CN201366382Y - Cyclone separator with orifice plate exhaust structure - Google Patents
Cyclone separator with orifice plate exhaust structure Download PDFInfo
- Publication number
- CN201366382Y CN201366382Y CNU2009200181410U CN200920018141U CN201366382Y CN 201366382 Y CN201366382 Y CN 201366382Y CN U2009200181410 U CNU2009200181410 U CN U2009200181410U CN 200920018141 U CN200920018141 U CN 200920018141U CN 201366382 Y CN201366382 Y CN 201366382Y
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- China
- Prior art keywords
- orifice plate
- separator tube
- separator
- blast pipe
- cyclone separator
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Abstract
The utility model relates to a cyclone separator with orifice plate exhaust structure, comprising a guide apparatus, a separator tube, an exhaust pipe and an ash bucket, wherein the lower port of the exhaust pipe is provided with an orifice plate which is connected into a whole, and the orifice plate is evenly provided with ostioles; the lower part of the exhaust pipe extends deeply into the upper part inside the separator tube in a coaxial way, and the guide apparatus which is installed on the exhaust pipe coaxially is arranged between the exhaust pipe and the separator tube; a plurality of guide vanes uniformly arranged on the guide apparatus circumferencially and the inner wall of the separator tube form a flow channel leading air flow to change direction. The lower end of the separator tube is provided with an arc taper section connected into a whole, and the arc taper section is installed inside the ash bucket closedly. The cyclone separator has the advantages of high separating efficiency, little pressure reduction and low energy consumption, and can be separately used or combined into a multi-tube cyclone separator so as to be widely applied to dedusting and purifying petrochemical high-temperature flue gas as well as recovering solid particles, and used for industrial departments of coal gasification, plastics, light industry, metallurgy and the like.
Description
Technical field
The utility model relates to a kind of cyclone separator that has the orifice plate exhaust structure, belongs to the device that utilizes action of centrifugal force to come dust in the divided gas flow.
Background technology
The cyclone separator of now general axial admission is by guider, separator tube, compositions such as blast pipe and ash bucket.The coaxial top that is deep in the separator tube of exhaust pipe lower part, be the coaxial guider that is installed on the blast pipe between blast pipe and the separator tube, the runner that the formation of several along the circumferential direction evenly distributed guide vanes and separator tube inwall turns to air-flow above the guider.The bottom sealing of separator tube is installed in the ash bucket.Ubiquitous problem is that cyclone separator exports local regional gas stream and has pulsation of high turbulent flow and strong secondary vortices motion phenomenon in the commercial Application process, cause the cyclone separator operating flexibility poor thus, pressure drop is big, and the energy consumption height has seriously hindered the energy efficiency of enterprise.
The utility model content
The technical problems to be solved in the utility model provides a kind of separative efficiency height, pressure drop is little, energy consumption the is low cyclone separator that has the orifice plate exhaust structure.
A kind of cyclone separator that has the orifice plate exhaust structure of the utility model comprises guider, separator tube and blast pipe, and the blast pipe lower port is provided with the orifice plate that is connected as a single entity, and is provided with aperture on orifice plate uniformly; The separator tube lower end is provided with the circular arc awl section that is connected as a single entity.
A kind of cyclone separator that has the orifice plate exhaust structure of the utility model, its aperture plate height are 0.05～4 times of blast pipe internal diameter; The cross sectional shape of opening aperture on the orifice plate is circular, square and oval; The angle θ of aperture is 0 °～45 °, and θ is the central axis of aperture and the angle between the blast pipe central axis; The aperture gross area is 30%～80% of a blast pipe internal diameter area.
A kind of cyclone separator that has the orifice plate exhaust structure of the utility model, wherein the height of circular arc awl section is 0.6～0.9 times of separator tube interior diameter; Arc radius is 1.3～1.6 times of separator tube interior diameter; Circular arc awl section lower port interior diameter is 0.5～0.7 times of separator tube interior diameter, is 0.9～1.2 times of blast pipe interior diameter.
A kind of advantage and good effect that has the cyclone separator of orifice plate exhaust structure of the utility model is: in blast pipe lower port installing hole plate structure, to become multiply by one from the air-flow that the blast pipe lower port enters according to the perforate number like this, strengthened high turbulent flow pulsation that exports local regional gas stream and the inhibition ability that strong secondary vortices is moved, reduced tornadotron pressure drop and energy consumption significantly; The variation of orifice plate perforated area and blowing angle can be regulated the interaction between the multiply air-flow, weakens the rotation function loss of air-flow in the blast pipe, further reduces the pressure drop of tornadotron; The orifice plate of blast pipe inlet reduces the exhaust circulation area, increased the spin intensity of air-flow in the tornadotron, has prolonged particle separated time in tornadotron, has improved the separative efficiency of tornadotron.
