CN201055814Y - Cyclone gas-liquid separator with automatic oil-gas discharge function - Google Patents
Cyclone gas-liquid separator with automatic oil-gas discharge function Download PDFInfo
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技术领域 technical field
本实用新型涉及一种油田采油集输技术领域,特别涉及一种原油油气分离设备,是一种带有气、液自动排放装置的分离器。The utility model relates to the technical field of oil production gathering and transportation in an oil field, in particular to crude oil and gas separation equipment, which is a separator with an automatic gas and liquid discharge device.
背景技术 Background technique
目前,油田采油集输过程中,大量使用油气分离设备,将原油与天然气分离。虽然现有的油气旋流器油气分离效果好,但分离器本身并不能实现对排气、排液过程的自动控制。中国专利公告号为CN1295024C,提供了一种高效自调整旋流气液分离器。自动控制一般都需要辅助系统如自动化仪表装置来实现,技术复杂,成本高,维修麻烦。有不需要配备自动仪表的液面自控分离器。中国专利公告号为CN1242826C的液面自控一体化气液分离器,采用非密闭浮筒设计,利用浮力向上或向下运动与浮筒连在一起的排液阀杆,以控制排液速度,达到自动排液目的。这种分离器所采用的浮筒较大,占据了分离器的大部分空间,比较适用于较大液滴的分离。当气液分离要求较高,需改进内部分离配件时,不容易实现;浮筒内污物较多时还会降低浮筒的浮力,影响自动排液效果;没有对气体的排出进行自动控制,当分离器内液面太高时易产生气体带出液体现象;采用空心球体实现自动排液,球体加工困难且不能进行体积调节。At present, oil and gas separation equipment is widely used to separate crude oil from natural gas during oil production, gathering and transportation. Although the existing oil-gas cyclone has good oil-gas separation effect, the separator itself cannot realize the automatic control of the exhaust and liquid discharge process. The Chinese patent notification number is CN1295024C, which provides a high-efficiency self-adjusting cyclone gas-liquid separator. Automatic control generally needs auxiliary systems such as automatic instrumentation devices to realize, the technology is complicated, the cost is high, and maintenance is troublesome. There are liquid level automatic control separators that do not need to be equipped with automatic instruments. The Chinese patent announcement number is CN1242826C. The liquid level automatic control integrated gas-liquid separator adopts the non-airtight buoy design, and uses the buoyancy to move up or down the liquid discharge valve stem connected with the buoy to control the liquid discharge speed and achieve automatic discharge. liquid purpose. The buoy used in this separator is relatively large, occupying most of the space of the separator, and is more suitable for the separation of larger droplets. When the requirements for gas-liquid separation are high and internal separation accessories need to be improved, it is not easy to achieve; when there is a lot of dirt in the buoy, the buoyancy of the buoy will be reduced, affecting the effect of automatic liquid discharge; there is no automatic control of gas discharge, when the separator When the inner liquid level is too high, it is easy to cause the gas to carry out the liquid; the hollow sphere is used to realize automatic liquid drainage, and the sphere is difficult to process and cannot be adjusted in volume.
现有旋流气液分离器中的自动排放装置,基本是利用信号转换及自动化仪表系统或人工控制分离器的方法排出流体。现有气液分离和液面控制一体化设计中,分离器内部采用与分离器体积基本相同的浮筒,仅靠气液比重差进行分离,不能有效分离体积较小的液滴。现有技术仅对分离器内气相进入液相时进行控制,没有对液位高时液体进入气相进行控制。The automatic discharge device in the existing cyclone gas-liquid separator basically discharges the fluid by utilizing signal conversion and automatic instrument system or manually controlling the separator. In the existing integrated design of gas-liquid separation and liquid level control, the inside of the separator uses a buoy that is basically the same volume as the separator, and the separation is performed only by the difference in gas-liquid specific gravity, which cannot effectively separate small droplets. The prior art only controls when the gas phase in the separator enters the liquid phase, but does not control the liquid entering the gas phase when the liquid level is high.
