Oil pipe suitable for foam drainage gas production of highly deviated well
阅读说明:本技术 一种适用于大斜度井泡沫排水采气的油管 (Oil pipe suitable for foam drainage gas production of highly deviated well ) 是由 石书强 戚志林 王佳伟 万小进 谢思宇 黄小亮 袁辉 张旭 成涛 莫非 梁玉凯 于 2020-07-02 设计创作,主要内容包括:本发明公开了一种适用于大斜度井泡沫排水采气的油管,包括外筒,以及以可转动方式设置于外筒内的内筒,所述内筒与外筒同轴设置,外筒的上下两端具有相互匹配的螺纹配合结构,内筒的内壁一侧具有沿其长度方向分布的弧形凸起部,所述弧形凸起部沿内筒的径向向内凸起,其凸出最高点靠近弧形凸起部的上端。对油管结构进行优化,主要采用与传统动态搅拌混合理论相反的静态混合理念,充分利用气液在大斜度井段分层特性,以静态结构进行各方向流体引导交汇,从而使气液在该井段内的油管中,上升过程能够持续混合,其混合更均匀彻底,大大提高气体携液能力,同时减小生产压力损耗,有利于保证正常产能。(The invention discloses an oil pipe suitable for foam drainage gas production of a highly deviated well, which comprises an outer barrel and an inner barrel rotatably arranged in the outer barrel, wherein the inner barrel and the outer barrel are coaxially arranged, the upper end and the lower end of the outer barrel are provided with thread matching structures matched with each other, one side of the inner wall of the inner barrel is provided with an arc-shaped bulge distributed along the length direction of the inner barrel, the arc-shaped bulge is inwards bulged along the radial direction of the inner barrel, and the highest point of the bulge is close to the upper end of the arc-shaped bulge. Optimize oil pipe structure, mainly adopt the static mixing theory opposite with traditional dynamic stirring theory, make full use of gas-liquid is at highly deviated well section layering characteristic to static structure carries out each direction fluid guide and crosses, thereby makes the gas-liquid in the oil pipe of this well section, and the process of rising can continuously mix, and its mixes more evenly thoroughly, improves gaseous liquid carrying ability greatly, reduces production pressure loss simultaneously, is favorable to guaranteeing normal productivity.)
1. The utility model provides an oil pipe suitable for gas production of highly deviated well foam drainage which characterized in that: including urceolus (1) to and set up inner tube (2) in urceolus (1) with rotatable mode, inner tube (2) and urceolus (1) coaxial setting, the upper and lower both ends of urceolus (1) have the screw-thread fit structure of mutual matching, and inner wall one side of inner tube (2) has arc bellying (20) along its length direction distribution, radial inside arch of inner tube (2) is followed in arc bellying (20), and its protrusion peak (H) is close to the upper end of arc bellying (20).
2. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 1, wherein: the outer wall of the inner barrel (2) is provided with outer channels (21) which are in one-to-one correspondence with the arc-shaped protrusions (20), the outer channels (21) are spiral, the upper end and the lower end of each outer channel are communicated with the inside of the inner barrel (2), the lower end of each outer channel is communicated with the lower portion of one side, opposite to the arc-shaped protrusions (20), of the corresponding inner channel, and the upper end of each outer channel is communicated with the highest point (H) of the corresponding arc-shaped protrusion (20).
3. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 2, wherein: the rotating directions of two adjacent outer channels (21) are opposite.
4. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 1, wherein: form concave part (22) between two adjacent arc bellying (20), have on the inner wall of inner tube (2) and set up with arc bellying (20) one-to-one interior passageway (23), interior passageway (23) are the heliciform, and both ends are uncovered from top to bottom, and the lower extreme is located one side relative with arc bellying (20), and the upper end corresponds concave part (22).
5. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 4, wherein: the rotating directions of the upper and lower adjacent inner channels (23) are opposite.
6. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 1, wherein: the lower end of the inner cylinder (2) is provided with a conical insertion part (24), and the contour of the inner cavity at the upper end of the inner cylinder (2) is adapted to the insertion part (24).
7. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 6, wherein: and a sealing ring (25) is sleeved on the insertion part (24).
8. Oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 6 or 7, characterized in that: the end part of the insertion part (24) is provided with a key groove (26) with an opening at the lower end, and the inner wall of the upper end of the inner cylinder (2) is provided with a flat key (27) matched with the key groove (26).
9. The oil pipe suitable for foam drainage gas production of highly deviated wells according to claim 8, wherein: the flat key (27) and the arc-shaped bulge (20) are positioned on the same side.
10. An oil pipe suitable for foam drainage gas production of highly deviated wells according to any one of claims 1 to 7, characterized in that: the inner cylinder (2) is arranged in the outer cylinder (1) through a tapered roller bearing (3).
Technical Field
The invention relates to the field of oil gas exploitation tools, in particular to an oil pipe suitable for foam drainage gas exploitation of a highly deviated well.
Background
Foam drainage gas production is one of the main means of natural gas exploitation, and it mainly produces water foam through the physical chemistry mode at the shaft bottom, and under the air current drive, through water foam with shaft bottom hydrops take away from the shaft bottom to reach clean shaft bottom, resume normal production's purpose, nevertheless because the influence of factors such as gas well output, hydrops volume, area of contact, it is not good often to have the foaming effect after adding the foaming agent, and it is relatively poor to carry the liquid effect, and drainage efficiency is low, needs some physical devices, carries out the physics stirring bubble.
In the prior art, a dynamic stirring device is mainly adopted, for example, patent number "CN 201610912449.4", entitled "foaming agent downhole stirring device suitable for foam drainage gas production process", in which the purpose of stirring and mixing is achieved mainly by driving blades to rotate by airflow, and patent number "CN 201510295693.6", entitled "cohesive foam drainage stirrer", which is mainly invented to improve foam drainage effect by changing flow pattern and blade rotation stirring and mixing.
However, when the production well is a highly deviated well and gas and liquid are conveyed by an underground oil pipe, the gas and liquid are seriously separated in the oil pipe of the inclined section because the oil pipe is of a smooth tube structure, the liquid carrying capacity of water bubbles is relatively weak in the process of rising along with airflow, the gas and the liquid must be continuously mixed, and if the stirring device adopting the scheme is adopted, the on-way pressure loss is large, the pressure is insufficient, the normal production is influenced and the like.
The invention mainly aims to solve the problem of serious layering of gas and liquid in an inclined oil pipe, realize static mixing of gas and liquid in an inclined shaft section by optimizing the structure of the oil pipe, reduce pressure loss, ensure production pressure and the like.
Disclosure of Invention
In order to solve the problems, the invention provides an oil pipe suitable for foam drainage gas production of a highly deviated well, which mainly weakens the gas-liquid stratification phenomenon in a static diversion impact mixing mode, improves the gas-liquid mixing effect, reduces the pressure loss and ensures the normal production.
In order to achieve the purpose, the technical scheme of the invention is as follows:
the utility model provides an oil pipe suitable for gas production of highly deviated well foam drainage which the key lies in: the inner cylinder is arranged in the outer cylinder in a rotatable mode, the inner cylinder and the outer cylinder are arranged coaxially, the upper end and the lower end of the outer cylinder are provided with thread matching structures which are matched with each other, one side of the inner wall of the inner cylinder is provided with arc-shaped protrusions distributed along the length direction of the inner cylinder, the arc-shaped protrusions are protruded inwards along the radial direction of the inner cylinder, and the highest point of the protrusions is close to the upper end of the arc-shaped protrusions.
