CN2173661Y - Solid-containing liquid-containing gas separator - Google Patents
Solid-containing liquid-containing gas separator Download PDFInfo
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- CN2173661Y CN2173661Y CN 93246064 CN93246064U CN2173661Y CN 2173661 Y CN2173661 Y CN 2173661Y CN 93246064 CN93246064 CN 93246064 CN 93246064 U CN93246064 U CN 93246064U CN 2173661 Y CN2173661 Y CN 2173661Y
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- riser
- air
- guide vane
- vane mechanism
- outlet
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- 239000007788 liquid Substances 0.000 title claims abstract description 20
- 239000007787 solid Substances 0.000 title claims abstract description 12
- 239000012530 fluid Substances 0.000 claims abstract description 15
- 239000004576 sand Substances 0.000 claims description 19
- 238000000926 separation method Methods 0.000 abstract description 8
- 239000007789 gas Substances 0.000 description 21
- 238000004519 manufacturing process Methods 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
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- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Abstract
一种新型的含固含液气体分离器,它是对含固、 液气体的机械分离装置的改进。它是利用旋流分离 的原理,优化设计成合理的流体流道来达到机械分离 的目的。它主要是由分离器壳体、升气管、特殊的导 流叶片机构及增旋锥筒所构成。
A new type of gas separator containing solid and liquid is an improvement on the mechanical separation device for gas containing solid and liquid. It utilizes the principle of cyclone separation and optimizes the design of a reasonable fluid flow path to achieve the purpose of mechanical separation. It is mainly composed of a separator shell, a riser pipe, a special guide vane mechanism and a spiral cone.
Description
本实用新型涉及一种新型的含固含液气体分离器,它是对含固、液气体的机械分离装置的改进。它是利用叶片机构分离的原理,优化设计成合理的流体流道来达到机械分离的目的,它主要是由壳体、升气管和导流叶片机构所构成。The utility model relates to a novel solid-containing liquid-containing gas separator, which is an improvement of a mechanical separation device for solid-containing and liquid-containing gas. It utilizes the principle of separation of the vane mechanism to optimize the design of a reasonable fluid flow path to achieve the purpose of mechanical separation. It is mainly composed of a shell, a riser pipe and a guide vane mechanism.
在石油的开发工程中,尤其是油气田的开发,常常遇到一些油气田的某些浅层气井井底地层结构松散,采出的气流中含砂量较高,给地面的集输系统造成了许多问题,如带砂气流对地面集输管道、计量仪表及气体处理设备的磨损,都大大地降低了集气系统的寿命,同时由于所带出的砂还将在集气管道、设备内部沉积,使气体过流面积减小,流动阻力增加,也往往给清理和维修带来诸多不变,尤其是含砂气体对节流气嘴的磨损会造成井口流量的失控。虽然并底防砂是比较有效的措施,但其作业费用昂贵,一般只用举高产气井。从经济角度考虑,一般的低产气井采用井下防砂是不合理的。所以,在油气田中,大部分出砂严重的低产气井都被迫关闭。这不仅浪费大量的钻井费用,也使这部分天然气资源得不到及时的开发和利用。因此,如何有效经济地对含砂含液气体进行分离是石油科技工作者所一直研究和探索的。In petroleum development projects, especially in the development of oil and gas fields, it is often encountered that the bottom of some shallow gas wells in some oil and gas fields has a loose stratum structure, and the sand content in the produced gas flow is high, causing many problems to the gathering and transportation system on the ground. Problems, such as the wear and tear on the ground gathering and transportation pipelines, metering instruments and gas processing equipment by the sand-laden airflow, greatly reduce the life of the gas gathering system. The gas flow area is reduced and the flow resistance is increased, which often brings many changes to the cleaning and maintenance, especially the wear of the sand-containing gas on the throttle nozzle will cause the wellhead flow to be out of control. Although bottom sand control is a relatively effective measure, its operation cost is expensive, and generally only high-production gas wells are used. From an economic point of view, it is unreasonable to use downhole sand control in general low-yield gas wells. Therefore, in oil and gas fields, most of the low-production gas wells with severe sand production are forced to shut down. This not only wastes a lot of drilling costs, but also prevents this part of natural gas resources from being developed and utilized in time. Therefore, how to effectively and economically separate sand-containing liquid-containing gas has been researched and explored by petroleum scientists.
