CN200979427Y - An automatic measurement device for the oil well three-phase flow - Google Patents
An automatic measurement device for the oil well three-phase flow Download PDFInfo
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- CN200979427Y CN200979427Y CN 200620079589 CN200620079589U CN200979427Y CN 200979427 Y CN200979427 Y CN 200979427Y CN 200620079589 CN200620079589 CN 200620079589 CN 200620079589 U CN200620079589 U CN 200620079589U CN 200979427 Y CN200979427 Y CN 200979427Y
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Abstract
The utility model relates to a well-producing oil-water-gas three-phase flow automatic metering device. A separation control jug, a fluid flow meter, an oil-water-gas compositional instruction, a gas metering instrument and a gas-liquid dashpot are connected through a flange and a pipe line to form an oil-water-gas phase-splitting gage ductwork. The separation control jug is connected with a gas discharging pipe and a gas-liquid admitting pipe in the upper portion, is arranged with a float adjusting valve inside, and is connected with a liquid outlet pipe on the lower portion, wherein, the gas discharging pipe is current collected with a liquid discharging pipe and is connected with a gas-liquid outlet pipe. The gas discharging pipe is arranged with a gas metrical instrument. The liquid discharging pipe is arranged with a fluid flow meter and an oil-water-gas compositional instruction. The metering accuracy of the utility model is high, the designed liquid metering accuracy can achieve more than +-1%, the real metering accuracy can achieve within +-2%, and the repetitiveness and reliability are good. The measuring range is wide and can reach over 1:30 at most, the linearity is good, and is especially suitable for measuring the oil well which has low production, interval producing and bigger gas change. The utility model has the advantages of high automation degree, simple structure, small volume, light weight, portable and time-saving dismounting and simple repair, thereby the utility model is very suitable for prize measuring and multi-phase measuring of ocean platform, and is suitable to be mounted and used in the environment of desert, high-cold oil field with unattended operation.
Description
Technical field
The utility model relates to a kind of produced liquid in oil well three-phase flow metering device, especially profit gas three-phase flow flow self-measuring device.
Background technology
The metering of oil well output is an important process in the field production management, measures oil well output accurately, timely, to grasping the oil reservoir situation, formulates production decision, has crucial directive significance.
At present, the production metering of oil wells method of domestic each Oilfield using mainly contains glass tube oil gauge, tipping bucket gauging, software gauging, two-phase partition density method and three-phase separator measurement method etc.Glass tube oil gauge is the classic method that generally adopt in domestic each oil field, accounts for more than 80% of oil well sum, adopts the mode of intermittence, human metering to convert output, and the metering system error is bigger.Software instrument gauging is the oil well at the characteristics or the ring-type flow process of oil well low yield weak breath, used the gauging mode of principles such as liquid level build-up method, power graph method, usually adopt portable gauging instrument to measure the production fluid amount of oil well at well head, this gauging mode can reduce investment significantly, streamlining management, but also have its limitation, can not use, and to intermittently oil well result of use fuel-displaced, that tolerance is bigger is undesirable for the oil well of ring-type flow process, screw pump oil production.Therefore oil well measurement will be along with the variation of development of technology and oil-field development form, needs more and more that function is strong, measuring accuracy, metering outfit that automaticity is high, to reduce labor strength, to raise labour productivity and the management level in oil field.In existing oil well measurement technology, Chinese patent discloses a kind of " oil gas self-measuring device " (ZL 200420041937.5), provided a kind of oil gas self-measuring device, and the application of having succeeded in the production in oil field by land, but said apparatus especially is applied to skid measurement and ocean platform for oil well measurement, it is complicated that its structure still seems, has volume defective bigger than normal.
Summary of the invention
In order to overcome the deficiencies in the prior art part, the purpose of this utility model is for a kind of automatic metering device for oil well three-phase flow is provided; This measuring apparatus is simple in structure, volume is little; Need not automatically controlled backup system, the pressure loss is little; Be applicable to that the automatic phase-splitting on-line metering of Oil, Water, Gas of multiple flow patterns such as individual well, gas-liquid delivery, especially skid-mounted type are measured and the multiphase flow rates of ocean platform is measured, and phase-splitting liquid capacity metering degree of accuracy can reach ± 1～2%.
