CN210331962U - Gas-liquid cyclone separator - Google Patents
Gas-liquid cyclone separator Download PDFInfo
- Publication number
- CN210331962U CN210331962U CN201920941312.0U CN201920941312U CN210331962U CN 210331962 U CN210331962 U CN 210331962U CN 201920941312 U CN201920941312 U CN 201920941312U CN 210331962 U CN210331962 U CN 210331962U
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- barrel
- cylinder body
- gas
- liquid cyclone
- cyclone separator
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- 239000007788 liquid Substances 0.000 title claims abstract description 21
- 238000003756 stirring Methods 0.000 claims abstract description 19
- 238000009434 installation Methods 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 3
- 230000007423 decrease Effects 0.000 claims description 2
- 238000000926 separation method Methods 0.000 abstract description 4
- 239000007791 liquid phase Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000007792 gaseous phase Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 210000002445 nipple Anatomy 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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Abstract
The utility model relates to a gas-liquid cyclone separator, which comprises a cylinder body, wherein the upper part of the cylinder body is a conical cylinder body, the middle part is a columnar cylinder body, the lower part is an inverted cone cylinder body, the middle part of the upper end of the conical cylinder body is provided with an exhaust pipe communicated with the inside of the cylinder body, the inverted cone cylinder body is internally and vertically provided with a stirring shaft which is coaxial with the inverted cone cylinder body, at least one stirrer is arranged on the stirring shaft at intervals from top to bottom, the lower bottom of the inverted cone cylinder body is provided with a drain pipe communicated with the inside of the cylinder body at the side of the stirring shaft, the lower part of the columnar cylinder body is peripherally provided with two inlet pipes which are tangential with the columnar cylinder body, the inlet pipes are communicated with the inside of the cylinder body and are parallel to the two inlet pipes, one inlet pipe, reasonable in design can carry out cyclone to the gas-liquid, and the separation is effectual.
Description
Technical Field
The utility model relates to a gas-liquid cyclone.
Background
The gas-liquid separation technology is generally applied to the fields of petroleum energy, mineral processing, biological medical treatment and the like, and is particularly widely applied to certain industries with high pollution control and environmental protection requirements. However, the conventional gas-liquid separator has a complicated structure and a poor separation effect.
Disclosure of Invention
In view of this, the utility model provides a gas-liquid cyclone.
The utility model provides a scheme that technical problem adopted is, a gas-liquid cyclone, the novel nipple rectifier comprises a cylindrical shel, mid-mounting has the inside blast pipe of intercommunication barrel on the barrel, the (mixing) shaft rather than with the axle center is installed to the lower part in the barrel, from top to bottom interval installation at least one agitator on the (mixing) shaft, two and its tangent inlet pipes are installed to the lower part in the barrel, inlet pipe intercommunication barrel is inside, two inlet pipes parallel, one of them inlet pipe is located even another inlet pipe offside, the inside fluid-discharge tube of intercommunication barrel is installed to the bottom under the barrel in the (mixing) shaft side, inside at least one conical plate of interval installation from top to bottom of barrel, a plurality of exhaust apertures have been seted up on the conical plate, the conical.
Further, barrel upper portion is the toper barrel, the middle part is the column barrel, the lower part is the back taper barrel, the blast pipe is installed in toper barrel upper end middle part, the conical plate is installed on the column barrel, the inlet pipe is installed in column barrel lower part week side and tangent with the column barrel, the (mixing) shaft is installed in the back taper barrel, the fluid-discharge tube is installed in back taper barrel bottom.
Furthermore, the stirring shaft is installed in the cylinder through a bearing seat, and the lower end of the stirring shaft penetrates through the lower bottom of the inverted cone-shaped cylinder and then is connected with the motor through a coupler for transmission.
Further, the agitator sets up threely at least, and the diameter of each agitator decreases progressively from top to bottom in proper order.
Furthermore, the stirrer comprises a mounting sleeve, a plurality of stirring blades are uniformly distributed on the periphery of the mounting sleeve, the mounting sleeve is sleeved on the stirring shaft and locked by screws, and the stirring blades and the mounting sleeve are welded into a whole.
Further, the conical plates are arranged in at least three numbers.
Furthermore, the upper end of the conical plate is provided with an opening, and the opening, the cylinder and the exhaust pipe are coaxial.
Compared with the prior art, the utility model discloses following beneficial effect has: simple structure, reasonable in design can carry out cyclone to the gas-liquid, and the separation is effectual.
Drawings
The following describes the present invention with reference to the accompanying drawings.