实用新型内容Utility model content
本实用新型的目的是:提供一种油气自动排放旋流气液分离器,针对上述现有技术的不足,设计一种结构简单,可拆卸可组装的自动排放装置和内部带有旋流器的分离器。这种分离器无需自动化仪表控制气液自动排放,以适应原油气液分离效果要求高;气相、液相不得互相携带,尤其是液相不能从气相出口溢出的现场要求,并且具有制造工艺简单,成本低,易于安装维护的特点。The purpose of this utility model is to provide a cyclone gas-liquid separator with automatic discharge of oil and gas, aiming at the deficiencies of the prior art above, to design a detachable and assembled automatic discharge device and a separator with a cyclone inside. device. This kind of separator does not need automatic instruments to control the automatic discharge of gas and liquid, so as to meet the high requirements of crude oil gas-liquid separation effect; the gas phase and liquid phase must not carry each other, especially the field requirements that the liquid phase cannot overflow from the gas phase outlet, and has simple manufacturing process, Low cost, easy to install and maintain.
本实用新型采用的技术方案是:油气自动排放旋流气液分离器,包括罐体,罐体底部有排污口,罐体中部有进口。罐体内有旋流器和气相引入口。其特征是:在罐体顶部固定有气相自动排放装置,气相自动排放装置连接气相排放管线,气相排放管线连接有气相出口定压控流阀。罐体下部连接有液相排放管线,液相排放管线连接液相自动排放装置,液相自动排放装置连接有液相出口定压控流阀。The technical scheme adopted by the utility model is: the cyclone gas-liquid separator for automatic discharge of oil and gas, including a tank body with a sewage outlet at the bottom of the tank body and an inlet in the middle of the tank body. There is a cyclone and a gas phase inlet in the tank. It is characterized in that: a gas phase automatic discharge device is fixed on the top of the tank body, the gas phase automatic discharge device is connected with a gas phase discharge pipeline, and the gas phase discharge pipeline is connected with a gas phase outlet constant pressure flow control valve. The lower part of the tank body is connected with a liquid phase discharge pipeline, and the liquid phase discharge pipeline is connected with a liquid phase automatic discharge device, and the liquid phase automatic discharge device is connected with a liquid phase outlet constant pressure flow control valve.
为了检修时方便排液,在液相排放管线与液相出口定压控流阀的管线上连接有辅助排液管,辅助排液管上有阀门。In order to facilitate liquid discharge during maintenance, an auxiliary liquid discharge pipe is connected between the liquid phase discharge pipeline and the liquid phase outlet constant pressure flow control valve, and there is a valve on the auxiliary liquid discharge pipe.
所述的定压控流阀的结构是:包括锥法兰、锥封头、弹簧、阀体、喷嘴、喷嘴座和法兰,锥法兰的中心孔为锥形孔,中心孔内有锥封头,锥法兰锥形孔与锥封头的锥度相同。在锥法兰和法兰之间有圆柱筒形的阀体。阀体内有压缩弹簧。法兰的中心孔内螺纹连接有喷嘴座。喷嘴座内有喷嘴,喷嘴座与喷嘴螺纹连接。喷嘴中心孔为锥形。弹簧控制压力,喷嘴控制流量。定压控流阀用于控制气相,当罐体内压力与下游气相系统压力相差大时,控制排气压力和排气流量,以防止因压差大在排气时造成罐体内压力急剧下降而影响分离器的正常排液工作;定压控流阀用于控制液相,当罐体压力与下游液相系统压力相差大时,控制罐体排液压力和排液流量,以防止因压差大造成液相自动排放装置内的可调柱塞不能正常浮起。气相或液相定压控流阀的预定工作压力均要小于罐体内实际生产中的最小工作压力,并大于与罐体连通的气相液相系统压力。当罐体内压力与下游气相或液相系统压力相近时,可以省略此阀,简化分离工艺。The structure of the constant pressure flow control valve is: including a cone flange, a cone head, a spring, a valve body, a nozzle, a nozzle seat and a flange, the center hole of the cone flange is a tapered hole, and there is a cone Head, tapered flange The tapered hole is the same as the taper of the tapered head. There is a cylindrical valve body between the tapered flange and the flange. There is a compression spring in the valve body. The inner thread of the center hole of the flange is connected with a nozzle seat. A nozzle is arranged in the nozzle seat, and the nozzle seat is threadedly connected with the nozzle. The center hole of the nozzle is tapered. The spring controls the pressure and the nozzle controls the flow. The constant pressure flow control valve is used