CN101053723A - Self controlled high efficient gas and liquid separator - Google Patents
Self controlled high efficient gas and liquid separator Download PDFInfo
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- CN101053723A CN101053723A CN 200610069670 CN200610069670A CN101053723A CN 101053723 A CN101053723 A CN 101053723A CN 200610069670 CN200610069670 CN 200610069670 CN 200610069670 A CN200610069670 A CN 200610069670A CN 101053723 A CN101053723 A CN 101053723A
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Abstract
The invention relates to a self-control gas-liquid separator, especially to a control and separation integral self-control high efficiency gas-liquid separator. The embodiment is to connect to the gas valve (7) of said gas conditioning unit through the lower end of the spring (1) in which a bracket (2) is mounted. The bracket (2) vertically hangs a liquid level transmitting control unit, and basipetally impenetrates the said gas conditioning unit and gas-liquid separating unit in turn. The beneficial effect is that: control-separate one-piece design of the self-control gas-liquid separator, whose control unit uses self-operated control principle and whose separating unit gives priority to hydrocyclone Separation process and assists with gravity separation, the efficiency for gas-liquid separating is high, and the effect of separation is excellent; the reasonable structure makes it easily to manufacturing activity and have a low manufacturing and using cost without maintenance and have a long longevity; compared with conventional gravity separator matching to the self-control system, the gas-liquid separating technological process is largely simplified and the cost can save larger than 70 percent at the same time.
Description
One, technical field:
The present invention relates to a kind of auto-controlled gas-liquid separator, particularly relate to the separation integrated self controlled high efficient gas and liquid separator of a kind of control.
Two, background technology:
The separation of gas, liquid mixture in the heterogeneous metering of separate type, oil-gas gathering and transportation treatment process process, usually adopt gas-liquid separator, gas-liquid separator at present commonly used mainly contains vertical separator, horizontal separator, tubular vortex separator etc., and which kind of separator all needs supporting control corresponding system could realize the normal separation of gas-liquid.Vertical separator and horizontal separator need enough big separator volume and stable separator liquid level, could guarantee gas-liquid separation effect preferably, and its supporting control method mainly contains floating ball rod control valve, the moving instrument for automatic control of gas () etc.The type separator exists mainly that volume is big, technology shortcomings such as complexity, cost height; The tubulose cyclone separator is to utilize centrifugal principle to realize separating of gas and liquid, the type separator volume is less, but control system is had relatively high expectations, need supporting automatic control system accurately and reliably, therefore exist control complex process, cost height, use and maintenance technology to require high shortcoming.
Three, summary of the invention:
Purpose of the present invention is exactly the above-mentioned defective that exists at prior art, and a kind of Passive Shape Control and self controlled high efficient gas and liquid separator that can effectively reduce the manufacturing use cost that separates one of adopting is provided.
Technical scheme is: the air valve body (7) that connects described gas regulation unit by spring shield (1) lower end, be provided with support (2) in the spring shield (1), support (2) vertical hanging liquid level becomes send control module, and runs through described gas regulation unit and gas-liquid separation unit successively from top to bottom;
Constitute gas-liquid separation unit by rotational flow separation unit (13), communicating pipe (14), auxiliary separation unit (15,16), Gravity Separation body (18);
Set upright the gas regulation unit that part (12) constitutes by air valve body (7), air valve seat (8), air valve keeper (9), air valve core bar (10), air valve seat sealing ring (11), air valve;
Constitute the liquid level change by adjusting lever (3), flexible member and connector (5), support (2), connecting rod (17), float (19) and send control module.
Another kind of preferable technical scheme is: in such scheme, the lower end of gas-liquid separation unit can also connect the liquid regulon, and described liquid regulon is set upright part (23), liquid valve keeper (24,28) formation by liquid valve body (22), liquid outlet tube (22.3), liquid valve seat (26), liquid valve core rod (27), liquid valve seat insert (25), liquid valve.
