CN200991661Y - Air-liquid cyclone separator with conic-cover shape exhaust pipe structure - Google Patents
Air-liquid cyclone separator with conic-cover shape exhaust pipe structure Download PDFInfo
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- CN200991661Y CN200991661Y CN 200620176017 CN200620176017U CN200991661Y CN 200991661 Y CN200991661 Y CN 200991661Y CN 200620176017 CN200620176017 CN 200620176017 CN 200620176017 U CN200620176017 U CN 200620176017U CN 200991661 Y CN200991661 Y CN 200991661Y
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- exhaust pipe
- gas
- cyclone separator
- cone
- feed cavity
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- 239000007788 liquid Substances 0.000 title claims abstract description 21
- 238000007599 discharging Methods 0.000 claims description 9
- 238000000926 separation method Methods 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000003814 drug Substances 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 239000003208 petroleum Substances 0.000 abstract 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 abstract 1
- 230000001174 ascending effect Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
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Abstract
本实用新型公开了一种具有锥罩形排气管结构的气液旋流分离器，属于气－液分离设备。它由进料腔、导向器、排气管、筒体、锥体、排液管等构成等构成，其特征在于：进料口为轴向或切向进料，排气管为倒锥形结构。其优点在于：分离效率高；结构简单，加工制造方便，成本较低；锥形排气管适用各种结构的气液旋流器，具有广泛的用途。本实用新型适用于石油、化工、环保、医药、食品等行业的气－液分离用的旋流分离设备。
The utility model discloses a gas-liquid cyclone separator with a cone-shaped exhaust pipe structure, which belongs to gas-liquid separation equipment. It consists of a feed chamber, a guide, an exhaust pipe, a cylinder, a cone, a liquid discharge pipe, etc. It is characterized in that: the feed inlet is axial or tangential feeding, and the exhaust pipe is an inverted cone structure. Its advantages are: high separation efficiency; simple structure, convenient processing and manufacturing, and low cost; the tapered exhaust pipe is suitable for gas-liquid cyclones of various structures, and has a wide range of uses. The utility model is suitable for cyclone separation equipment used for gas-liquid separation in petroleum, chemical industry, environmental protection, medicine, food and other industries.
Description
Technical field
The utility model relates to a kind of separation equipment, specifically is a kind of gas-liquid cyclone separator with the hood-shaped exhaust pipe structure of awl, is applicable to the separation of production industries such as oil, chemical industry, environmental protection, medicine, food to drop in the gas.
Background technology
Present widely used gas-liquid cyclone separator, its primary structure comprise feed cavity 1, blast pipe 3, cylindrical shell 4, cone 5 and discharging tube 6, and blast pipe 3 mostly is straight barrel structure (as shown in Figure 1) or funnel-shaped structure (as shown in Figure 2) greatly.For gas-liquid cyclone separator with Fig. 1, Fig. 2 tradition exhaust pipe structure, drop moves near exhaust pipe mouth in the outside wall surface of the acting in conjunction lower edge blast pipe 3 of surface tension, gravity and separator internal pressure field, form " lid is short-circuit flow down ", finally carried out separator, cause separative efficiency to descend by ascending air; And with the increase of separator inlet flow, the liquid measure that is carried out by ascending air also significantly increases.
Summary of the invention
The purpose of this utility model provides a kind of gas-liquid cyclone separator with the hood-shaped exhaust pipe structure of awl, and short-circuit flow is carried out separator by ascending air, the problem that causes separative efficiency to descend owing to cover down to solve that prior art exists.
The purpose of this utility model realizes by following measure: comprise feed cavity, blast pipe, cylindrical shell, cone and discharging tube, feed cavity is connected with the upper end of cylindrical shell, and the lower end of cylindrical shell is connected with the big opening end of cone, and the osculum end of cone is connected with discharging tube; The coaxial feed cavity upper end that penetrates of blast pipe is to cylindrical shell, and it is characterized in that: the bottom of described blast pipe is the horn mouth pyramidal structure.
The semi-cone angle scope of described horn mouth taper is 5 °～80 °.
Described feed cavity is axial-flow type, cut-in type or scroll casing type structure.The eddy flow guider is housed in the axial-flow type feed cavity.
Major advantage of the present utility model is:
1. separative efficiency height.Measuring, separative efficiency can improve more than 10%;
2. simple in structure, convenient processing and manufacture, cost is lower;
3. operating flexibility is big, and when inlet tolerance changed in a big way, separator all can be obtained higher separative efficiency.
4. be suitable for the gas-liquid cyclone separator of various structures, have been widely used.