to control the gas phase. When the pressure difference between the tank internal pressure and the downstream gas phase system pressure is large, the exhaust pressure and exhaust flow are controlled to prevent the pressure in the tank from falling sharply due to the large pressure difference when exhausting. The normal discharge work of the separator; the constant pressure flow control valve is used to control the liquid phase. When the pressure difference between the tank body pressure and the downstream liquid phase system pressure is large, control the tank body discharge pressure and flow rate to prevent the liquid phase from being caused by a large pressure difference. The adjustable plunger in the liquid phase automatic discharge device cannot float normally. The predetermined working pressure of the gas-phase or liquid-phase constant pressure control valve should be lower than the minimum working pressure in actual production in the tank, and higher than the pressure of the gas-liquid phase system connected to the tank. When the pressure inside the tank is close to the pressure of the downstream gas phase or liquid phase system, this valve can be omitted to simplify the separation process.
气相自动排放装置包括法兰、凡尔座、凡尔罩和可调柱塞,凡尔座连接在法兰内孔,凡尔座内孔有一个锥面。凡尔罩连接在凡尔座上。凡尔罩为筒状,凡尔罩壁上均布有筛孔,底部有底孔。在凡尔罩内有一个可调柱塞。可调柱塞的结构是:在圆筒状空心柱体的一端螺纹连接有凡尔塞,另一端连接有堵头。凡尔塞的端部为椎体,椎体的锥度与凡尔座内孔锥面的锥度相同。可以根据现场需要的可调柱塞浮力大小,调整空心柱体内的空间大小,改变可调柱塞浮力。The gas phase automatic discharge device includes a flange, a valve seat, a valve cover and an adjustable plunger. The valve seat is connected to the inner hole of the flange, and the valve seat inner hole has a tapered surface. The valve cover is connected on the valve seat. The valve cover is cylindrical, with sieve holes evenly distributed on the wall of the valve cover and bottom holes at the bottom. Inside the valve housing is an adjustable plunger. The structure of the adjustable plunger is: one end of the cylindrical hollow cylinder is threaded with Versailles, and the other end is connected with a plug. The end of Versailles is a vertebral body, and the taper of the vertebral body is the same as that of the taper surface of the inner hole of the Versailles seat. According to the buoyancy of the adjustable plunger required on site, the size of the space in the hollow cylinder can be adjusted to change the buoyancy of the adjustable plunger.
液相自动排放装置的内部结构与气相自动排放装置的结构基本相同,不同点是:液相自动排放装置是在法兰上固定有一个密闭圆筒,密闭圆筒侧壁连接液相排放管线。密闭圆筒内能储存液体,液体进入凡尔罩内,可调柱塞可以悬浮在液面上。另一个不同点是液相自动排放装置的安装方向与气相自动排放装置的安装方向相反。另外液相自动排放装置和气相自动排放装置的尺寸大小可根据气液两相的不同含量进行设计,以更有利于气液两相的顺利排出。The internal structure of the liquid phase automatic discharge device is basically the same as that of the gas phase automatic discharge device. The difference is that the liquid phase automatic discharge device has a closed cylinder fixed on the flange, and the side wall of the closed cylinder is connected to the liquid phase discharge pipeline. The liquid can be stored in the airtight cylinder, and the liquid enters the valve cover, and the adjustable plunger can be suspended on the liquid surface. Another difference is that the installation direction of the liquid phase automatic discharge device is opposite to that of the gas phase automatic discharge device. In addition, the size of the liquid phase automatic discharge device and the gas phase automatic discharge device can be designed according to the different contents of the gas and liquid phases, so as to be more conducive to the smooth discharge of the gas and liquid phases.
