CN202270591U - Horizontal gas-solid cyclone separator - Google Patents
Horizontal gas-solid cyclone separator Download PDFInfo
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- CN202270591U CN202270591U CN2011201961563U CN201120196156U CN202270591U CN 202270591 U CN202270591 U CN 202270591U CN 2011201961563 U CN2011201961563 U CN 2011201961563U CN 201120196156 U CN201120196156 U CN 201120196156U CN 202270591 U CN202270591 U CN 202270591U
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Abstract
The utility model relates to a horizontal gas-solid cyclone separator which comprises a gas-solid two-phase flow inlet (1), a gas outlet (2), a separator cylinder body (3), a separator cone (4), a solid dust collecting box (5); the gas inlet (1) enters the separator cylinder body (3) along a tangential direction of the separator cylinder body (3) or in a spiral case manner; the gas outlet (2) is axially disposed at the left side of the separator cylinder body (3). The utility model is simple in structure, and easy to arrangement, can greatly reduce flue gas outlet height, shorten the length of flue gas outlet pipelines, has a more compact structure, low manufacturing cost, and relatively low resistance, and is convenient for maintenance; the utility model is applicable to dedusting and purification of dust-containing industrial gas, and gas-solid separation in industry such as chemical engineering, metallurgy, building materials, energy power, and the like.
Description
Technical field
The utility model belongs to Dual-Phrase Distribution of Gas olid separation, powder technology field, particularly relates to a kind of horizontal gas-solid cyclone separator.
Background technology
Cyclone separator is simple in structure because of it, make and install easily and operating cost is low and have feed separation and the dust Control that separative efficiency preferably is widely used in related industries fields such as chemical industry, building materials, the energy, metallurgy, the key equipment in the correlative technology field.Conventional cyclone separator is normally vertical, and promptly the main body of separator is vertically arranged.When the dust-contained airflow flow is big, the height of required separator and the diameter of cylindrical shell will be very big, thereby need a sufficiently high space to be used for the installation of separator.In addition, the air-flow that contains solid material also needed a longer pipe road to connect separator import and the outlet of other relevant devices before getting into cyclone separator.
Horizontal cyclone separator then can be avoided this problem.When adopting horizontal separator, the separator main body horizontal arrangement, then can reduce the whole height of separator significantly, the installing space height that needs reduces, and also is convenient to the operations such as maintenance of installation and operation process.Horizontal cyclone separator can reduce the exhanst gas outlet height behind the separator significantly, shortens the length of exhanst gas outlet pipeline, makes the overall structure of equipment compact more, thereby reaches the purpose of reducing investment outlay and improving its exterior tubing layout.
The utility model content
The utility model technical problem to be solved provides a kind of horizontal gas-solid cyclone separator, and vertical cyclone separator installing space is high in the prior art, equipment is huge to solve, the difficult problem of investment height and operational management inconvenience etc.
The utility model solves the technical scheme that its technical problem adopted: a kind of horizontal gas-solid cyclone separator is provided; Comprise Dual-Phrase Distribution of Gas olid import, gas vent, separator cylindrical shell, separator cone, solid dust collecting box; Described gas feed is for to get into the separator cylindrical shell along the tangential of separator cylindrical shell or by the spiral case mode; Gas vent is coaxial with the separator cylindrical shell, and is positioned at the left side of separator cylindrical shell.
Described separator cylindrical shell horizontal arrangement, the inner surface of separator cylindrical shell are that smooth surface or spiral become 60 °～30 ° angles to arrange the spiral stream guidance fin with the separator cartridge body axis.
Described separator cone is pressed the oblique angle symmetric arrangement in the bottom of separator cylindrical shell, and described oblique angle scope is at 0～30 °; Or in the bottom of separator cylindrical shell vertical, the opposite side of one side is in tilted layout, range of tilt angles is at 0～30 °.
Beneficial effect
The utility model can reduce the whole height of separator significantly, and the installing space height that needs reduces, and is convenient to the operations such as maintenance of installation and operation process.Reduce the exhanst gas outlet height behind the separator significantly, shorten the length of exhanst gas outlet pipeline, make the overall structure of equipment compact more, reduce investment outlay and improve the purpose that its exterior tubing is arranged thereby reach.
Description of drawings
Fig. 1 is horizontal gas-solid cyclone separator principle schematic.
Fig. 2 is horizontal gas-solid cyclone separator vertical view.
Fig. 3 is horizontal gas-solid cyclone separator structure one side cutaway view.
Fig. 4 is horizontal gas-solid cyclone separator structure two side cutaway views.
The specific embodiment
Below in conjunction with specific embodiment, further set forth the utility model.Should be understood that these embodiment only to be used to the utility model is described and be not used in the restriction the utility model scope.Should be understood that in addition those skilled in the art can do various changes or modification to the utility model after the content of having read the utility model instruction, these equivalent form of values fall within the application's appended claims institute restricted portion equally.
Embodiment 1
As shown in Figure 1, a kind of horizontal gas-solid cyclone separator comprises the Dual-Phrase Distribution of Gas olid import 1, gas vent 2, separator cylindrical shell 3, separator cone 4, the solid dust collecting box 5 that are linked in sequence.