The purpose of this utility model can realize by following measure:
A kind of automatic metering device for oil well three-phase flow is to connect to form profit gas phase-splitting metering pipe network by flange and pipeline separating controlling jar, liquid flowmeter, profit gas component instrument, gas meter, gas-liquid surge tank.Separating controlling jar top links to each other with gas outlet tube, gas-liquid induction pipe, its underpart is communicated with liquid outlet tube, gas-liquid induction pipe and separating controlling jar connecting place are provided with the gas-liquid cyclone centrifugal separator, in the separating controlling jar flow regulation valve is housed, gas vent valve and gas meter are housed on the outlet gas line, between gas meter endpiece and the gas-liquid header gas-liquid surge tank are housed; Liquid outlet valve, liquid flowmeter and profit gas component instrument are housed on the liquid exit line; Gas-liquid header place has the gas liquid outlet pipe, and pressure unit and temperature transmitter all are located on the separating controlling jar.
Above-mentioned gas-liquid cyclone centrifugal separator is columnar structured, vertically places the middle and upper part in the separating controlling jar, and the center symmetry; Its centrifugal separator end that enters the mouth links to each other with the gas-liquid induction pipe, and the other end is connected with spiral centrifuge tube tangent line; The spiral centrifuge tube is square or rectangle, and spiral places guiding to separate in the sleeve pipe from top to bottom, and spiral is at least two circles, and the circulation area of spiral centrifuge tube is less than or equal to the circulation area of gas-liquid induction pipe; Guiding is separated sleeve pipe and is the hollow sleeve tubulose, and is concentric with the separating controlling jar, on the hypomere box face mesh arranged.
The valve seat connecting pipe of above-mentioned flow regulation valve is connected with valve seat, gas outlet tube smooth transition, the valve seat connecting pipe is communicated with gas outlet tube, and be fixed on the bottom at end cap center, separating controlling tank top, and there is a valve opening at the valve seat center, and the valve opening diameter is less than the gas outlet tube caliber; The bottom surface of spool is connected with the valve body smooth transition; One end of floating ball rod is connected with valve body center symmetry smooth transition, and other end center symmetry penetrates ball float, and smooth transition connects; Spool is a cone; Valve body is smooth sphere shape or truncated cone-shaped, and its external diameter is greater than the valve opening aperture; Ball float is hollow ball or hollow cylinder, places on the ball float guides in the separating controlling jar, and floating ball rod is the pipe of diameter less than valve diameter.
Guide rod one end of above-mentioned ball float guides is vertically fixed on the center on chassis, and the other end straight up; Chassis level is fixed in middle and lower part and concentricity with the gas-liquid separation controlling tank in the separating controlling jar, has into the liquid flow hole of net form on the chassis.The circulation area of above-mentioned spiral centrifuge tube is less than or equal to the circulation area of gas-liquid induction pipe.
Guiding is separated the external diameter of the internal diameter of sleeve pipe greater than ball float, and guiding separation sleeve external diameter of pipe is less than or equal to separating controlling jar internal diameter.
The surface of contact of valve body and valve opening is smooth sphere shape or truncated cone-shaped.
Spool tapering size and cone length depend on measures gas-liquid range ability size, and its maximum sole diameter is less than valve opening;
The diameter of guide rod is less than the internal diameter of floating ball rod, and length is greater than the length of spool; Total circulation area of liquid flow hole perforate is greater than the circulation area of gas-liquid induction pipe.
Liquid level height when the gas liquid outlet height of gas-liquid header is higher than the ball float floating that places in the separating controlling jar; Be lower than valve body and push up the liquid level of valve seat in the separating controlling jar.
The volume of gas-liquid surge tank arrives the volume in the pipeline between the gas-liquid surge tank upper end greater than gas outlet tube.
The utility model compared with prior art has following advantage:
1, the utility model is simple in structure, volume is little, in light weight, dismounting is convenient saves time, the automaticity height is highly suitable for installing and using among the multiphase flow measurement of skid measurement and ocean platform and land, desert, the high and cold oil field unattended operation environment.
2, the utility model measuring accuracy height, and not influenced by gas-liquid flow pattern and fluid state, design liquid volume measurement error can reach more than 1.0%, the actual metered error can reach ± 2% in, and repeatability, good reliability.
