil, gas and water with high water content
CN200984473Y (en) * 2006-12-21 2007-12-05 吴培森 Full-automatic air, liquid and oil three-phase separation apparatus
CN101042304A (en) * 2007-04-24 2007-09-26 胜利油田胜利工程设计咨询有限责任公司 Oil gas and water mixed flow phase-splitting contimuous measuring equipment

Also Published As

Publication number Publication date
CN102322908A (en) 2012-01-18

Similar Documents

Publication Publication Date Title
CN102322908B (en) Differential pressure type oil-gas-water three-phase metering device
CN203658217U (en) Seepage starting pressure gradient test device
CN201705330U (en) Mobile Oil Well Multiphase Flow Metering Device
CN2826373Y (en) Oil-gas-water automatic gauging instrument
CN103257099A (en) Device for measuring seepage of porous medium
CN101464181A (en) Quantitative weighing system based on buoyant force weighing sensing principle
CN101629890B (en) Float type fiber grating liquid densimeter
CN202188873U (en) Differential pressure type oil, gas and water three-phase metering device
CN201892552U (en) Oil, gas and water multiphase flowmeter
CN111141332B (en) Flow guiding device for distilled liquor picking process and online measuring system and method
CN104977227A (en) Online liquid density meter
CN101794627B (en) Rod position measuring device based on differential pressure variation
CN211824530U (en) Guiding device and online measurement system for liquor picking process of distilled liquor
CN104234691A (en) High-precision real-time online multi-phase flow meter for oil field
CN202066539U (en) Device used for high-precisely and automatically measuring flow rate of liquid
CN201650537U (en) Microcomputer high-precision fuel-measuring test-bed for fuel injection pump
CN205619974U (en) Laboratory is with physical simulation high accuracy three-phase metering device
CN102749119B (en) Liquid volume metering method and continuous metering method
CN2704825Y (en) Meter regulator for oil, vapour and water output
Wang et al. Study on flow velocity distribution in open channel with flexible vegetation
CN201780286U (en) Light-operated metering device
CN201464321U (en) Float type fiber-grating liquid densitometer
CN109506882A (en) The experimental provision and method that a kind of slip boundary condition density current and salt wedge generate
CN201420546Y (en) Full-automatic differential pressure weighing type oil-gas metering device
CN201241693Y (en) Slurry flow measuring tank

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20121114

CF01 Termination of patent right due to non-payment of annual fee