Structure more than adopting, each oil pipe connects gradually through the urceolus during use, and the inner tube is then gas-liquid transmission channel, when using it for highly deviated well, when oil pipe is in the inclined shaft section, because arc bellying place one side is heavier relatively, so under the action of gravity, this side is more close to inclined shaft section downside wall of a well relatively, gas-liquid is when this section flows, liquid is close to inner tube length direction's downside, gaseous upside that is close to length direction, nevertheless under the effect of arc bellying, liquid is every through an arc bellying, must be towards the upside and splash a section distance, thereby produce the mixture with the gas that is in the upside, through following journey multiple action, improve gas-liquid mixture effect greatly, guarantee that gaseous has better liquid-carrying capacity, and because adopt static structure, so loss of pressure is also less relatively.
Preferably, the method comprises the following steps: the outer wall of the inner barrel is provided with outer channels which are arranged in one-to-one correspondence with the arc-shaped protrusions, the outer channels are spiral, the upper ends and the lower ends of the outer channels are communicated with the inside of the inner barrel, the lower end of each outer channel is communicated with the lower portion of one side, opposite to the arc-shaped protrusions, of the inner barrel, and the upper end of each outer channel is communicated with the highest point, corresponding to the arc-shaped protrusions, of. Scheme more than adopting, will be in the gas guide of upside to the downside through outer passageway, and at the emergence of the protrusion peak position of arc bellying, be favorable to improving the height that can reach behind the liquid through protrusion peak, make it more be close to in the upside gas, thereby make gas-liquid mixture more abundant, and because the gas entry point is located the below of arc bellying, can reduce relatively and change side gas pressure, also enable liquid and move towards the upside more easily, in addition, with the direction leading-in and the emergence of spiral, the mixed liquid that produces like this has certain tangential upturned speed, be favorable to further improving mixing effect.
Preferably, the method comprises the following steps: the rotating directions of the upper and lower adjacent outer channels are opposite. By adopting the scheme, the outgoing directions of the two adjacent outer channels form mixed flow in the inner cylinder, the mixed flow is opposite in rotating direction and mutually intersected and impacted, and the mixed flow can be more fully and thoroughly mixed.
Preferably, the method comprises the following steps: a concave part is formed between every two adjacent arc-shaped protruding parts, inner channels which are arranged in one-to-one correspondence with the arc-shaped protruding parts are arranged on the inner wall of the inner barrel, each inner channel is in a spiral shape, the upper end and the lower end of each inner channel are open, the lower end of each inner channel is located on one side opposite to the corresponding arc-shaped protruding part, and the upper end of each inner channel corresponds to the corresponding concave part. The structure and principle of interior passageway and outer passageway are similar, and it is mainly with the gas guide of upside to the concave part position, when improving liquid towards the upside impact capacity, reduce the hydrops of concave part position.
Preferably, the method comprises the following steps: the rotating directions of the upper and lower adjacent inner channels are opposite. By adopting the scheme, the inner channels which are arranged in a staggered mode can serve as guide structures with different rotation directions, and meanwhile, fluid impact guiding can be performed, so that a liquid film is prevented from being formed on the inner wall of the inner cylinder, and the inner cylinder can be better converted into liquid drops so as to be convenient to carry.
Preferably, the method comprises the following steps: the lower end of the inner cylinder is provided with a conical insertion part, and the outline of the inner cavity at the upper end of the inner cylinder is adapted to the insertion part. By adopting the scheme, when the upper oil pipe and the lower oil pipe are connected, the inserting part of the inner cylinder in the upper oil pipe can be inserted into the upper end of the lower inner cylinder, and the conical structure can ensure that the two oil pipes are more tightly inserted, ensure that gas and liquid only flow in the inner cylinder, avoid entering a gap between the inner cylinder and the outer cylinder, and be beneficial to reducing pressure loss.
Preferably, the method comprises the following steps: the insertion part is sleeved with a sealing ring. By adopting the scheme, the connection sealing performance of the inner cylinders is improved, and gas-liquid mixing is further prevented.
Preferably, the method comprises the following steps: the end part of the insertion part is provided with a key groove with an opening at the lower end, and the inner wall of the upper end of the inner cylinder is provided with a flat key matched with the key groove. By adopting the scheme, when the oil pipes are connected, the arc-shaped protrusions of all the inner cylinders can be positioned on the same straight line through the matching of the flat keys and the key grooves, so that the inner cylinders can synchronously rotate after entering the well, namely the arc-shaped protrusions of the inner cylinders of the inclined shaft section are positioned on the lower side of the shaft.
