CN212039403U - Novel gas-liquid separator - Google Patents
Novel gas-liquid separator Download PDFInfo
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- CN212039403U CN212039403U CN201922288804.7U CN201922288804U CN212039403U CN 212039403 U CN212039403 U CN 212039403U CN 201922288804 U CN201922288804 U CN 201922288804U CN 212039403 U CN212039403 U CN 212039403U
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Abstract
The utility model relates to a gas-liquid double-phase separation field is a novel vapour and liquid separator for oil-gas separation. The novel gas-liquid separator comprises an inlet, a guide vane, a rotational flow cavity, a bracket, an outlet, an inertia separation pipe, a gas return pipe, a liquid collection tank, a liquid level pipe and a liquid discharge valve. The gas-liquid separator can perform two-stage separation on the gas-liquid mixture. The gas-liquid mixture enters the inclined rotational flow cavity from the inlet, linear flow of the gas-liquid mixture is changed into rotational flow after passing through the guide vanes, and gas is discharged from the outlet after rotational flow separation. The liquid collected at the bottom of the cyclone cavity flows into a liquid collecting tank through an inertia separation pipe and is collected. The gas-liquid mixture after the first-stage separation can be separated again when flowing through the inertia separation pipe. The utility model discloses a comprehensive utilization hydrocyclone separation and inertial separation technique solve the gas-liquid separation problem, simple structure, and the cost is low, and the practicality is strong, is worth promoting on a large scale.
Description
Technical Field
The utility model relates to a gas-liquid double-phase separation field is a novel vapour and liquid separator who is used for oil-gas separation in the oil gas field development process.
Background
Natural gas is transported in pipelines, often accompanied by condensation or reverse condensation phenomena, as the temperature and pressure vary. When condensation occurs, condensate water and oil condensate appear in the pipeline, and these condensate water and oil condensate form tiny liquid drops in the pipeline under the impact of the high-speed gas flow and are entrained in the natural gas. Meanwhile, the liquid drops can combine with chloride ions in natural gas and carbon dioxide and sulfide in air, and acidic substances are formed to corrode metal equipment such as pipelines and compressors. If the natural gas contains water drops and liquid hydrocarbons, the sealing effect of the compressor can be affected, and the blockage of a pressure regulator of a gas system can be caused. Therefore, to ensure the life and proper operation of the gas transmission equipment, the natural gas needs to be purified.
Disclosure of Invention
The utility model relates to a gas-liquid double-phase separation field is a novel vapour and liquid separator who is used for oil-gas separation in the oil gas field development process. The novel gas-liquid separator comprises an inlet, a guide vane, a rotational flow cavity, a bracket, an outlet, an inertia separation pipe, a gas return pipe, a liquid collection tank, a liquid level pipe and a liquid discharge valve.
This vapour and liquid separator can carry out twice separation to the gas-liquid mixture through whirl chamber and inertia separator tube, and the gas-liquid mixture gets into the whirl chamber of slope by the import, and behind the stator, the straight line of gas-liquid mixture flows and becomes the rotatory flow, and at the rotatory in-process of gas-liquid mixture, the liquid drop can be to the wall motion of limit under the centrifugal force effect simultaneously, and gas can flow to the export from whirl chamber center. The liquid collected at the bottom of the cyclone cavity flows into the liquid collecting tank through the inertia separation pipe. The liquid level pipe is installed in the outside of collection liquid jar, can survey the interior liquid level condition of collection liquid jar through the liquid level pipe. The liquid discharge valve can control the liquid level in the liquid collection tank, so that the liquid after being discharged and separated can be ensured, the liquid sealing effect in the liquid collection tank can be realized, and gas discharge is prevented. When part of the gas-liquid mixture after primary separation flows through the inertia separation pipe, liquid drops impact the semicircular baffle plate in the inertia separation pipe due to inertia to be captured, and gas flows back to the outlet.
Preferably, the novel gas-liquid separator as described above is characterized in that: the gas-liquid separator is mainly made of metal materials, an inlet, an outlet, a cyclone cavity, an inertia separation pipe and the like are connected in a welding mode, and a liquid discharge valve is connected in a threaded mode.
Preferably, the novel gas-liquid separator as described above is characterized in that: the separator is fixed on the bracket for use, so that vibration in the operation process of the equipment is prevented.
The invention comprehensively utilizes the cyclone separation and inertia separation technology, solves the problem of gas-liquid separation, has strong practicability, can improve the separation efficiency by completing the gas-liquid separation in two separation processes, and has low energy consumption and low cost.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below.
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a partial enlarged view of the vortex chamber of the present invention;
1-inlet, 2-guide vane, 3-rotational flow cavity, 4-support, 5-outlet, 6-inertia separation tube, 7-gas return tube, 8-liquid collecting tank, 9-liquid level tube and 10-liquid discharge valve
Detailed Description
The following detailed description of the preferred embodiments of the present invention is provided in conjunction with the accompanying drawings so that the advantages and features of the present invention will be more readily understood by those skilled in the art.