油气自动排放旋流气液分离器工作过程:The working process of the oil and gas automatic discharge cyclone gas-liquid separator:
当含有天然气的原油从进口进入罐体后,流入旋流器。在旋流器高速旋转,使天然气从原油中分离。分离后的天然气经气相引入口上升至罐体顶部,通过气相自动排放装置排出。When the crude oil containing natural gas enters the tank from the inlet, it flows into the cyclone. The cyclone rotates at high speed to separate the natural gas from the crude oil. The separated natural gas rises to the top of the tank through the gas phase introduction port, and is discharged through the gas phase automatic discharge device.
分离出的原油沿罐体壁向下流至底部。当分离后的原油累积到一定高度时,从液相排放管进入液相自动排放装置的密闭圆筒。液相自动排液装置进液后,经过凡尔罩筛孔进入凡尔罩。可调柱塞由于浮力作用逐渐离开凡尔座,使原油通过凡尔座的锥孔排出。当罐体的液位逐渐降低,直到无液体进入液相自动排液装置时,可调柱塞会随着液位的下降而下降,直至将凡尔座堵塞。如此反复,完成自动排液任务。The separated crude oil flows down the tank wall to the bottom. When the separated crude oil accumulates to a certain height, it enters the closed cylinder of the liquid phase automatic discharge device from the liquid phase discharge pipe. After the liquid phase automatic draining device enters the liquid, it passes through the sieve hole of the valve cover and enters the valve cover. The adjustable plunger gradually leaves the valve seat due to buoyancy, so that the crude oil is discharged through the tapered hole of the valve seat. When the liquid level of the tank gradually decreases until no liquid enters the liquid-phase automatic liquid draining device, the adjustable plunger will drop along with the liquid level until the valve seat is blocked. Repeat this to complete the automatic draining task.
当罐体内液位太多,来不及排液时,液位上升至气相自动排放装置下部并进入凡尔罩,可调柱塞随液位上浮,并逐渐堵塞凡尔座锥孔。罐体内部压力上升,能加快排液;当罐体内充满液体时,可调柱塞会完全堵塞凡尔座,封住气出口,防止原油从气相出口溢出事故的发生。When the liquid level in the tank is too much to drain, the liquid level rises to the lower part of the gas phase automatic discharge device and enters the valve cover, the adjustable plunger floats up with the liquid level, and gradually blocks the tapered hole of the valve seat. The internal pressure of the tank rises, which can speed up the liquid discharge; when the tank is full of liquid, the adjustable plunger will completely block the valve seat, seal the gas outlet, and prevent the accident of crude oil overflowing from the gas phase outlet.
旋流器的高度应处于罐体进口的下部,气相引入口应高于罐体的进口位置,以达到最佳油气分离效果。The height of the cyclone should be at the lower part of the tank inlet, and the gas phase inlet should be higher than the tank inlet to achieve the best oil-gas separation effect.
本实用新型的有益效果:油气自动排放旋流气液分离器能使气液分离更彻底,气液自动排放装置结构简单体积小,操作时不需要任何外来动力,操作成本低,可以省略掉价格高、结构复杂、操作成本高的电气化自动仪表系统。具有信号转换自动化系统和大浮筒式的液面自控一体化分离器的优点,达到提高气液分离效果又自动排放的功能,并且自动排放装置可拆卸可调节,能够适应不同密度差的气液分离,尤其适合天然气生产场合。The beneficial effects of the utility model: the automatic oil and gas discharge cyclone gas-liquid separator can make the gas-liquid separation more thorough, the structure of the gas-liquid automatic discharge device is simple and small in size, no external power is required for operation, the operation cost is low, and the high price can be omitted , Electrified automatic instrument system with complex structure and high operation cost. It has the advantages of a signal conversion automation system and a large buoy type liquid level automatic control integrated separator, which can improve the gas-liquid separation effect and automatically discharge the function, and the automatic discharge device is detachable and adjustable, and can adapt to gas-liquid separation with different density differences , especially suitable for natural gas production occasions.