本实用新型的目的就在于避免现有技术的不足之处而提供了一种可有效的分离含砂含液气体中的砂、液的汽体除砂除液器。它是利用叶片机构离心的分离原理,将气体中的砂体和液体分离出去。它主要是由圆柱形空心壳体、升气管、导流叶片机构及增旋锥筒构成,其主要的技术特征在于壳体内设置有升气管,并在升气管与壳体的环形空间处设置有导流叶片机构,升气管的出气口设置在壳体顶端外面,升气管的进气口设置在导流叶片机构的下端,其壳体的流体入口设置在升气管出气口和导流叶片机构的中间位置,增旋锥筒设置在升气管的下方。这样,由流体入口进入到壳体内的流体就会在自身压力的作用下再进入导流叶片机构中,通过该机构的导流加速,促使流体中的砂体和液体增大离心力而沿壳体内壁下滑至出口。The purpose of the utility model is to avoid the deficiencies of the prior art and provide a gas desander and liquid remover that can effectively separate sand and liquid in sand-containing and liquid-containing gas. It uses the centrifugal separation principle of the blade mechanism to separate the sand and liquid in the gas. It is mainly composed of a cylindrical hollow shell, a riser, a guide vane mechanism and a spiral cone. Its main technical feature is that a riser is arranged in the shell, and a For the guide vane mechanism, the air outlet of the air riser is arranged outside the top of the housing, the air inlet of the air riser is arranged at the lower end of the guide vane mechanism, and the fluid inlet of the housing is arranged between the air outlet of the air riser and the guide vane mechanism In the middle position, the spiral-increasing cone is arranged under the air pipe. In this way, the fluid entering the casing from the fluid inlet will enter the guide vane mechanism under the action of its own pressure, and the flow through the mechanism will be accelerated, prompting the sand and liquid in the fluid to increase the centrifugal force and flow along the inside of the casing. The wall slides down to the exit.
附图1即为本实用新型的总体结构示意图。Accompanying
附图2即为本实用新型导流叶片机构的结构示意图。Accompanying drawing 2 is the structural representation of the guide vane mechanism of the present utility model.
为了更好地实现本实用新型的上述目的,本实用新型的设计者将导流叶片机构(5)设计成是由水平叶片(10)和垂直叶片(9)组成,其水平叶片(10)的母线为水平线,并与升气管(3)的中心轴线垂直相交;垂直叶片(9)的母线与升气管(3)的中心轴线相平行,其上、下两边分别与水平叶片(10)相连,而其导流叶片机构(5)的水平叶片(10)的两边分别与壳体(4)内壁和升气管(3)外壁相连,并在两个水平叶片(10)的投影相叠处与垂直叶片一起构成叶片机构入口,在投影相叠的末端与垂直叶片(9)一起构成叶片机构出口。In order to better realize the above-mentioned purpose of the utility model, the designer of the utility model designs the guide vane mechanism (5) to be composed of a horizontal blade (10) and a vertical blade (9), and the horizontal blade (10) The busbar is a horizontal line and vertically intersects with the central axis of the air riser (3); the busbar of the vertical blade (9) is parallel to the central axis of the air riser (3), and its upper and lower sides are respectively connected with the horizontal blade (10). The two sides of the horizontal vane (10) of its guide vane mechanism (5) are respectively connected with the inner wall of the casing (4) and the outer wall of the air riser (3), and are vertically aligned with the projections of the two horizontal vanes (10). The vanes together form the vane mechanism inlet, and the projected overlapping ends together with the vertical vanes (9) form the vane mechanism outlet.
对升气管(3),则将其设计成为空心圆柱筒体,上端为出气口(1),设置在壳体(4)顶端的外面;下端为进气口(6),设置在导流叶片机构(5)的下方;其外壁则与导流叶片机构(5)相连。For the air riser (3), it is designed as a hollow cylinder, the upper end is the air outlet (1), which is set outside the top of the casing (4); the lower end is the air inlet (6), which is set on the guide vane The bottom of the mechanism (5); its outer wall is connected with the guide vane mechanism (5).