Wherein: the air valve body (7) that connects described gas regulation unit by spring shield (1) lower end, be provided with support (2) in the spring shield (1), support (2) vertical hanging liquid level becomes send control module, and runs through described gas regulation unit, gas-liquid separation unit, liquid regulon from top to bottom successively.It is to be gone up and connection successively in support (2) by adjusting lever (3) upper end vertical hanging that control module is sent in preferably described liquid level change: the adjusting lever locking device, be arranged on the air valve core bar (10) in the air valve body (7), be arranged on connecting rod (17), float (19), connector (21) in the Gravity Separation body (18), be arranged on the interior liquid valve core rod of liquid valve body (22) (27), constitute the liquid level change and send control module.
More preferably described adjusting lever locking device comprises: locking nut and packing ring (4) and flexible member and connector (5); Described flexible member is a spring.
Described connecting rod (17) can be the hard connecting rod, can also be soft connection cord.
Described gas-liquid separation unit comprises as follows: rotational flow separation unit (13) are are tangentially connected and composed with rotational flow separation body (13.1) by inclination angle downward gas-liquid inlet tube and nozzle (13.2), auxiliary separation unit (15,16) is fixed in the Gravity Separation body (18), and rotational flow separation unit (13) are connected by flange with Gravity Separation body (18).
Described gas regulation unit comprises as follows: air valve body (7) is made of outer valve (7.1), inner valve body (7.2), outlet (7.3), inner valve body (7.2) bottom has the gas communication hole, air valve seat (8), air valve keeper (9) are packed into successively from top, air valve seat (8) is by air valve seat sealing ring (11) and inner valve body (7.2) sealing, and air valve seat (8), air valve are in one heart after setting upright part (12) assembling.
Described liquid regulon comprises as follows: liquid valve body (22) is by liquid valve outer valve (22.1), inner valve body (22.2), liquid outlet tube (22.3) constitutes, there is internal thread to be used to install the liquid valve on the inner valve body (22.2) and sets upright part (23), the liquid valve is set upright and is processed with center righting hole and liquid communication hole on the part (23), liquid valve seat (26), liquid valve keeper (24,28) the liquid valve is set upright part (23) has and goes up and pack into successively down, setting upright part (23) by the liquid valve compresses, liquid valve seat (26) is by liquid valve seat insert (25) and inner valve body (22.2) sealing, liquid valve seat (26), the liquid valve will be in one heart after setting upright part (23) assembling.
Separator is in working order the time, gas-liquid mixed phase medium is after gas-liquid inlet tube (13.2) enters rotational flow separation body (13.1), form a vortex face by centrifugal force, gravity and buoyancy, the liquid phase that density is big flows to the bottom along rotational flow separation body tube wall, the gas phase that density is little rises to rotational flow separation body top and flows out through the gas control module, the liquid phase that flows to rotational flow separation body bottom flows to Gravity Separation body (18) through auxiliary separation unit (15,16), gas phase is further separated with liquid phase under the gravity effect, and last liquid phase flows out through the liquid phase control module.The liquid level of gas-liquid separation unit and pressure become the self-operated control system control of sending control module, liquid regulon to form by gas regulation unit, liquid level, guarantee the steady operation of gas-liquid separation unit, realize that gas-liquid two-phase efficiently separates.
Control system is in working order the time, the part of float (19) is by liquid-immersed, float (19) is moved up by buoyancy function, drive air valve core bar (10), liquid valve core rod (27) move up synchronously, air valve opening reduces, the liquid valve opening increases, and produces new balance until gas flow, fluid flow and liquid level; When liquid level changes downwards, in like manner.Liquid level variable quantity and gas, liquid valve position move into proportional relationship, and proportionality coefficient is by spring rate and the decision of float sectional area.Δ H=K* Δ X Δ H-liquid level variable quantity
Δ X-control module displacement (gas, liquid valve core rod displacement)
K-proportionality coefficient (determining) by spring rate and float sectional area
The invention has the beneficial effects as follows:
(1) be that self controlled high efficient gas and liquid separator is controlled separation integrated design, control section adopts the self-operated type control principle, and it is that main Gravity Separation is the technology of assisting that separating part adopts rotational flow separation, gas-liquid separation efficient height, good separating effect.