下面结合附图和具体实施例对本实用新型作进一步详细说明。Below in conjunction with accompanying drawing and specific embodiment the utility model is described in further detail.
附图说明 Description of drawings
图1是油气自动排放旋流气液分离器整体结构剖面示意图。Fig. 1 is a schematic cross-sectional view of the overall structure of a cyclone gas-liquid separator with automatic discharge of oil and gas.
图2是定压控流阀结构剖面示意图。Fig. 2 is a schematic cross-sectional view of the structure of the constant pressure flow control valve.
图3是气相自动排放装置结构剖面示意图。Fig. 3 is a schematic cross-sectional view of the structure of the gas phase automatic discharge device.
图中,1.排污口,2.罐体,3.旋流器,4.进口,5.气相引入口,6.气相自动排放装置,7.气相排放管线,8.定压控流阀,9.液相排放管线,10.液相自动排放装置,11.辅助排液管,12.阀门,13.锥法兰,14.锥封头,15.弹簧,16.阀体,17.喷嘴,18.喷嘴座,19.法兰,20.法兰,21.凡尔座,22.凡尔罩,23.筛孔,24.凡尔塞,25.空心柱体,26.堵头,27.底孔。In the figure, 1. Sewage outlet, 2. Tank body, 3. Cyclone, 4. Inlet, 5. Gas phase inlet, 6. Gas phase automatic discharge device, 7. Gas phase discharge pipeline, 8. Constant pressure flow control valve, 9. Liquid phase discharge pipeline, 10. Liquid phase automatic discharge device, 11. Auxiliary liquid discharge pipe, 12. Valve, 13. Cone flange, 14. Cone head, 15. Spring, 16. Valve body, 17. Nozzle , 18. Nozzle seat, 19. Flange, 20. Flange, 21. Verseille seat, 22. Verseille cover, 23. Sieve hole, 24. Versailles, 25. Hollow cylinder, 26. Plug, 27. Bottom hole.
具体实施方式 Detailed ways
实施例1:参阅图1。油气自动排放旋流气液分离器,罐体2为立式密闭罐,直径1.5米,高4米。罐体2底部有一个排污口1。罐体2中部距离底部2米处有一个内径为80毫米的进口4。罐体2内距离罐体底部1.5米处有一个旋流器3。罐体2内距离罐体底部1.8米处有一个气相引入口5。在罐体2顶部固定有气相自动排放装置6。气相自动排放装置6连接内径为50毫米的气相排放管线7。气相排放管线7连接有气相出口定压控流阀8。罐体2下部连接有内径为80毫米的液相排放管线9。液相排放管线9连接液相自动排放装置10。液相自动排放装置10连接有液相出口定压控流阀8。在液相排放管线9与液相出口定压控流阀8的管线上连接有辅助排液管11,辅助排液管上有一个手动阀门12。Embodiment 1: Refer to Fig. 1. Oil and gas automatic discharge cyclone gas-liquid separator, the
参阅图2。定压控流阀的结构是由锥法兰13锥封头14弹簧15阀体16喷嘴17喷嘴座18法兰19组成,锥法兰13的中心孔为锥形孔,其锥度是75度。锥法兰13中心孔内有锥封头14,锥法兰13锥形孔与锥封头14的锥度相同,也75度。在锥法兰13和法兰19之间有圆柱筒形的阀体16。阀体16内径是60毫米。阀体16内有压缩弹簧15。法兰19的中心孔内螺纹连接有喷嘴座18。喷嘴座18内有喷嘴17。喷嘴座18与喷嘴17螺纹连接。喷嘴17中心孔为锥形,喷嘴17的中心孔最小直径为10毫米。See Figure 2. The structure of constant pressure flow control valve is made up of
参阅图3。气相自动排放装置6包括法兰20、凡尔座21、凡尔罩22和可调柱塞。凡尔座21螺纹连接在法兰20内孔,凡尔座21内孔有一个锥面,锥度为75度。凡尔罩22螺纹连接在凡尔座21上。凡尔罩22为筒状,直径为100毫米,长度为250毫米。凡尔罩22壁上均布有直径为10毫米的筛孔23。凡尔罩22底部有一个80毫米的底孔27。在凡尔罩22内有一个可调柱塞。可调柱塞的结构是:在圆筒状空心柱体25的一端螺纹连接有凡尔塞24,另一端连接有堵头26。空心柱体25的直径为95毫米,长度100毫米。凡尔塞24的端部为椎体,椎体的锥度为75度,与凡尔座21内孔锥面的锥度相同。See Figure 3. The gas phase
参阅图1。液相自动排放装置10的内部结构与气相自动排放装置6的结构基本相同,不同点是:液相自动排放装置10是在法兰20上固定有一个密闭圆筒,密闭圆筒的直径为120毫米,长度400毫米。密闭圆筒侧壁连接液相排放管线9。液相自动排放装置10的安装方向与气相自动排放装置6的安装方向相反。See Figure 1. The internal structure of the liquid phase