对其壳体(4),则将其设计成为两端封堵的空心圆柱筒体,其流体入口(2)设置在升气管(3)的出气口(1)与导流叶片机构(5)的中间位置;其出砂口(8)则设置在壳体(4)的底端;并在升气管(3)的进气口(6)下面和出砂口(8)的上方沿壳体(4)内壁设置有增旋锥筒(7),其增旋锥筒(7)带有出口的锥端向下与壳体(4)的出砂口(8)相对。For the shell (4), it is designed as a hollow cylinder with both ends blocked, and its fluid inlet (2) is set at the air outlet (1) of the air riser (3) and the guide vane mechanism (5) the middle position; its sand outlet (8) is set at the bottom of the shell (4); (4) The inner wall is provided with an increasing-rotation cone (7), and the conical end of the increasing-rotation cone (7) with the outlet faces downwards to the sand outlet (8) of the housing (4).
为了更加优化导流叶片机构,设计者则将其导流叶片机构(5)的水平叶片(10)设计成与升气管(3)外壁的交线可以展开成圆弧线、幂函数曲线和指数函数曲线。In order to optimize the guide vane mechanism, the designer designed the horizontal blade (10) of the guide vane mechanism (5) so that the intersection line with the outer wall of the air riser (3) can be developed into arc lines, power function curves and exponential curves. function curve.
附图的图面说明如下:The descriptions of the attached drawings are as follows:
1---升气管出气口 2---流体入口 3---升气管 4---壳体1---air pipe outlet 2---
5---导流叶片机构 6---升气管进气口 7---增旋锥筒 8---出砂口5---Guide vane mechanism 6---Intake port of
9---垂直叶片 10---水平叶片9---
下面将结合附图和实施例来详叙本实用新型的结构特点:The structural characteristics of the utility model will be described in detail below in conjunction with the accompanying drawings and embodiments:
在实际设计和制造中,本实用新型的设计者是将流体入口设计成由切向或径向进入分离器壳体内,以便使含砂含液气体也沿切向或径向进入分离器,然后再进入导流叶片机构内;其导流叶片机构则是设计成由水平叶片和垂直叶片组成,均由三片或四片构成,其两个水平叶片的投影相叠处构成旋转流体的入口和出口,并在两个水平叶片投影相叠处加设垂直叶片;其中,水平叶片的母线为水平线,且与升气管的中心轴垂直相交,水平叶片与升气管外壁的交线可展开成圆弧线、幂函数线或指数曲线。水平叶片的包角在135~225°,水平叶片的入口角在45~75°之间,出口角在10~20°之间;垂直叶片的母线与中心轴平行,其上下两边分别与水平叶片相连,其前缘与升气管外壁相连,其未端与上下水平叶片及壳体构成叶片机构出口,垂直叶片在水平面上的投影可以是圆弧线、椭圆线、渐开线或螺旋线。In actual design and manufacture, the designer of the utility model designed the fluid inlet to enter the separator shell tangentially or radially, so that the sand-containing liquid gas also enters the separator tangentially or radially, and then Then enter the guide vane mechanism; the guide vane mechanism is designed to be composed of horizontal blades and vertical blades, all of which are composed of three or four pieces, and the overlapping projections of the two horizontal blades form the inlet and outlet of the rotating fluid. exit, and add vertical blades where the projections of the two horizontal blades overlap; wherein, the generatrix of the horizontal blades is a horizontal line and intersects vertically with the central axis of the air riser, and the intersection line between the horizontal blades and the outer wall of the air riser can be expanded into a circular arc line, power line, or exponential curve. The wrap angle of the horizontal blade is 135-225°, the inlet angle of the horizontal blade is between 45-75°, and the outlet angle is between 10-20°; Its front edge is connected with the outer wall of the air pipe, and its end forms the outlet of the blade mechanism with the upper and lower horizontal blades and the shell. The projection of the vertical blades on the horizontal plane can be arc lines, ellipse lines, involute lines or spiral lines.
这样,含砂含液流体沿分离器的流体入口进入分离器,经导流叶片机构后加速旋转,形成旋涡流,同时旋涡流在下部的增旋锥筒内可得到进一步的加强,在离心力的作用下,密度较大的固体、液体向壳体壁面运移,气体则形成内叶片机构,向上通过升气管排出,固、液体则由下边的出砂口排出。从而实现除砂液的目的。In this way, the sand-containing liquid-containing fluid enters the separator along the fluid inlet of the separator, and accelerates to rotate after passing through the guide vane mechanism to form a vortex flow. At the same time, the vortex flow can be further strengthened in the lower swirling cone tube. Under the action, the denser solids and liquids migrate to the wall of the shell, the gas forms an inner blade mechanism, and is discharged upward through the air riser, and the solids and liquids are discharged from the sand outlet below. Thereby achieving the purpose of desanding fluid.
