CN204953153U - Ally oneself with level formula cyclone - Google Patents
Ally oneself with level formula cyclone Download PDFInfo
- Publication number
- CN204953153U CN204953153U CN201520557911.4U CN201520557911U CN204953153U CN 204953153 U CN204953153 U CN 204953153U CN 201520557911 U CN201520557911 U CN 201520557911U CN 204953153 U CN204953153 U CN 204953153U
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- level
- cylinder
- baffle
- grade
- pipe
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- Expired - Fee Related
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Abstract
The utility model discloses a doublestage hydrocyclone separation device relates to technical field such as chemical industry, oil, medicine, include the one -level cyclone who constitutes by one -level cylinder, one -level underflow pipe, one -level cone, one -level overflow pipe, the upper portion of one -level cylinder is equipped with the feed inlet of radial setting the inner wall of one -level cylinder the below of feed inlet is equipped with the one -level baffle, the overflow pipe sets up stretch out in the axle center of baffle the upper portion of cylinder, the sub -unit connection of one -level underflow pipe has a second grade cyclone, second grade cyclone comprises second grade cylinder, second grade cone, second grade overflow pipe and second grade underflow pipe, the one -level underflow pipe with inner wall between the second grade cylinder is equipped with the second grade baffle, the axle center of second grade baffle is equipped with the second grade overflow pipe, the utility model discloses can solve the not thorough problem of weight material separation that ordinary cyclone exists.
Description
Technical field
The utility model relates to the manufacturing technology fields such as chemical industry, oil, medicine, especially a kind of for the device by weight separating substances in gas or liquid or solid.
Background technology
Cyclone separator is a kind of equipment separated from gas or liquid or solid by materials different for proportion (density) in gas or liquid or solid, and this device structure is simple, easy to maintenance, is used widely in every profession and trade; Common cyclone separator is a separable cartridge be made up of circle straight tube and cone cylinder, a tangential input port is arranged at its top, tangentially separable cartridge is entered along separable cartridge for material, material forms one and is rotated down fluid along cylinder barrel after being arranged on the air deflector on separable cartridge top, material heavy in material is downwards from the overflow pipe outflow tube of separable cartridge bottom, in material, the material of lighter weight is not then with the air-flow risen, by the discharging opening outflow tube on cylinder top, enter lower operation, this completes the separation of weight material in material.Because this cyclone separator only has single cylinder, when the difference of input state of matter, there is the halfway problem of weight separating substances.
Summary of the invention
The purpose of this utility model is to provide a kind of twin-stage cyclone separation device, and it can solve the halfway problem of weight separating substances that common cyclone separator exists.
In order to solve the problem, the technical solution adopted in the utility model is:
This twin-stage cyclone separation device, comprise the primary cyclone be made up of one-level cylinder, one-level underflow pipe, one-level cone, one-level overflow pipe, the top of described one-level cylinder is provided with the radial charging aperture arranged, one-level baffle is provided with in the inwall of described one-level cylinder, the below of described charging aperture, described overflow pipe is arranged on the axle center of described baffle and stretches out the top of described cylinder, and the bottom of described one-level underflow pipe is connected with a two-stage cyclone separator; Described two-stage cyclone separator is made up of secondary cylinder, secondary cone, secondary overflow pipe and secondary underflow pipe, inwall between described one-level underflow pipe and described secondary cylinder is provided with secondary baffle, and the axle center of described secondary baffle is provided with secondary overflow pipe.
Further: the surface of described one-level baffle is provided with helicla flute.
Further: the surface of described secondary baffle is provided with helicla flute.
Further: described one-level underflow pipe and described secondary cylinder internal diameter etc. are large.
Further: described one-level baffle is identical with the spiral fluted direction of described secondary baffle.
Further: the diameter of described one-level overflow pipe is greater than the diameter of described secondary overflow pipe.
Owing to have employed technique scheme, the utility model compared with prior art has following beneficial effect:
1, the utility model connects a second-order separation cylinder again in the overflow pipe bottom of one-level cylinder, and make the material flowed downward after one-level cylinder is separated again through secondary separation, separating effect improves greatly;
2, the utility model compact conformation, floor space is little.