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| CNU2007201493374U Expired - Lifetime CN201055814Y (en) | 2007-05-29 | 2007-05-29 | Cyclone gas-liquid separator with automatic oil-gas discharge function |
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| Country | Link |
|---|---|
| CN (1) | CN201055814Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102794236A (en) * | 2012-08-23 | 2012-11-28 | 上海华畅环保设备发展有限公司 | Method and apparatus for strengthening gas-liquid swirling separation process by underflow gas leakage |
| CN104888981A (en) * | 2015-05-28 | 2015-09-09 | 成都乾瑞矿山工程有限公司 | Overflow pipe |
| CN105736381A (en) * | 2014-12-31 | 2016-07-06 | 英格索尔-兰德公司 | Compressor system with variable lubricant injection orifice |
| WO2018112901A1 (en) * | 2016-12-20 | 2018-06-28 | 中国科学院广州能源研究所 | Gas-liquid separation device suitable for gas hydrate slurry |
| CN110709587A (en) * | 2017-04-14 | 2020-01-17 | Dlh鲍尔斯公司 | Bi-directional jet PCV valve assembly and system |
| CN110939427A (en) * | 2019-12-09 | 2020-03-31 | 哈尔滨工程大学 | Active liquid level control gas-liquid separator utilizing gravity ball |
-
2007
- 2007-05-29 CN CNU2007201493374U patent/CN201055814Y/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102794236A (en) * | 2012-08-23 | 2012-11-28 | 上海华畅环保设备发展有限公司 | Method and apparatus for strengthening gas-liquid swirling separation process by underflow gas leakage |
| CN102794236B (en) * | 2012-08-23 | 2015-12-09 | 上海华畅环保设备发展有限公司 | The method and apparatus of underflow gas leakage strengthening solution-air cyclonic separation process |
| CN105736381A (en) * | 2014-12-31 | 2016-07-06 | 英格索尔-兰德公司 | Compressor system with variable lubricant injection orifice |
| CN105736381B (en) * | 2014-12-31 | 2021-05-04 | 英格索兰工业美国公司 | Compressor system with variable lubricant injection orifices |
| CN104888981A (en) * | 2015-05-28 | 2015-09-09 | 成都乾瑞矿山工程有限公司 | Overflow pipe |
| WO2018112901A1 (en) * | 2016-12-20 | 2018-06-28 | 中国科学院广州能源研究所 | Gas-liquid separation device suitable for gas hydrate slurry |
| CN110709587A (en) * | 2017-04-14 | 2020-01-17 | Dlh鲍尔斯公司 | Bi-directional jet PCV valve assembly and system |
| CN110709587B (en) * | 2017-04-14 | 2021-10-15 | Dlh鲍尔斯公司 | Bidirectional Jet PCV Valve Assemblies and Systems |
| CN110939427A (en) * | 2019-12-09 | 2020-03-31 | 哈尔滨工程大学 | Active liquid level control gas-liquid separator utilizing gravity ball |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Effective date of abandoning: 20070529 |
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| C25 | Abandonment of patent right or utility model to avoid double patenting |