3, measurement broad quantum of the present utility model, maximum can reach more than 1: 30, and good linearity, is particularly useful for low yield, intermittently fuel-displaced, tolerance changes well measurement greatly.
4, the utility model gas-liquid individual phase measurement is steady, and whole device does not have auxiliary electric-control system, and Max pressure loss is less than 0.025MPa;
Description of drawings
Fig. 1 is a structural representation of the present utility model
Fig. 2 a is the structural representation of gas-liquid cyclone centrifugal separator
Fig. 2 b is a guiding separation sleeve pipe network hole synoptic diagram
Fig. 3 a is valve seat connecting piece and valve seat construction synoptic diagram
Fig. 3 b is the flow regulation valve structural representation
Fig. 4 is a ball float guide structure synoptic diagram
Description of reference numerals is as follows:
1-gas-liquid induction pipe 2-separating controlling jar 3-separating controlling tank top end cap
4-gas-liquid cyclone centrifugal separator 41-centrifugal separator inlet 42-spiral centrifuge tube
The 43-guiding is separated sleeve pipe 44-mesh
5-flow regulation valve 50-valve seat connecting pipe 51-valve seat 511-valve opening 52-spool
53-valve body 54-floating ball rod 55-ball float
6-gas outlet tube 7-ball float guides 71-guide rod 72-chassis 73-liquid flow hole
8-liquid outlet tube 9-liquid outlet valve 10-liquid flowmeter 11-profit gas component instrument
12-gas vent valve 13-gas meter 14-gas-liquid surge tank 15-gas-liquid header
16-gas liquid outlet pipe 17-pressure unit 18-temperature transmitter 19-controlling tank base
20-blowoff valve 21-measuring apparatus base
Embodiment
Below in conjunction with accompanying drawing the utility model is described in any further:
As shown in Figure 1, gas-liquid induction pipe 1 is connected with the centrifugal separator inlet 41 of the gas-liquid cyclone centrifugal separator 4 that is arranged at separating controlling jar 2 interior middle and upper parts, separating controlling jar 2 tops are communicated with gas outlet tube 6, gas and liquid mixture enters gas-liquid cyclone centrifugal separator 4 by gas-liquid induction pipe 1 (tangentially), gas-liquid realizes the gas-liquid initial gross separation by spiral centrifuge tube 42, the air containing fluid that separates through spiral centrifuge tube 42 is at inertia---separates continuation centrifuging in the sleeve pipe 43 in guiding under gravity and the action of centrifugal force, the back flows down along the inwall of separating controlling jar 2, through the centrifuging of gas-liquid cyclone centrifugal separator 4, can reach separation fully and the centrifuging of most of hatching gas thus by the free gas in the gas and liquid mixture of gas-liquid induction pipe 1.
Gas-liquid cyclone centrifugal separator 4 is columnar structured, vertically place the middle and upper part in the separating controlling jar 2, and center symmetry (with reference to Fig. 2 a, Fig. 2 b), centrifugal separator 41 1 ends that enter the mouth link to each other with gas-liquid induction pipe 1, and the other end is communicated with spiral centrifuge tube 42 (tangentially); Spiral centrifuge tube 42 is square, and spiral places guiding to separate in the sleeve pipe 43 from top to bottom, and spiral is two circles, and the circulation area of spiral centrifuge tube 42 is less than or equal to the circulation area of gas-liquid induction pipe 1; Guiding is separated sleeve pipe 43 and is the hollow sleeve tubulose, and is concentric with separating controlling jar 2, and mesh 44 is arranged on the hypomere box face, so that increase liquid gas release surface, guarantees separated gas upper reaches of separating out; The external diameter of gas-liquid cyclone centrifugal separator 4 is less than the internal diameter of separating controlling jar 2, its objective is in order to flow down along separating controlling jar 2 inwalls from the fallen liquid of spiral centrifuge tube 42 eddy flows, a small amount of remaining gas is further separated out, when avoiding simultaneously pulsing feed liquor and feed liquor to the disturbance of ball float 55.