Accompanying drawing explanation
Fig. 1 the utility model structural representation.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described:
This twin-stage cyclone separation device, as shown in Figure 1, comprise the primary cyclone be made up of one-level cylinder 4, one-level underflow pipe 8, one-level cone 5, one-level overflow pipe 3, the top of one-level cylinder 4 is provided with the radial charging aperture 1 arranged, one-level baffle 2 is provided with in the inwall of one-level cylinder 4, the below of charging aperture 1, the surface of one-level baffle 2 is provided with helicla flute, and the material that spiral fluted angle need be able to be separated according to reality is arranged; Overflow pipe 3 is pipe, and be arranged on the shaft core position of baffle 2 and stretch out the top seal lid of cylinder 4, the bottom of one-level underflow pipe 8 is connected with a two-stage cyclone separator; Two-stage cyclone separator is made up of secondary cylinder 9, secondary cone 10, secondary overflow pipe 8 and secondary underflow pipe 11, inwall between one-level underflow pipe 8 and secondary cylinder 9 is provided with secondary baffle 7, the surface of secondary baffle 7 is provided with helicla flute, and one-level baffle 2 is identical with the spiral fluted direction of secondary baffle 7; The axle center of secondary baffle 7 is provided with secondary overflow pipe 8, and the diameter of secondary overflow pipe 8 is less than the diameter of one-level overflow pipe 3; One-level underflow pipe 6 and secondary cylinder 9 internal diameter etc. are large.
Claims (6)
1. a twin-stage cyclone separation device, comprise by one-level cylinder (4), one-level underflow pipe (8), one-level cone (5), the primary cyclone that one-level overflow pipe (3) forms, the top of described one-level cylinder (4) is provided with the radial charging aperture (1) arranged, at the inwall of described one-level cylinder (4), the below of described charging aperture (1) is provided with one-level baffle (2), described overflow pipe (3) is arranged on the axle center of described baffle (2) and stretches out the top of described cylinder (4), it is characterized in that: the bottom of described one-level underflow pipe (8) is connected with a two-stage cyclone separator, described two-stage cyclone separator is made up of secondary cylinder (9), secondary cone (10), secondary overflow pipe (8) and secondary underflow pipe (11), inwall between described one-level underflow pipe (8) and described secondary cylinder (9) is provided with secondary baffle (7), and the axle center of described secondary baffle (7) is provided with secondary overflow pipe (8).
2. twin-stage cyclone separation device according to claim 1, is characterized in that: the surface of described one-level baffle (2) is provided with helicla flute.
3. twin-stage cyclone separation device according to claim 1 and 2, is characterized in that: the surface of described secondary baffle (7) is provided with helicla flute.
4. twin-stage cyclone separation device according to claim 3, is characterized in that: described one-level underflow pipe (6) and described secondary cylinder (9) internal diameter etc. are large.
5. twin-stage cyclone separation device according to claim 4, is characterized in that: described one-level baffle (2) is identical with the spiral fluted direction of described secondary baffle (7).
6. twin-stage cyclone separation device according to claim 5, is characterized in that: the diameter of described one-level overflow pipe (3) is greater than the diameter of described secondary overflow pipe (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520557911.4U CN204953153U (en) | 2015-07-29 | 2015-07-29 | Ally oneself with level formula cyclone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520557911.4U CN204953153U (en) | 2015-07-29 | 2015-07-29 | Ally oneself with level formula cyclone |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204953153U true CN204953153U (en) | 2016-01-13 |
Family
ID=55048251
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520557911.4U Expired - Fee Related CN204953153U (en) | 2015-07-29 | 2015-07-29 | Ally oneself with level formula cyclone |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204953153U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110283631A (en) * | 2019-06-18 | 2019-09-27 | 鲁西化工集团股份有限公司 | A kind of device and method of fine coal pressurization continuous gasification furnace crude synthesis gas gas, liquid, solid three phase separation |
-
2015
- 2015-07-29 CN CN201520557911.4U patent/CN204953153U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110283631A (en) * | 2019-06-18 | 2019-09-27 | 鲁西化工集团股份有限公司 | A kind of device and method of fine coal pressurization continuous gasification furnace crude synthesis gas gas, liquid, solid three phase separation |
| CN110283631B (en) * | 2019-06-18 | 2020-09-29 | 鲁西化工集团股份有限公司 | Gas, liquid and solid three-phase separation device and method for coarse synthesis gas of pulverized coal pressurized continuous gasifier |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160113 Termination date: 20160729 |