(2) be rational in infrastructure, be easy to processing, manufacturing and use cost are low, non-maintaining, and the life-span is long.
(3) be to compare with the supporting automatic control system of traditional gravity separator, can simplify gas-liquid separating technological process significantly, cost can be saved more than 70% simultaneously.
(4) be to become the heterogeneous metering device of separate type with gas phase, liquid phase, moisture single-phase bank of meter, solve the heterogeneous measurement problem of produced liquid in oil well in the oil field development preferably, and technology be simple, production cost is low.
Four, description of drawings:
Accompanying drawing 1 is the cutaway view of a kind of embodiment of the present invention;
Accompanying drawing 2 is cutaway views of another kind of embodiment of the present invention;
Accompanying drawing 3 is A-A cutaway views of two kinds of embodiment of the present invention.
Among the figure: set upright part 12, rotational flow separation unit 13, rotational flow separation body 13.1, gas-liquid inlet tube and nozzle 13.2, communicating pipe 14, auxiliary separation unit 15,16, gas equalizing line 15.1, liquid level spacing ring 15.2, disk 15.3, connecting rod 17, Gravity Separation body 18, float 19 by spring shield 1, support 2, adjusting lever 3, locking nut and packing ring 4, flexible member and connector 5, gas valve core fixture 6, air valve body 7, outer valve 7.1, inner valve body 7.2, outlet 7.3, air valve seat 8, air valve keeper 9, air valve core bar 10, air valve seat sealing ring 11, air valve; Pipe nipple 20, connector 21, liquid valve body 22, liquid valve outer valve 22.1, inner valve body 22.2, liquid outlet tube 22.3, liquid valve are set upright part 23, liquid valve seat insert 25, liquid valve seat 26, liquid valve core rod 27, liquid valve keeper 24,28.
Five, the specific embodiment:
Embodiment 1: in conjunction with the accompanying drawings 1 and 3, and the present invention is described in further detail (gas-liquid mixed phase medium through the scheme of above-mentioned self controlled high efficient gas and liquid separator can effectively with gas phase separation):
Its technical scheme is: by spring shield 1, support 2, adjusting lever 3, locking nut and packing ring 4, flexible member and connector 5, gas valve core fixture 6, air valve body 7, outer valve 7.1, inner valve body 7.2, outlet 7.3, air valve seat 8, air valve keeper 9, air valve core bar 10, air valve seat sealing ring 11, air valve is set upright part 12, rotational flow separation unit 13, rotational flow separation body 13.1, gas-liquid inlet tube and nozzle 13.2, communicating pipe 14, auxiliary separation unit 15,16, gas equalizing line 15.1, liquid level spacing ring 15.2, disk 15.3, connecting rod 17, Gravity Separation body 18, float 19.
Rotational flow separation unit 13 is is tangentially connected and composed with rotational flow separation body 13.1 by inclination angle downward gas-liquid inlet tube and nozzle 13.2, auxiliary separation unit 15,16 is fixed in the Gravity Separation body 18, and rotational flow separation unit 13 and Gravity Separation body 18 are connected by flange.
Embodiment 2: in conjunction with the accompanying drawings 2 and 3, another kind of embodiment of the present invention is described in further detail (gas-liquid mixed phase medium through the scheme of above-mentioned self controlled high efficient gas and liquid separator can effectively with gas phase and liquid phase separation):
Its technical scheme is: above-mentioned other structures are constant, the lower end of gas-liquid separation unit can also connect the liquid regulon, and described liquid regulon is set upright part 23, liquid valve seat insert 25, liquid valve seat 26, liquid valve core rod 27,24,28 of liquid valve keepers by the pipe nipple 20 that is used to adjust the position, connector 21, liquid valve body 22, liquid valve outer valve 22.1, inner valve body 22.2, liquid outlet tube 22.3, liquid valve and constituted.