Separating controlling jar 2 mainly is made up of can body, separating controlling tank top end cap 3, gas-liquid cyclone centrifugal separator 4, flow regulation valve 5, gas outlet tube 6, liquid outlet tube 8, blowoff valve 20 and ball float guides 7: separating controlling tank top end cap 3 is fixed by bolts to the top of can body, and valve seat connecting pipe 50 is fastened on the separating controlling tank top end cap 3 with valve seat 51; The outlet valve seat connecting pipe 50 of flow regulation valve 5 is connected with gas outlet tube 6 and gas outlet valve 12, and the back links to each other with gas liquid outlet pipe 16 with gas meter 13, gas-liquid surge tank 14, gas-liquid header 15 again; Separating controlling jar 2 middle and lower parts are provided with liquid outlet tube 8, and liquid outlet valve 9, liquid flowmeter 10 and profit gas component instrument 11 are housed on the liquid exit line; The bottom is provided with sewage draining exit 20.Separating controlling jar 2 bottoms are provided with separating controlling jar base 19, and whole erection seat drops on the measuring apparatus base 21.
Shown in Fig. 3 a, 3b, flow regulation valve 5 is located at the inside of separating controlling jar 2, is made up of valve seat connecting pipe 50, valve seat 51, spool 52, valve body 53, floating ball rod 54, ball float 55.Valve seat connecting pipe 50 is fixed on the bottom at end cap 3 centers, separating controlling tank top, and valve seat connecting pipe 50 is connected with valve seat 51, gas outlet tube 6 smooth transition, and there is a valve opening 511 at valve seat 51 centers, and valve opening 511 apertures are less than gas outlet tube 6 calibers; Spool 52 is a cone, and tapering size and cone length depend on measures gas-liquid range ability size, and its maximum sole diameter is less than valve opening 511 apertures; Valve body 53 is smooth sphere shapes with the surface of contact of valve seat 51, and valve body 53 its maximum outside diameters are greater than valve opening 511 apertures; The bottom surface of spool 52 (largest end face) is connected with valve body 53 smooth transition; Floating ball rod 54 is the pipe of diameter less than valve body 53, and ball float 55 is a hollow cylinder; One end of floating ball rod 54 is connected with valve body 53 centers symmetry smooth transition, and other end center symmetry penetrates ball float 55 and smooth transition connects; Ball float 55 places on the ball float guides 7 in the separating controlling jar 2, and fluctuating on the ball float guides 7 with the tank level fluctuation under buoyancy function: the level fluctuation of separating controlling jar 2 acts on knee-action in the valve opening 511 of spools 52 at valve seat 51 by ball float 55 by floating ball rod 54, with the free area of adjustments of gas outlet, reach automatic adjusting with this and stablize in the separating controlling jar 2 and the pressure reduction between the gas liquid outlet pipe 16 and the gas flow on control tank body top and the fluid flow of bottom.
With reference to Fig. 4, ball float guides 7 places middle and lower part and concentric in the separating controlling jar 2, and ball float guides 7 is made up of guide rod 71, chassis 72 and liquid flow hole 73.Guide rod 71 1 ends are vertically fixed on the center on chassis 72, and the other end straight up.The diameter of guide rod 71 is less than the internal diameter of floating ball rod 54, the length length greater than spool 52; Chassis 72 horizontal fixed place middle and lower part and concentricity with tank body in the gas-liquid separation controlling tank 2, have the liquid flow hole 73 that is net form on the chassis 72, total circulation area of institute's perforate is greater than the circulation area of induction pipe 1, with guarantee the ball float guides about in the of 7 liquid do not have crushing and flow.The purpose that ball float guides 7 is set is to be used to control ball float 55 swing when liquid level rises or descend and influence the stable of liquid level.
Liquid outlet tube 8, liquid outlet valve 9 and liquid flowmeter 10 link to each other on same pipeline, profit gas component instrument 11 vertically is connected in 15 of the endpiece of liquid flowmeter 10 and gas-liquid headers, liquid level when the Horizontal Exit height of gas-liquid header 15 need be higher than ball float 55 floatings that place in the separating controlling jar 2 is lower than valve body 53 and pushes up the liquid level of valve seat 51 in separating controlling jar 2; Gas-liquid surge tank 14 lower ends vertically are connected with gas-liquid header 15, the upper end is connected with gas meter 13 outlets, the volume of gas-liquid surge tank 14 needs to arrive the volume in the pipeline between gas-liquid surge tank 14 upper ends greater than gas outlet tube 6, its objective is the measuring accuracy that influences gas meter 13 in order to stop backflowing of gas-liquid header 15 place's liquid.