Description of drawings
Fig. 1 is the structure diagram of the gas-liquid cyclone separator of the straight tube of tradition exhaust pipe structure;
Fig. 2 is the structure diagram of the gas-liquid cyclone separator of conventional funnel shape exhaust pipe structure;
Fig. 3 is the structural representation that the utlity model has the embodiment of taper blast pipe, scroll casing type structure, and wherein last figure is axial cutaway view, and figure below is the vertical view of last figure;
Fig. 4 is the structural representation that the utlity model has the embodiment of taper blast pipe, cut-in type structure, and wherein last figure is axial cutaway view, and figure below is the vertical view of last figure;
Fig. 5 is the axial sectional structure schematic diagram that the utlity model has the embodiment of taper blast pipe, shaft flow structure;
Fig. 6 is the structural representation of the utility model guider.
The specific embodiment
Below in conjunction with accompanying drawing structure of the present utility model and work characteristics are described further.
Referring to Fig. 3～Fig. 6, basic structure of the present utility model comprises feed cavity 1, blast pipe 3, cylindrical shell 4, cone 5, discharging tube 6, feed cavity 1 is connected with the upper end of cylindrical shell 4, and the lower end of cylindrical shell 4 is connected with the big opening end of cone 5, and the osculum end of cone 5 is connected with discharging tube 6.Blast pipe 3 coaxial feed cavity 1 upper ends that penetrate are to cylindrical shell 4, and the bottom of this blast pipe 3 is the horn mouth pyramidal structure.
Described feed cavity 1 is divided into scroll casing type structure (as shown in Figure 3), cut-in type structure (as shown in Figure 4) or axial arrangement (as shown in Figure 5).In the feed cavity 1 of axial arrangement shown in Figure 5, eddy flow guider 2 is housed, is provided with the runner C (referring to Fig. 6) that forms by helicla flute or helical blade at these guider 2 outer peripheral faces.
The utility model is in when work, for embodiment shown in Figure 5, contain liquid gas by feed cavity 1 in guider 2 enters cylindrical shell 4, by cylindrical shell 4 in, forms the centrifugal force field that a high speed is rotated to device 2.Wherein liquid phase is descending at the effect lower edge of centrifugal force field and axial compressive force cylindrical shell 4 and cone 5, discharges through discharging tube 6, and ascending air is discharged through blast pipe 3; Air-flows still are and rotatablely move in the blast pipe 3, wherein the residual liquid mist of part secondary separation to blast pipe inner conical surface under action of centrifugal force forms drop, drop is under surface tension and gravity effect, along conical surface reverse flow to the blast pipe end opening, under the effect of swirling eddy, got rid of again to separator barrel 4, final through discharging tube 6 discharges down.
And, just do not need guider 2 to produce eddy flow, but produce eddy flow by the feed cavity 1 of scroll casing type structure and cut-in type structure for Fig. 3 and embodiment shown in Figure 4.
Claims (4)
1. one kind has the gas-liquid cyclone separator of boring hood-shaped exhaust pipe structure, comprise feed cavity (1), blast pipe (3), cylindrical shell (4), cone (5) and discharging tube (6), feed cavity (1) is connected with the upper end of cylindrical shell (4), the lower end of cylindrical shell (4) is connected with the big opening end of cone (5), and the osculum end of cone (5) is connected with discharging tube (6); Coaxial feed cavity (1) upper end that penetrates of blast pipe (3) is to cylindrical shell (4), and it is characterized in that: the bottom of described blast pipe (3) is the horn mouth pyramidal structure.
2. the gas-liquid cyclone separator with the hood-shaped exhaust pipe structure of awl as claimed in claim 1, it is characterized in that: the semi-cone angle scope of described horn mouth taper is 5 °～80 °.
3. the gas-liquid cyclone separator with the hood-shaped exhaust pipe structure of awl as claimed in claim 1 or 2, it is characterized in that: described feed cavity (1) is cut-in type or scroll casing type structure.
