CN102322908A - Differential pressure type oil-gas-water three-phase metering device - Google Patents
Differential pressure type oil-gas-water three-phase metering device Download PDFInfo
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- CN102322908A CN102322908A CN 201110229611 CN201110229611A CN102322908A CN 102322908 A CN102322908 A CN 102322908A CN 201110229611 CN201110229611 CN 201110229611 CN 201110229611 A CN201110229611 A CN 201110229611A CN 102322908 A CN102322908 A CN 102322908A
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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
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 differential pressure pick-up on the said gas-liquid separator; Be connected with differential pressure pick-up, solenoid valve and balance on the oil-water separator, 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 differential pressure pick-up 2 on the said gas-liquid separator; Be connected with differential pressure pick-up 1, solenoid valve and balance on the oil-water separator, 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 (3)
1. differential pressure type oil-gas-water three-phase metering device; It is characterized in that; Comprise constant temperature oven, gas-liquid separator, oil-water separator and computer acquisition control processing system; Be connected with check valve, gas meter and differential pressure pick-up on the said gas-liquid separator, be connected with differential pressure pick-up, solenoid valve and balance on the oil-water separator, gas-liquid separator links to each other with oil-water separator.
2. differential pressure type oil-gas-water three-phase metering device according to claim 1 is characterized in that, 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.
3. differential pressure type oil-gas-water three-phase metering device according to claim 1 is characterized in that 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.
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| CN201110229611XA CN102322908B (en) | 2011-08-11 | 2011-08-11 | Differential pressure type oil-gas-water three-phase metering device |
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| CN201110229611XA CN102322908B (en) | 2011-08-11 | 2011-08-11 | Differential pressure type oil-gas-water three-phase metering device |
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| CN102322908B CN102322908B (en) | 2012-11-14 |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103292843A (en) * | 2013-07-15 | 2013-09-11 | 钱如树 | Oil and water two-phase metering device |
| CN103645302A (en) * | 2013-12-17 | 2014-03-19 | 中国石油大学(北京) | Experiment device and method for realizing CO2 reservoir oil displacement dynamic monitoring and inversion dynamic simulation |
| CN103823045A (en) * | 2014-02-26 | 2014-05-28 | 中国海洋石油总公司 | Separating, acquiring and metering method and apparatus for fluid produced in thermal recovery physical simulation experiment on heavy oil |
| CN104089665A (en) * | 2014-06-26 | 2014-10-08 | 卢玖庆 | Single-pipe three-phase flowmeter |
| CN107144312A (en) * | 2017-05-26 | 2017-09-08 | 苏州天大泰和自控仪表技术有限公司 | Flow measuring apparatus and flow meter assembly |
| CN108017033A (en) * | 2016-10-28 | 2018-05-11 | 株式会社龙野 | Refueling device |
| 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 |
| CN108590626A (en) * | 2018-04-27 | 2018-09-28 | 成都理工大学 | A kind of micro self-measuring device of oil gas water three phase and method |
| CN108709842A (en) * | 2018-04-26 | 2018-10-26 | 中国石油天然气股份有限公司 | A kind of oil-water separation metering method and device |
| 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 |
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Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103292843A (en) * | 2013-07-15 | 2013-09-11 | 钱如树 | Oil and water two-phase metering device |
| CN103292843B (en) * | 2013-07-15 | 2015-05-20 | 钱如树 | Oil and water two-phase metering device |
| CN103645302A (en) * | 2013-12-17 | 2014-03-19 | 中国石油大学(北京) | Experiment device and method for realizing CO2 reservoir oil displacement dynamic monitoring and inversion dynamic simulation |
| 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 |
| CN103823045A (en) * | 2014-02-26 | 2014-05-28 | 中国海洋石油总公司 | Separating, acquiring and metering method and apparatus for fluid produced in thermal recovery physical simulation experiment on heavy oil |
| 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 |
| CN108017033A (en) * | 2016-10-28 | 2018-05-11 | 株式会社龙野 | Refueling device |
| CN108017033B (en) * | 2016-10-28 | 2021-06-11 | 株式会社龙野 | Oil filling device |
| CN107144312A (en) * | 2017-05-26 | 2017-09-08 | 苏州天大泰和自控仪表技术有限公司 | Flow measuring apparatus and flow meter assembly |
| 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 |
| CN108709842A (en) * | 2018-04-26 | 2018-10-26 | 中国石油天然气股份有限公司 | A kind of oil-water separation metering method and device |
| 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 |
| CN108590626A (en) * | 2018-04-27 | 2018-09-28 | 成都理工大学 | A kind of micro self-measuring device of oil gas water three phase 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 |
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