A novel gas-liquid separator is characterized in that: the novel gas-liquid separator comprises an inlet (1), guide vanes (2), a rotational flow cavity (3), a bracket (4), an outlet (5), an inertia separation pipe (6), a gas return pipe (7), a liquid collection tank (8), a liquid level pipe (9) and a liquid discharge valve (10).
The gas-liquid mixture flows in from the inlet (1), and after flowing through the guide vane (2), the linear flow of the gas-liquid mixture is changed into spiral type rotational flow in the rotational flow cavity (3). In the process of rotating flow, liquid drops move towards the side wall under the action of centrifugal force, and gas flows in the center of the rotating flow cavity (3) and reaches the outlet (5) through a pipeline extending into the rotating flow cavity (3) to be discharged. Liquid drops thrown onto the inner wall of the rotational flow cavity (3) can be gathered to flow towards the bottom, finally flow into the inertia separation pipe (6) from the bottom of the rotational flow cavity (3), a semicircular baffle plate is arranged in the inertia separation pipe (6), and after the gas-liquid mixture subjected to primary separation impacts the baffle plate, the liquid drops can be gathered on the surface of the baffle plate and flow into the liquid collection tank (8). The gas separated by the inertia separation pipe (6) can be gathered into the outlet (5) from the gas return pipe (7). The liquid can be collected in the liquid collecting tank (8), and the liquid level in the liquid collecting tank (8) can be observed through the liquid level pipe (9). The liquid discharge valve (10) can control the liquid level to be kept at a certain position of the liquid collection tank, so that a liquid sealing effect is achieved, and gas is prevented from being discharged from the liquid discharge valve (10). The separator is fixed on the bracket (4) for use, so that the vibration in the operation process of the equipment is prevented.
The utility model discloses utilize integrated cyclone and inertial separation technique, solve the gas-liquid separation problem, the practicality is strong, accomplishes gas-liquid separation through twice separation process and can improve separation efficiency, and this equipment energy consumption is little, with low costs simultaneously.
The basic principles and main features of the present invention, and the advantages of the present invention have been described above. Without departing from the spirit and scope of the present invention, there are also provided various changes and modifications that fall within the scope of the claimed invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (7)
1. A novel gas-liquid separator is characterized in that: the gas-liquid separator comprises an inlet (1), a guide vane (2), a rotational flow cavity (3), a support (4), an outlet (5), an inertia separation pipe (6), a gas return pipe (7), a liquid collection tank (8), a liquid level pipe (9) and a liquid discharge valve (10).
2. The novel gas-liquid separator according to claim 1, wherein: the gas-liquid mixture enters the inclined rotational flow cavity (3) from the inlet (1), linear flow of the gas-liquid mixture is changed into rotational flow after passing through the guide vanes (2), meanwhile, in the rotating process of the gas-liquid mixture, liquid drops move to the side wall under the action of centrifugal force, and gas flows to the outlet from the center of the rotational flow cavity (3).
3. The novel gas-liquid separator according to claim 1, wherein: the liquid collected at the bottom of the cyclone cavity (3) flows into a liquid collecting tank (8) through an inertia separation pipe (6) to be collected.
4. The novel gas-liquid separator according to claim 1, wherein: the inertia separation pipe is internally provided with a baffle plate, and the included acute angle between the baffle plate and the horizontal direction is 15 degrees.
5. The novel gas-liquid separator according to claim 1, wherein: when the gas-liquid mixture after primary separation flows through the inertia separation pipe (6), liquid drops in the gas-liquid mixture move along a straight line, collide with the baffle plate when flowing through the semicircular baffle plate in the inertia separation pipe (6), and are gathered on the surface of the baffle plate to be captured and collected.
6. The novel gas-liquid separator according to claim 1, wherein: a liquid level pipe (9) is arranged on the outer side of the liquid collection tank (8), and the liquid level in the liquid collection tank (8) can be observed through the liquid level pipe (9).
7. The novel gas-liquid separator according to claim 1, wherein: the liquid discharge valve (10) can control the liquid level height in the liquid collection tank (8) to achieve a liquid seal effect and prevent gas from being discharged from the liquid discharge valve (10).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201922288804.7U CN212039403U (en) | 2019-12-19 | 2019-12-19 | Novel gas-liquid separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201922288804.7U CN212039403U (en) | 2019-12-19 | 2019-12-19 | Novel gas-liquid separator |
Publications (1)
Publication Number | Publication Date |
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CN212039403U true CN212039403U (en) | 2020-12-01 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201922288804.7U Expired - Fee Related CN212039403U (en) | 2019-12-19 | 2019-12-19 | Novel gas-liquid separator |
Country Status (1)
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CN (1) | CN212039403U (en) |
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2019
- 2019-12-19 CN CN201922288804.7U patent/CN212039403U/en not_active Expired - Fee Related
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20201201 Termination date: 20211219 |