Fig. 1 is a schematic structural view of the separator without a motor.
In the figure: 1-an exhaust pipe; 2-a conical cylinder; 3-a tapered plate; 4-exhaust aperture; 5-a cylindrical barrel; 6-feeding pipe; 7-inverted cone-shaped cylinder; 8-a liquid discharge pipe; 9-stirring shaft; 10-a stirrer.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and the following detailed description.
As shown in figure 1, the gas-liquid cyclone separator comprises a cylinder body, wherein the upper part of the cylinder body is a conical cylinder body 2, the middle part of the cylinder body is a columnar cylinder body 5, the lower part of the cylinder body is an inverted cone-shaped cylinder body 7, the middle part of the upper end of the conical cylinder body is provided with an exhaust pipe 1 communicated with the inside of the cylinder body, a stirring shaft 9 which is coaxial with the inverted cone-shaped cylinder body is vertically arranged in the inverted cone-shaped cylinder body, at least one stirrer 10 is arranged on the stirring shaft at intervals from top to bottom, a liquid discharge pipe 8 communicated with the inside of the cylinder body is arranged at the lower bottom of the inverted cone-shaped cylinder body at the, one of them inlet pipe is located and links another inlet pipe offside, and at least one toper board 3 is installed from top to bottom interval to the inside cylindrical barrel, has seted up a plurality of exhaust apertures 4 on the toper board, and the toper board is located the inlet pipe top. During the use, in the fluid flowed into the column barrel simultaneously from two inlet pipes, formed the whirl, the whirl is under the effect of the agitator of same direction of rotation, and the power of rotation further strengthens, and the increase of power of rotation can form stronger centrifugal force, and centrifugal force makes the gaseous phase and the liquid phase in the fluid separate, and liquid phase main distribution is in being close to barrel wall department, and gaseous phase main distribution is in the central point position around the barrel axis. Meanwhile, as the gas phase and the liquid phase have density difference, the gas phase flows to the upper part of the cylinder body and further intercepts part of the liquid phase by the conical plate when passing through the conical plate, and the gas phase continuously flows upwards from the small exhaust hole and flows out through the exhaust pipe.
In this embodiment, the stirring shaft is installed in the barrel through the bearing frame, and the transmission is connected with the motor through the shaft coupling behind the (mixing) shaft lower extreme wears to establish the bottom under the back taper barrel.
In this embodiment, the agitator sets up threely at least, and the diameter of each agitator from top to bottom progressively reduces in proper order, and such structural design can cooperate with the structure of back taper barrel, is favorable to improving the homogeneity of power soon.
In this embodiment, the agitator includes the installation cover, and a plurality of stirring vane are evenly distributed to installation cover periphery circumference, and the installation cover suit is on the (mixing) shaft and through the screw lock solid, and stirring vane welds integratively with the installation cover.
In this embodiment, the toper board sets up three at least, sets up three and above toper board, is favorable to many times to effectively separating the liquid phase, prevents that the liquid phase from flowing by the blast pipe. Meanwhile, the small exhaust holes are densely distributed on the conical plate, so that the liquid phase can be effectively intercepted, the gas phase is discharged from the small exhaust holes, and the liquid phase flows away from the liquid discharge pipe due to the influence of gravity.
In this embodiment, the upper end of the conical plate is open, and the opening, the cylinder and the exhaust pipe are coaxial.
The above-mentioned preferred embodiments, further detailed description of the objects, technical solutions and advantages of the present invention, it should be understood that the above-mentioned are only preferred embodiments of the present invention, and should not be construed as limiting the present invention, and any modifications, equivalent substitutions, improvements, etc. made within the spirit and principle of the present invention should be included within the scope of the present invention.
Claims (7)
1. The utility model provides a gas-liquid cyclone, includes the barrel, its characterized in that: the utility model discloses a barrel, including the barrel, the barrel is provided with the inlet pipe of intercommunication barrel, the middle part is installed the blast pipe of intercommunication barrel inside on the barrel, the (mixing) shaft rather than with the axle center is installed to the lower part in the barrel, from top to bottom interval installation at least one agitator on the (mixing) shaft, two inlet pipes rather than tangent inlet pipes are installed to the lower part in the barrel, inlet pipe intercommunication barrel is inside, two inlet pipes parallel, one of them inlet pipe is located and links another inlet pipe offside, the inside fluid-discharge tube of intercommunication barrel is installed to the bottom under the barrel in the (mixing) shaft side, barrel is inside from top to bottom interval installation at least.