Its operation principle is: separator is in working order the time, gas-liquid mixed phase medium is after gas-liquid inlet tube 13.2 enters rotational flow separation body 13.1, by centrifugal force, gravity and buoyancy form a vortex face, the big liquid phase of density is along the rotational flow separation body, tube wall flows to the bottom, the gas phase that density is little rises to rotational flow separation body top and flows out through the gas control module, the liquid phase that flows to rotational flow separation body bottom flows to Gravity Separation body 18 through auxiliary separation unit 15, specifically be that liquid phase is through liquid level spacing ring 15.2, disk 15.3, because liquid velocity reduces, gas phase is further separated with liquid phase under the gravity effect, gas separated is through gas equalizing line 15.1 once more, communicating pipe 14, flow to rotational flow separation body top 13.1, and the liquid phase of separating once more flows out through the liquid phase control module.The liquid level of gas-liquid separation unit and pressure become the self-operated control system control of sending control module, liquid regulon to form by gas regulation unit, liquid level, guarantee the steady operation of gas-liquid separation unit, realize that gas-liquid two-phase efficiently separates.
Control system is in working order the time, the part of float 19 is by liquid-immersed, float 19 is moved up by buoyancy function, drive air valve core bar 10, liquid valve core rod 27 move up synchronously, air valve opening reduces, the liquid valve opening increases, and produces new balance until gas flow, fluid flow and liquid level; When liquid level changes downwards, in like manner.
Claims (9)
1, a kind of self controlled high efficient gas and liquid separator, it is characterized in that: the air valve body (7) that connects described gas regulation unit by spring shield (1) lower end, be provided with support (2) in the spring shield (1), support (2) vertical hanging liquid level becomes send control module, and runs through described gas regulation unit and gas-liquid separation unit successively from top to bottom;
Described gas-liquid separation unit is made of rotational flow separation unit (13), gas-liquid inlet tube and nozzle (13.2), communicating pipe (14), auxiliary separation unit (15,16), Gravity Separation body (18);
Described gas regulation unit is set upright part (12) by air valve body (7), outlet (7.3), air valve seat (8), air valve keeper (9), air valve core bar (10), air valve seat sealing ring (11), air valve and is constituted;
Described liquid level becomes send control module to be made of adjusting lever (3), flexible member (5), support (2), connecting rod (17), float (19).
2, self controlled high efficient gas and liquid separator according to claim 1, it is characterized in that: the lower end of described gas-liquid separation unit can also connect the liquid regulon, and described liquid regulon is set upright part (23), liquid valve keeper (24,28) formation by liquid valve body (22), liquid outlet tube (22.3), liquid valve seat (26), liquid valve core rod (27), liquid valve seat insert (25), liquid valve.
3, self controlled high efficient gas and liquid separator according to claim 1, it is characterized in that: it is to be gone up and connection successively in support (2) by adjusting lever (3) upper end vertical hanging that control module is sent in described liquid level change: the adjusting lever locking device, be arranged on the air valve core bar (10) in the air valve body (7), be arranged on connecting rod (17), float (19), connector (21) in the Gravity Separation body (18), be arranged on the interior liquid valve core rod of liquid valve body (22) (27), constitute the liquid level change and send control module.
4, self controlled high efficient gas and liquid separator according to claim 3 is characterized in that: described adjusting lever locking device comprises: locking nut and packing ring (4) and flexible member and connector (5).
5, self controlled high efficient gas and liquid separator according to claim 4 is characterized in that: described flexible member is a spring.
6, according to claim 3,4 or 5 described self controlled high efficient gas and liquid separators, it is characterized in that: described connecting rod (17) can be the hard connecting rod, can also be soft connection cord.