The utility model adopts centrifugal cyclone separation and Floating Ball Liquid Level to regulate control, and the separation fully that free gas in the pipeline gas/liquid mixed liquor has been satisfied in effective combination separates with most of hatching the automatic of gas.Flow regulation valve 5 utilizes that liquid level height has directly been controlled the flow of gas vent, the flow of the indirect controlling liquid outlet of differential pressure that forms by the height and the liquid road flow resistance of outlet gas-liquid header 15, has realized the automatic steady control to the gas-liquid flow; Its principle of work is: profit gas mixed liquor is realized the initial gross separation of free gas centrifugal cyclone by spiral centrifuge tube 42, the air containing fluid that separates through spiral centrifuge tube 42 separates continuation centrifuging in the sleeve pipe 43 in the effect lower edge of inertia (gravity and centrifugal force) guiding, the back flows down along the inwall of separating controlling jar 2, through the centrifuging of gas-liquid cyclone centrifugal separator 4, the free gas in the gas and liquid mixture that pipeline comes can reach and separate fully and the centrifuging of most of hatching gas thus.
Before separating controlling jar 2 normal liquid levels were not set up as yet, flow regulation valve 5 was in position, the end, the state of promptly opening fully for a short time in the effect of gravity.Separated gas is by without hindrance discharge between the valve opening 511 opened and the spool 52, this moment since jar in a liquid level be lower than the open height that of outlet gas-liquid header 15, no liquid measure discharge; When rising to the range of control lower limit gradually and continue, the liquid level of separating controlling jar 2 rises, ball float 55 under buoyancy function along ball float guides 7 buoyance lift upwards, spool 52 rises with ball float 55, circulation area between valve opening 511 and the spool 52 reduces, the gas discharge rate reduces, liquid level further rises in jar, separating controlling jar 2 rises gradually with the differential pressure at gas-liquid header 15 places, liquid level rises to the height that is higher than 15 outlets of gas-liquid header in jar, when the jar internal pressure reaches the required pressure reduction of discharge opeing (flow resistance differential pressure) with the differential pressure that exports header 15, liquid begins to discharge separating controlling jar 2, gas-liquid induction pipe 1 comes liquid big at this moment, liquid level continues to rise in jar, then the gas delivery flow reduces, differential pressure increases, and draining flow increases thereupon; A jar interior liquid level begins to descend subsequently, the ball-cock assembly circulation area becomes greatly, the increase of outlet tolerance, and differential pressure reduces thereupon, and the outlet liquid measure also reduces thereupon, repeats said process, reaches a kind of gas-liquid at last and passes in and out plateau; Tathagata airshed is big, differential pressure increases, liquid level begins to descend in jar, when dropping to the height that is lower than gas-liquid header 15 outlet and the required differential pressure of discharge opeing, draining flow diminishes thereupon, the liquid level of separating controlling jar 2 begins again to rise gradually simultaneously, repeats above-mentioned liquid level ascending and descending process, reaches separating controlling jar 2 interior liquid levels and changes within a certain height.After this, if the gas liquid ratio of the gas and liquid mixture that pipeline comes and efflux line pressure variations, cause the rising or the decline of liquid level in the separating controlling jar 2, flow regulation valve 5 all can be controlled at pressure reduction on the required numerical value of discharge opeing automatically, liquid level is controlled in the scope of setting.For low discharge,, form gap discharge opeing metering (atmospheric pressure apocenosis) by the height and the required differential pressure of liquid road flow resistance of gas-liquid header 15 outlets; For little tolerance is gap exhaust metering too.
Temperature transmitter 18, pressure unit 17 are installed in separating controlling jar 2 bottoms, gas vent valve 12, gas meter 13, gas-liquid surge tank 14, liquid flowmeter 10 and profit gas component instrument 11 are installed respectively behind the gas outlet tube 6, and with the supporting use of computer system, form the on-line metering device of the complete gas-liquid delivery fluid of a cover.It is to influence the gasometer accuracy of measurement for the pressure surge of avoiding gas liquid outlet pipe 23 causes the anti-gas meter that is poured into of liquid that gas-liquid surge tank 14 purposes wherein are installed, and profit gas component instrument 11 is used for water percentage, the void fraction of on-line monitoring liquid road fluid.