When dust-contained airflow carries out the separation of particle by the air inlet pipeline system through separator cylindrical shell 3, separator cone 4 that Dual-Phrase Distribution of Gas olid import 1 gets into the separator level layout; The particle that separates is collected by solid dust collecting box 5, and the air-flow after the separation gets into gas discharge pipe system through gas vent 2.The inner surface of separator cylindrical shell is smooth surface or arranges the spiral stream guidance fin by certain spiral angle (60 °～30 °) that the eddy flow turbulent motion of strengthening flow improves separative efficiency.
Horizontal gas-solid cyclone separator vertical view is as shown in Figure 2.
2 kinds of structures of horizontal gas-solid cyclone separator cone are like Fig. 3, shown in 4.Fig. 3 is that separator cone is pressed certain oblique angle symmetric arrangement in the bottom of the cylindrical shell of separator level layout, and the oblique angle scope is at 0～30 °.Fig. 4 is for separator cone is vertical in bottom one side of the cylindrical shell of separator level layout, opposite side is in tilted layout, and range of tilt angles is at 0～30 °.
Claims (3)
1. horizontal gas-solid cyclone separator; Comprise Dual-Phrase Distribution of Gas olid import (1), gas vent (2), separator cylindrical shell (3), separator cone (4), solid dust collecting box (5); It is characterized in that: described gas feed (1) is for to get into separator cylindrical shell (3) along the tangential of separator cylindrical shell (3) or by the spiral case mode; Gas vent (2) is coaxial with separator cylindrical shell (3), and is positioned at the left side of separator cylindrical shell (3).
2. a kind of horizontal gas-solid cyclone separator according to claim 1; It is characterized in that: described separator cylindrical shell (3) horizontal arrangement, the inner surface of separator cylindrical shell (3) are that smooth surface or spiral become 60 °～30 ° angles to arrange the spiral stream guidance fin with the separator cartridge body axis.
3. a kind of horizontal gas-solid cyclone separator according to claim 1 and 2 is characterized in that: described separator cone (4) is pressed the oblique angle symmetric arrangement in the bottom of separator cylindrical shell (3), and described oblique angle scope is at 0～30 °; Or in the bottom of separator cylindrical shell (3) vertical, the opposite side of a side is in tilted layout, range of tilt angles is at 0～30 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201961563U CN202270591U (en) | 2011-06-13 | 2011-06-13 | Horizontal gas-solid cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201961563U CN202270591U (en) | 2011-06-13 | 2011-06-13 | Horizontal gas-solid cyclone separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202270591U true CN202270591U (en) | 2012-06-13 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201961563U Expired - Fee Related CN202270591U (en) | 2011-06-13 | 2011-06-13 | Horizontal gas-solid cyclone separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202270591U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874236A (en) * | 2015-06-02 | 2015-09-02 | 青岛科技大学 | Horizontal circulating type dust collector |
| US9353586B2 (en) | 2012-05-11 | 2016-05-31 | Mathena, Inc. | Control panel, and digital display units and sensors therefor |
| USD763414S1 (en) | 2013-12-10 | 2016-08-09 | Mathena, Inc. | Fluid line drive-over |
| CN106269312A (en) * | 2015-06-25 | 2017-01-04 | 特斯拉汽车公司 | There is the energy storage volume of whirlpool separator |
| US10160913B2 (en) | 2011-04-12 | 2018-12-25 | Mathena, Inc. | Shale-gas separating and cleanout system |
| CN110735625A (en) * | 2018-07-19 | 2020-01-31 | 中石化洛阳工程有限公司 | online desanding device for oil and gas pipeline without stopping transmission |
| CN110735624A (en) * | 2018-07-19 | 2020-01-31 | 中石化广州工程有限公司 | full-bore pipeline type desander |
| CN110735627A (en) * | 2018-07-19 | 2020-01-31 | 中石化洛阳工程有限公司 | On-line sand remover for oil-gas pipeline without stopping transmission |
-
2011
- 2011-06-13 CN CN2011201961563U patent/CN202270591U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10160913B2 (en) | 2011-04-12 | 2018-12-25 | Mathena, Inc. | Shale-gas separating and cleanout system |
| US9353586B2 (en) | 2012-05-11 | 2016-05-31 | Mathena, Inc. | Control panel, and digital display units and sensors therefor |
| USD763414S1 (en) | 2013-12-10 | 2016-08-09 | Mathena, Inc. | Fluid line drive-over |
| CN104874236A (en) * | 2015-06-02 | 2015-09-02 | 青岛科技大学 | Horizontal circulating type dust collector |
| CN106269312A (en) * | 2015-06-25 | 2017-01-04 | 特斯拉汽车公司 | There is the energy storage volume of whirlpool separator |
| CN106269312B (en) * | 2015-06-25 | 2021-05-14 | 特斯拉公司 | Energy storage container with vortex separator |
| CN110735625A (en) * | 2018-07-19 | 2020-01-31 | 中石化洛阳工程有限公司 | online desanding device for oil and gas pipeline without stopping transmission |
| CN110735624A (en) * | 2018-07-19 | 2020-01-31 | 中石化广州工程有限公司 | full-bore pipeline type desander |
| CN110735627A (en) * | 2018-07-19 | 2020-01-31 | 中石化洛阳工程有限公司 | On-line sand remover for oil-gas pipeline without stopping transmission |
| CN110735624B (en) * | 2018-07-19 | 2021-10-08 | 中石化广州工程有限公司 | Full latus rectum pipeline formula desander |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120613 Termination date: 20150613 |
|
| EXPY | Termination of patent right or utility model |