7, self controlled high efficient gas and liquid separator according to claim 1, it is characterized in that: described gas-liquid separation unit comprises as follows: rotational flow separation unit (13) are are tangentially connected and composed with rotational flow separation body (13.1) by inclination angle downward gas-liquid inlet tube and nozzle (13.2), auxiliary separation unit (15,16) is fixed in the Gravity Separation body (18), and rotational flow separation unit (13) are connected by flange with Gravity Separation body (18).
8, self controlled high efficient gas and liquid separator according to claim 1, it is characterized in that: described gas regulation unit comprises as follows: air valve body (7) is by outer valve (7.1), inner valve body (7.2), outlet (7.3) constitutes, inner valve body (7.2) bottom has the gas communication hole, air valve seat (8), air valve keeper (9) is packed into successively from top, air valve seat (8) is by air valve seat sealing ring (11) and inner valve body (7.2) sealing, air valve seat (8), air valve is in one heart after setting upright part (12) assembling, and air valve inner valve body (7.2) lower end has internal thread to be used to install air valve to set upright part (12).
9, self controlled high efficient gas and liquid separator according to claim 1, it is characterized in that: described liquid regulon comprises as follows: liquid valve body (22) is by liquid valve outer valve (22.1), inner valve body (22.2), liquid outlet tube (22.3) constitutes, there is internal thread to be used to install the liquid valve on the inner valve body (22.2) and sets upright part (23), the liquid valve is set upright and is processed with center righting hole and liquid communication hole on the part (23), liquid valve seat (26), liquid valve keeper (24,28) the liquid valve is set upright part (23) has and goes up and pack into successively down, setting upright part (23) by the liquid valve compresses, liquid valve seat (26) is by liquid valve seat insert (25) and inner valve body (22.3) sealing, liquid valve seat (26), the liquid valve will be in one heart after setting upright part (23) assembling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100696704A CN100453144C (en) | 2006-08-07 | 2006-08-07 | Self controlled high efficient gas and liquid separator |
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2006100696704A CN100453144C (en) | 2006-08-07 | 2006-08-07 | Self controlled high efficient gas and liquid separator |
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| CN101053723A true CN101053723A (en) | 2007-10-17 |
| CN100453144C CN100453144C (en) | 2009-01-21 |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101865360A (en) * | 2010-07-16 | 2010-10-20 | 中国石油集团工程设计有限责任公司 | New type high-efficient whirl slug flow catcher |
| CN103285669A (en) * | 2013-05-09 | 2013-09-11 | 浙江大学 | Automatic gas-liquid separation and backflow integrated device and oil discharge stripping device |
| CN103306989B (en) * | 2013-05-09 | 2016-06-29 | 浙江大学 | A kind of stripping pump unit |
| CN107152269A (en) * | 2017-07-03 | 2017-09-12 | 新疆熙泰石油装备有限公司 | Independent external liquid level regulation device and the gs-oil separator of external liquid level regulation |
| CN107596797A (en) * | 2017-09-05 | 2018-01-19 | 中石化广州工程有限公司 | A kind of gas-liquid separator and gas-liquid separating method |
| CN108480068A (en) * | 2018-01-23 | 2018-09-04 | 博迈科海洋工程股份有限公司 | A kind of Pipe String Cyclone Gas-liquid Separator of adjustable float automatic liquid level control |
| CN110685341A (en) * | 2018-07-06 | 2020-01-14 | 深圳市迈斯艾尔科技发展有限公司 | Automatic drainage device for vacuum |