本实用新型具有较宽的流量适应范围,它可在低处理量下具有较高的分离效率。其重量轻、体积小,仅为目前油田气井计量站内重力沉降式分离器的数十分之一。The utility model has a wider adaptable flow range and can have higher separation efficiency under low processing capacity. It is light in weight and small in size, which is only a few tenths of the gravity sedimentation separator in the current oil field gas well metering station.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 93246064 CN2173661Y (en) | 1993-12-08 | 1993-12-08 | Solid-containing liquid-containing gas separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 93246064 CN2173661Y (en) | 1993-12-08 | 1993-12-08 | Solid-containing liquid-containing gas separator |
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| Publication Number | Publication Date |
|---|---|
| CN2173661Y true CN2173661Y (en) | 1994-08-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 93246064 Expired - Fee Related CN2173661Y (en) | 1993-12-08 | 1993-12-08 | Solid-containing liquid-containing gas separator |
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| Country | Link |
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| CN (1) | CN2173661Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404996C (en) * | 2006-11-14 | 2008-07-23 | 张曼丽 | River diversion apparatus preventing abrasion for socket-welding and the plate type solid-liquid phase flow heat-exchangers |
| CN103566698A (en) * | 2013-11-20 | 2014-02-12 | 四川科宏石油天然气工程有限公司 | Gas-liquid-solid three-phase separator |
| CN104179729A (en) * | 2014-08-08 | 2014-12-03 | 威海文润测控设备有限公司 | Full-automatic efficient oligodynamic energy-saving and environment-friendly vacuum system |
| CN104524871A (en) * | 2014-12-31 | 2015-04-22 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | Vertical gas-liquid separation device |
| CN104689931A (en) * | 2014-12-31 | 2015-06-10 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | High-pressure gas-liquid separation method |
| CN107013203A (en) * | 2016-01-28 | 2017-08-04 | 中国石油天然气股份有限公司 | Oilfield surface facilities |
| CN107362589A (en) * | 2017-08-01 | 2017-11-21 | 大连理工大学 | A two-stage multi-entry dynamic pressure degasser |
| CN115400506A (en) * | 2021-05-28 | 2022-11-29 | 中国石油天然气股份有限公司 | Sand removing device and sand removing system |
-
1993
- 1993-12-08 CN CN 93246064 patent/CN2173661Y/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404996C (en) * | 2006-11-14 | 2008-07-23 | 张曼丽 | River diversion apparatus preventing abrasion for socket-welding and the plate type solid-liquid phase flow heat-exchangers |
| CN103566698A (en) * | 2013-11-20 | 2014-02-12 | 四川科宏石油天然气工程有限公司 | Gas-liquid-solid three-phase separator |
| CN103566698B (en) * | 2013-11-20 | 2015-11-04 | 四川科宏石油天然气工程有限公司 | Gas-liquid-solid three-phase separator |
| CN104179729A (en) * | 2014-08-08 | 2014-12-03 | 威海文润测控设备有限公司 | Full-automatic efficient oligodynamic energy-saving and environment-friendly vacuum system |
| CN104179729B (en) * | 2014-08-08 | 2017-05-03 | 威海文润测控设备有限公司 | Full-automatic efficient oligodynamic energy-saving and environment-friendly vacuum system |
| CN104524871A (en) * | 2014-12-31 | 2015-04-22 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | Vertical gas-liquid separation device |
| CN104689931A (en) * | 2014-12-31 | 2015-06-10 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | High-pressure gas-liquid separation method |
| CN104689931B (en) * | 2014-12-31 | 2017-06-30 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | High-pressure gas-liquid separation method |
| CN107013203A (en) * | 2016-01-28 | 2017-08-04 | 中国石油天然气股份有限公司 | Oilfield surface facilities |
| CN107013203B (en) * | 2016-01-28 | 2019-05-07 | 中国石油天然气股份有限公司 | Oilfield Surface Facilities |
| CN107362589A (en) * | 2017-08-01 | 2017-11-21 | 大连理工大学 | A two-stage multi-entry dynamic pressure degasser |
| CN115400506A (en) * | 2021-05-28 | 2022-11-29 | 中国石油天然气股份有限公司 | Sand removing device and sand removing system |
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