Claims (10)
1. an automatic metering device for oil well three-phase flow is with separating controlling jar (2) by flange and pipeline, liquid flowmeter (10), profit gas component instrument (11), gas meter (13), gas-liquid surge tank (14) connects to form profit gas phase-splitting metering pipe network, it is characterized in that separating controlling jar (2) top and gas outlet tube (6), gas-liquid induction pipe (1) links to each other, its underpart is communicated with liquid outlet tube (8), gas-liquid induction pipe (1) is provided with gas-liquid cyclone centrifugal separator (4) with separating controlling jar (2) connecting place, flow regulation valve (5) is housed in the separating controlling jar (2), gas vent valve (12) and gas meter (13) are housed on the pipeline of gas outlet tube (6), between gas meter (13) endpiece and the gas-liquid header (15) gas-liquid surge tank (14) are housed; Liquid outlet valve (9), liquid flowmeter (10) and profit gas component instrument (11) are housed on the pipeline of liquid outlet tube (8); Gas-liquid header (15) locates to have gas liquid outlet pipe (16), and pressure unit (17) and temperature transmitter (18) all are located on the separating controlling jar (2).
2. a kind of automatic metering device for oil well three-phase flow according to claim 1, it is characterized in that gas-liquid cyclone centrifugal separator (4) is the cylindrical sleeve tubular-shaped structures, vertically place the middle and upper part in the separating controlling jar (2), and center symmetry, its centrifugal separator inlet (41) one ends link to each other with gas-liquid induction pipe (1), and the other end is connected with spiral centrifuge tube (42) tangent line; Spiral centrifuge tube (42) is square or rectangle, and spiral places guiding to separate in the sleeve pipe (43) from top to bottom, and spiral is at least two circles, and the circulation area of spiral centrifuge tube (42) is less than or equal to the circulation area of gas-liquid induction pipe (1); Guiding is separated sleeve pipe (43) and is the hollow sleeve tubulose, and is concentric with separating controlling jar (2), and mesh (44) is arranged on the hypomere box face.
3, a kind of automatic metering device for oil well three-phase flow according to claim 1, the valve seat connecting pipe (50) that it is characterized in that flow regulation valve (5) is connected with valve seat (51), gas outlet tube (6) smooth transition, valve seat connecting pipe (50) is communicated with gas outlet tube (6), and be fixed on the bottom at separating controlling tank top end cap (3) center, there is a valve opening (511) at valve seat (51) center, and valve opening (511) diameter is less than gas outlet tube (6) caliber; The bottom surface of spool (52) is connected with valve body (53) smooth transition; One end of floating ball rod (54) is connected with valve body (53) center symmetry smooth transition, and other end center symmetry penetrates ball float (55), and smooth transition connects; Spool (52) is a cone; Valve body (53) is smooth sphere shape or truncated cone-shaped, and its maximum outside diameter is greater than valve opening (511) aperture; Ball float (55) is hollow ball or hollow cylinder, places on the ball float guides (7) in the separating controlling jar (2), and floating ball rod (54) is the pipe of diameter less than valve body (53) diameter.
4, a kind of automatic metering device for oil well three-phase flow according to claim 3 is characterized in that guide rod (71) one ends of ball float guides (7) are vertically fixed on the center of chassis (72), and the other end straight up; Chassis (72) horizontal fixed is middle and lower part and concentricity with gas-liquid separation controlling tank (2) in separating controlling jar (2), has into the liquid flow hole (73) of net form on chassis (72).
5. according to claim 2 or 3 described a kind of automatic metering device for oil well three-phase flow, it is characterized in that the external diameter of the internal diameter of guiding separation sleeve pipe (43) greater than ball float (55), guiding is separated sleeve pipe (43) external diameter and is less than or equal to separating controlling jar (2) internal diameter.
6. a kind of automatic metering device for oil well three-phase flow according to claim 3 is characterized in that the valve body (53) and the surface of contact of valve opening (511) are smooth sphere shape or truncated cone-shaped.
7. a kind of automatic metering device for oil well three-phase flow according to claim 3 is characterized in that spool (52) tapering size and cone length depend on measurement gas-liquid range ability size, and its maximum sole diameter is less than valve opening (511) aperture.
8. according to claim 3 or 4 described a kind of automatic metering device for oil well three-phase flow, it is characterized in that the diameter of guide rod (71) is less than the internal diameter of floating ball rod (54), the length length greater than spool (52); Total circulation area of liquid flow hole (73) perforate is greater than the circulation area of gas-liquid induction pipe (1).