2. The gas-liquid cyclone separator according to claim 1, wherein: barrel upper portion is the toper barrel, the middle part is the column barrel, the lower part is the back taper barrel, the blast pipe is installed in toper barrel upper end middle part, the toper board is installed on the column barrel, the inlet pipe is installed in column barrel lower part week side and tangent with the column barrel, the (mixing) shaft is installed in the back taper barrel, the fluid-discharge tube is installed in back taper barrel bottom.
3. The gas-liquid cyclone separator according to claim 1 or 2, wherein: the stirring shaft is arranged in the barrel through a bearing seat, and the lower end of the stirring shaft penetrates through the lower bottom of the inverted cone-shaped barrel and is connected with the motor through a coupler for transmission.
4. The gas-liquid cyclone separator according to claim 2, wherein: the agitator sets up threely at least, and the diameter of each agitator from top to bottom decreases progressively in proper order.
5. The gas-liquid cyclone separator according to claim 4, wherein: the stirrer comprises a mounting sleeve, a plurality of stirring blades are uniformly distributed on the periphery of the mounting sleeve, the mounting sleeve is sleeved on the stirring shaft and locked by screws, and the stirring blades and the mounting sleeve are welded into a whole.
6. The gas-liquid cyclone separator according to claim 1, wherein: the conical plates are at least three.
7. The gas-liquid cyclone separator according to claim 1, wherein: the upper end of the conical plate is provided with an opening, and the opening, the cylinder body and the exhaust pipe are coaxial.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920941312.0U CN210331962U (en) | 2019-06-21 | 2019-06-21 | Gas-liquid cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920941312.0U CN210331962U (en) | 2019-06-21 | 2019-06-21 | Gas-liquid cyclone separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210331962U true CN210331962U (en) | 2020-04-17 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920941312.0U Active CN210331962U (en) | 2019-06-21 | 2019-06-21 | Gas-liquid cyclone separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210331962U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112827674A (en) * | 2020-12-30 | 2021-05-25 | 东北石油大学 | A reciprocating intermittent cyclone separation device |
| CN112827669A (en) * | 2020-12-30 | 2021-05-25 | 东北石油大学 | An intermittent gas-liquid cyclone separator |
| CN113144676A (en) * | 2021-04-02 | 2021-07-23 | 上海灿越化工科技有限公司 | Novel mixed liquid degasser |
| CN113187460A (en) * | 2021-04-16 | 2021-07-30 | 东北石油大学 | Shale oil production underground rotational flow gravity coupling driving type gas-liquid separation device |
| CN113262532A (en) * | 2021-05-21 | 2021-08-17 | 王雯雯 | Spiral-flow type sand settling device for hydraulic engineering construction and implementation method thereof |
| CN113457285A (en) * | 2021-08-06 | 2021-10-01 | 山西国际能源集团宏光发电有限公司 | Steam-water separation device at outlet of vacuum pump |
| CN117883881A (en) * | 2024-03-14 | 2024-04-16 | 福建伊普思实业有限公司 | Gas-liquid separator and preparation process thereof |
-
2019
- 2019-06-21 CN CN201920941312.0U patent/CN210331962U/en active Active
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112827674A (en) * | 2020-12-30 | 2021-05-25 | 东北石油大学 | A reciprocating intermittent cyclone separation device |
| CN112827669A (en) * | 2020-12-30 | 2021-05-25 | 东北石油大学 | An intermittent gas-liquid cyclone separator |
| CN113144676A (en) * | 2021-04-02 | 2021-07-23 | 上海灿越化工科技有限公司 | Novel mixed liquid degasser |
| CN113187460A (en) * | 2021-04-16 | 2021-07-30 | 东北石油大学 | Shale oil production underground rotational flow gravity coupling driving type gas-liquid separation device |
| CN113187460B (en) * | 2021-04-16 | 2022-04-19 | 东北石油大学 | Shale oil production underground rotational flow gravity coupling driving type gas-liquid separation device |
| CN113262532A (en) * | 2021-05-21 | 2021-08-17 | 王雯雯 | Spiral-flow type sand settling device for hydraulic engineering construction and implementation method thereof |
| CN113457285A (en) * | 2021-08-06 | 2021-10-01 | 山西国际能源集团宏光发电有限公司 | Steam-water separation device at outlet of vacuum pump |
| CN117883881A (en) * | 2024-03-14 | 2024-04-16 | 福建伊普思实业有限公司 | Gas-liquid separator and preparation process thereof |
| CN117883881B (en) * | 2024-03-14 | 2024-06-04 | 福建伊普思实业有限公司 | Gas-liquid separator and application method thereof |
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