Preferably, the method comprises the following steps: the flat key and the arc-shaped convex part are positioned on the same side. Scheme more than adopting, whether the follow well head that like this can be better judges the arc bellying and is located the downside of inclined shaft section pit shaft.
Preferably, the method comprises the following steps: the inner cylinder is arranged in the outer cylinder through a tapered roller bearing. The tapered roller bearing is adopted, so that the inner cylinder can smoothly rotate, and meanwhile, the tapered roller bearing has good axial load capacity and is beneficial to prolonging the service life of the whole tapered roller bearing.
Compared with the prior art, the invention has the beneficial effects that:
the oil pipe suitable for foam drainage gas production of the highly deviated well mainly adopts a static mixing concept opposite to the traditional dynamic stirring mixing theory, fully utilizes the layering characteristic of gas and liquid in the highly deviated well section, and conducts fluid guiding intersection in each direction by a static structure, so that the gas and the liquid can be continuously mixed in the oil pipe in the well section in the ascending process, the mixing is more uniform and thorough, the gas liquid carrying capacity is greatly improved, the production pressure loss is reduced, and the normal production capacity is favorably ensured.
Drawings
FIG. 1 is a cross-sectional view of the present invention;
FIG. 2 is a perspective view of FIG. 1;
FIG. 3 is a perspective view of the inner barrel;
FIG. 4 is a schematic illustration of the inner and outer channel distribution;
FIG. 5 is a cross-sectional view of FIG. 3;
FIG. 6 is an enlarged view of the upper end structure of the inner cylinder;
FIG. 7 is a schematic longitudinal cross-sectional view of an arcuate raised portion in an oil pipe of the present invention within an incline section;
fig. 8 is a transverse cross-sectional view of the arcuate lobe at the location of point H.
Detailed Description
The present invention will be further described with reference to the following examples and the accompanying drawings.
Referring to fig. 1 to 8, the oil pipe suitable for foam drainage gas production of highly deviated wells mainly comprises an outer cylinder 1 and an
The inner wall of the
On the basis, in the application, the outer wall of the
In a similar way, the inner channel 23 corresponding to the arc-
The outer channel 21 and the inner channel 23 may be formed by surrounding a metal sheet material with the corresponding outer wall or inner wall of the
In order to fully improve the mixing effect, the distribution form of the inner channel and the outer channel is studied, for example, the turning directions of the two upper and lower adjacent outer channels 21 are opposite, the turning directions of the two upper and lower adjacent inner channels 23 are also opposite, even, the turning directions between the outer channel 21 and the inner channel 23 corresponding to the same arc-shaped protruding
The
The connection of upper and lower oil pipe is mainly through the thread fit at upper and lower both ends of urceolus 1, but in order to prevent the gas-liquid cross flow between urceolus 1 and
In order to further ensure that all the
Further, in order to further improve the gas-liquid sealing effect, a packing 25 is fitted over the insertion portion 24, and the packing 25 is positioned above the key groove 26.
In consideration of the installation reliability and safety of the
Referring to fig. 1 to 8, the oil pipe suitable for foam drainage gas production of highly deviated well, during the use, mainly connect through the thread at urceolus 1 upper and lower both ends, connect simultaneously, realize grafting and relatively fixed between each
In the production process, when the
Compared with the traditional mixing and stirring structure, the invention mainly optimizes the structure of the existing oil pipe, adopts a static flow guiding and mixing mode, fully considers the gas-liquid flow characteristic of the inclined shaft section in the highly-inclined shaft, realizes gas-liquid mixing, improves the liquid carrying capacity, reduces the pressure loss and the like.
Finally, it should be noted that the above-mentioned description is only a preferred embodiment of the present invention, and those skilled in the art can make various similar representations without departing from the spirit and scope of the present invention.
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