4. the gas-liquid cyclone separator with the hood-shaped exhaust pipe structure of awl as claimed in claim 1 or 2 is characterized in that: described feed cavity (1) is equipped with eddy flow guider (2) for shaft flow structure in this feed cavity (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620176017 CN200991661Y (en) | 2006-12-29 | 2006-12-29 | Air-liquid cyclone separator with conic-cover shape exhaust pipe structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620176017 CN200991661Y (en) | 2006-12-29 | 2006-12-29 | Air-liquid cyclone separator with conic-cover shape exhaust pipe structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200991661Y true CN200991661Y (en) | 2007-12-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620176017 Expired - Fee Related CN200991661Y (en) | 2006-12-29 | 2006-12-29 | Air-liquid cyclone separator with conic-cover shape exhaust pipe structure |
Country Status (1)
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| CN (1) | CN200991661Y (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102423580A (en) * | 2011-08-25 | 2012-04-25 | 中国海洋石油总公司 | Axial-flow pipe type gas-liquid separator |
| CN103175752A (en) * | 2011-12-21 | 2013-06-26 | 中国石油大学(华东) | Intelligent online isokinetic sampling equipment |
| CN103880178A (en) * | 2014-03-07 | 2014-06-25 | 许中华 | Multistage gas stripping and separating integrated anaerobic treatment device |
| CN103880102A (en) * | 2014-03-07 | 2014-06-25 | 许中华 | Volute-type gas-liquid separation device |
| CN104492613A (en) * | 2014-12-09 | 2015-04-08 | 苏州爱纳杰智能科技有限公司 | Cyclone separator overflow pipe with horn-mouth-shaped flow guide plates and cyclone separator |
| CN109356562A (en) * | 2018-10-17 | 2019-02-19 | 青岛理工大学 | Underground sand-filtering type gas-liquid separation device |
| CN111659548A (en) * | 2019-03-08 | 2020-09-15 | 宁波方太厨具有限公司 | Cyclone separation device and range hood with same |
| CN113967392A (en) * | 2021-09-10 | 2022-01-25 | 上海齐耀动力技术有限公司 | Efficient gas-liquid separator, hydrogen-oxygen fuel cell and gas-liquid separation adjusting method |
| CN114273098A (en) * | 2021-12-29 | 2022-04-05 | 上海赛科石油化工有限责任公司 | System and method for separating polymer in acrylonitrile production process |
| WO2022221197A1 (en) * | 2021-04-12 | 2022-10-20 | Supercritical Fluid Technologies, Inc. | Gas-liquid separator assembly |
-
2006
- 2006-12-29 CN CN 200620176017 patent/CN200991661Y/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102423580A (en) * | 2011-08-25 | 2012-04-25 | 中国海洋石油总公司 | Axial-flow pipe type gas-liquid separator |
| CN103175752A (en) * | 2011-12-21 | 2013-06-26 | 中国石油大学(华东) | Intelligent online isokinetic sampling equipment |
| CN103880178A (en) * | 2014-03-07 | 2014-06-25 | 许中华 | Multistage gas stripping and separating integrated anaerobic treatment device |
| CN103880102A (en) * | 2014-03-07 | 2014-06-25 | 许中华 | Volute-type gas-liquid separation device |
| CN103880178B (en) * | 2014-03-07 | 2015-05-20 | 许中华 | Multistage gas stripping and separating integrated anaerobic treatment device |
| CN104492613A (en) * | 2014-12-09 | 2015-04-08 | 苏州爱纳杰智能科技有限公司 | Cyclone separator overflow pipe with horn-mouth-shaped flow guide plates and cyclone separator |
| CN109356562A (en) * | 2018-10-17 | 2019-02-19 | 青岛理工大学 | Underground sand-filtering type gas-liquid separation device |
| CN109356562B (en) * | 2018-10-17 | 2020-08-07 | 青岛理工大学 | Underground sand-filtering type gas-liquid separation device |
| CN111659548A (en) * | 2019-03-08 | 2020-09-15 | 宁波方太厨具有限公司 | Cyclone separation device and range hood with same |
| WO2022221197A1 (en) * | 2021-04-12 | 2022-10-20 | Supercritical Fluid Technologies, Inc. | Gas-liquid separator assembly |
| GB2620885A (en) * | 2021-04-12 | 2024-01-24 | Supercritical Fluid Tech Inc | Gas-liquid separator assembly |
| US12036566B2 (en) | 2021-04-12 | 2024-07-16 | Supercritical Fluid Technologies, Inc. | Gas-liquid separator assembly |
| CN113967392A (en) * | 2021-09-10 | 2022-01-25 | 上海齐耀动力技术有限公司 | Efficient gas-liquid separator, hydrogen-oxygen fuel cell and gas-liquid separation adjusting method |
| CN113967392B (en) * | 2021-09-10 | 2024-02-02 | 上海齐耀动力技术有限公司 | Efficient gas-liquid separator, oxyhydrogen fuel cell and gas-liquid separation adjusting method |
| CN114273098A (en) * | 2021-12-29 | 2022-04-05 | 上海赛科石油化工有限责任公司 | System and method for separating polymer in acrylonitrile production process |
| CN114273098B (en) * | 2021-12-29 | 2024-04-26 | 上海赛科石油化工有限责任公司 | System and method for separating polymer in acrylonitrile production flow |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071219 Termination date: 20101229 |