9. according to claim 1 or 3 described a kind of automatic metering device for oil well three-phase flow, liquid level when the Horizontal Exit height that it is characterized in that gas-liquid header (15) is higher than ball float (55) floating that places in the separating controlling jar (2) is lower than valve body (53) and pushes up the liquid level of valve seat (51) in separating controlling jar (2).
10. a kind of automatic metering device for oil well three-phase flow according to claim 1 is characterized in that the volume of gas-liquid surge tank (14) arrives the volume in the pipeline between gas-liquid surge tank (14) upper end greater than gas outlet tube (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620079589 CN200979427Y (en) | 2006-08-08 | 2006-08-08 | An automatic measurement device for the oil well three-phase flow |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620079589 CN200979427Y (en) | 2006-08-08 | 2006-08-08 | An automatic measurement device for the oil well three-phase flow |
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| Publication Number | Publication Date |
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| CN200979427Y true CN200979427Y (en) | 2007-11-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 200620079589 Expired - Fee Related CN200979427Y (en) | 2006-08-08 | 2006-08-08 | An automatic measurement device for the oil well three-phase flow |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102661142A (en) * | 2012-05-08 | 2012-09-12 | 陈爱民 | Method and device for measuring productivity of oil well |
| CN105999868A (en) * | 2016-05-10 | 2016-10-12 | 中国石油大学(北京) | Gas-liquid separator for testing open flow of oil and gas well |
| CN106595787A (en) * | 2017-01-10 | 2017-04-26 | 西南石油大学 | A Method for Calculating Gas Phase Flow Rate Using Gas Holdup in Low Production Gas Wells |
| CN107557087A (en) * | 2017-09-05 | 2018-01-09 | 中石化广州工程有限公司 | A kind of spiral-flow type gas-liquid separation device and method |
| CN109723429A (en) * | 2019-02-23 | 2019-05-07 | 江苏华尔威科技集团有限公司 | A kind of crude oil single well gas-liquid biphase flowmeter amount device |
| CN109990857A (en) * | 2019-01-22 | 2019-07-09 | 无锡洋湃科技有限公司 | Self-excitation type flux of moisture measuring device |
| CN113218478A (en) * | 2021-04-14 | 2021-08-06 | 新疆中元天能油气科技股份有限公司 | Online self-calibration oil-gas-water three-phase metering device and metering method |
-
2006
- 2006-08-08 CN CN 200620079589 patent/CN200979427Y/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102661142A (en) * | 2012-05-08 | 2012-09-12 | 陈爱民 | Method and device for measuring productivity of oil well |
| CN105999868A (en) * | 2016-05-10 | 2016-10-12 | 中国石油大学(北京) | Gas-liquid separator for testing open flow of oil and gas well |
| CN105999868B (en) * | 2016-05-10 | 2024-04-19 | 中国石油大学(北京) | Gas-liquid separator for open flow in oil-gas well test |
| CN106595787A (en) * | 2017-01-10 | 2017-04-26 | 西南石油大学 | A Method for Calculating Gas Phase Flow Rate Using Gas Holdup in Low Production Gas Wells |
| CN106595787B (en) * | 2017-01-10 | 2019-04-16 | 西南石油大学 | A kind of method that gas stringer calculates gas phase flow rate using gas holdup |
| CN107557087A (en) * | 2017-09-05 | 2018-01-09 | 中石化广州工程有限公司 | A kind of spiral-flow type gas-liquid separation device and method |
| CN107557087B (en) * | 2017-09-05 | 2020-06-23 | 中石化广州工程有限公司 | Spiral-flow type gas-liquid separation device and method |
| CN109990857A (en) * | 2019-01-22 | 2019-07-09 | 无锡洋湃科技有限公司 | Self-excitation type flux of moisture measuring device |
| CN109723429A (en) * | 2019-02-23 | 2019-05-07 | 江苏华尔威科技集团有限公司 | A kind of crude oil single well gas-liquid biphase flowmeter amount device |
| CN113218478A (en) * | 2021-04-14 | 2021-08-06 | 新疆中元天能油气科技股份有限公司 | Online self-calibration oil-gas-water three-phase metering device and metering method |
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