| CN110732188A (en) * | 2019-10-21 | 2020-01-31 | 西安交通大学 | In-pipe phase-separated split-flow high-flow gas-liquid separation device and method |
| CN113694567A (en) * | 2021-09-15 | 2021-11-26 | 中国石油大学(华东) | Two-stage gas-liquid mixing conical helical field separation device and online control system |
| CN115889004A (en) * | 2022-12-21 | 2023-04-04 | 杭州飞科电气有限公司 | Columnar cyclone separator structure |
| CN118327537A (en) * | 2024-05-06 | 2024-07-12 | 中国石油大学(北京) | Gas-liquid separation device and oil production device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JPS61146311A (en) * | 1984-12-19 | 1986-07-04 | Nitto Seiko Co Ltd | Gas separation apparatus |
| US4730634A (en) * | 1986-06-19 | 1988-03-15 | Amoco Corporation | Method and apparatus for controlling production of fluids from a well |
| CN1231279C (en) * | 2003-05-01 | 2005-12-14 | 胜利油田胜利工程设计咨询有限责任公司 | Oil gas separator with self controlled pressure and liquid level |
| CN2755400Y (en) * | 2004-11-23 | 2006-02-01 | 中国石化中原油气高新股份有限公司采油四厂 | Gas pipeline liquid preventor of oil-gas separator |
| CN100342942C (en) * | 2005-12-07 | 2007-10-17 | 房师礼 | Self-force type separation controller for gas and liquid |
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- 2006-08-07 CN CNB2006100696704A patent/CN100453144C/en not_active Expired - Fee Related
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| CN101865360B (en) * | 2010-07-16 | 2012-11-14 | 中国石油集团工程设计有限责任公司 | New type high-efficient whirl slug flow catcher |
| CN101865360A (en) * | 2010-07-16 | 2010-10-20 | 中国石油集团工程设计有限责任公司 | New type high-efficient whirl slug flow catcher |
| CN103285669A (en) * | 2013-05-09 | 2013-09-11 | 浙江大学 | Automatic gas-liquid separation and backflow integrated device and oil discharge stripping device |
| CN103306989B (en) * | 2013-05-09 | 2016-06-29 | 浙江大学 | A kind of stripping pump unit |
| CN107152269A (en) * | 2017-07-03 | 2017-09-12 | 新疆熙泰石油装备有限公司 | Independent external liquid level regulation device and the gs-oil separator of external liquid level regulation |
| CN107152269B (en) * | 2017-07-03 | 2023-03-21 | 新疆熙泰石油装备有限公司 | Independent external liquid level adjusting device and external liquid level adjusting oil-gas separator |
| CN107596797A (en) * | 2017-09-05 | 2018-01-19 | 中石化广州工程有限公司 | A kind of gas-liquid separator and gas-liquid separating method |
| CN107596797B (en) * | 2017-09-05 | 2020-05-19 | 中石化广州工程有限公司 | Gas-liquid separator and gas-liquid separation method |
| CN108480068A (en) * | 2018-01-23 | 2018-09-04 | 博迈科海洋工程股份有限公司 | A kind of Pipe String Cyclone Gas-liquid Separator of adjustable float automatic liquid level control |
| CN110685341B (en) * | 2018-07-06 | 2020-11-20 | 深圳市迈斯艾尔科技发展有限公司 | Automatic drainage device for vacuum |
| CN110685341A (en) * | 2018-07-06 | 2020-01-14 | 深圳市迈斯艾尔科技发展有限公司 | Automatic drainage device for vacuum |
| CN110732188A (en) * | 2019-10-21 | 2020-01-31 | 西安交通大学 | In-pipe phase-separated split-flow high-flow gas-liquid separation device and method |
| CN110732188B (en) * | 2019-10-21 | 2020-11-17 | 西安交通大学 | In-pipe phase separation and split-flow type high-flow-rate gas-liquid separation device and method |
| CN113694567A (en) * | 2021-09-15 | 2021-11-26 | 中国石油大学(华东) | Two-stage gas-liquid mixing conical helical field separation device and online control system |
| CN115889004A (en) * | 2022-12-21 | 2023-04-04 | 杭州飞科电气有限公司 | Columnar cyclone separator structure |
| CN118327537A (en) * | 2024-05-06 | 2024-07-12 | 中国石油大学(北京) | Gas-liquid separation device and oil production device |
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Granted publication date: 20090121 Termination date: 20090907 |