Description of drawings
Fig. 1 is a kind of cyclone separator aufbauprinciple schematic diagram that has the orifice plate exhaust structure of the utility model;
Fig. 2 is the A-A generalized section (amplification) of Fig. 1;
Fig. 3 is blowing angle schematic diagram (amplification).
1. cyclone inlet among the figure, 2. guider, 3. separator tube, 4. blast pipe, 5. orifice plate, 6. circular arc awl section, a 7. circular arc awl section lower port, 8. separator tube lower port, 9. ash bucket, 10. aperture, 11. blast pipe lower port.
The specific embodiment
A kind of cyclone separator that has the orifice plate exhaust structure of the utility model comprises separator tube 3, blast pipe 4 and ash bucket 9, the coaxial top that is deep in the separator tube 3, blast pipe 4 bottoms, be the coaxial guider 2 that is installed on the blast pipe 4 between blast pipe 4 and the separator tube 3, the runner that several along the circumferential direction evenly distributed guide vanes and the formation of separator tube 3 inwalls turn to air-flow above the guider 2; Blast pipe 4 lower port are provided with the coaxial orifice plate 5 that gos deep into blast pipe 4 that is connected as a single entity, and are provided with aperture 10 on orifice plate 5 uniformly; The lower end of separator tube 3 is provided with the circular arc awl section 6 that is connected as a single entity; The bottom sealing of separator tube 3 is installed in the ash bucket 9.
Orifice plate 5 highly is 0.1 times of blast pipe 4 internal diameters; The cross sectional shape of opening aperture 10 on the orifice plate 5 is for circular; The angle θ of aperture 10 is 0 °, and θ is the central axis of aperture 10 and the angle between blast pipe 4 central axis; Aperture 10 gross areas are 50% of blast pipe 4 internal diameter areas.
The height of circular arc awl section 6 is 0.7 times of separator tube 3 interior diameters; The arc radius of circular arc awl section 6 is 1.4 times of separator tube 3 interior diameters; Circular arc awl section lower port 7 interior diameters are 0.6 times of separator tube 3 interior diameters, are 0.9 times of blast pipe 4 interior diameters.
During use, dust-contained airflow enters cyclone separator from cyclone inlet 1 vertically, be transformed into high speed rotary motion after forming the runner that air-flow is turned to through the guide vane on the guider 2 and separator tube 3 inwalls, particle wherein is subjected to action of centrifugal force and separatedly gets off to the motion of separator tube 3 inwalls gradually.The air-flow entrained particles realizes the centrifugation of gas-solid two-phase downwards in separator tube 3 and circular arc awl section 6.The particle that separates enters circular arc awl section 6 with descending air-flow, enters ash bucket 9 from circular arc awl section lower port 7.Descending air-flow after the purification is turned back into air upflow in circular arc awl section 6 bottoms, and the separator tube lower port 8 of upwards flowing through, aperture 10 enter blast pipe 4 at last and discharge.The fraction air-flow that enters ash bucket 9 from circular arc awl section lower port 7 is turned back into air upflow in ash bucket 9 bottoms, enters circular arc awl section 6 through circular arc awl section lower port 7, and the separator tube lower port 8 of equally upwards flowing through, aperture 10 enter blast pipe 4 at last and discharge.
The utility model is a kind of, and to have the cyclone separator structure of orifice plate exhaust structure simply compact, both can use separately, also can form multicyclone, can be widely used in the dedusting of petrochemical industry high-temperature flue gas, purify recovery with solid particle, also can be applicable to coal gasification, industrial departments such as plastics, light industry and metallurgy.
Claims (3)
1, a kind of cyclone separator that has the orifice plate exhaust structure, it is by guider (2), separator tube (3), blast pipe (4), orifice plate (5), circular arc awl section (6), ash bucket (9) is formed; Described blast pipe (4) lower end is provided with the orifice plate (5) that is connected as a single entity, and it is characterized in that being provided with uniformly on described orifice plate (5) aperture (10); Described separator tube (3) lower end is provided with the circular arc awl section (6) that is connected as a single entity.
2, a kind of cyclone separator that has the orifice plate exhaust structure according to claim 1 is characterized in that described orifice plate (5) highly is 0.05～4 times of blast pipe (4) internal diameter; Described orifice plate (5) has aperture (10), and the cross sectional shape of aperture (10) is circular, square and oval; Described aperture (10) is to offer with angle θ, and angle θ is the central axis of described aperture (10) and the angle between blast pipe (4) central axis, and angle θ is 0 °～45 °; Described aperture (10) gross area is 30%～80% of described blast pipe (a 4) internal diameter area.
3, a kind of cyclone separator that has the orifice plate exhaust structure according to claim 1, the height that it is characterized in that described circular arc awl section (6) are 0.6～0.9 times of separator tube (3) interior diameter; The arc radius of described circular arc awl section (6) is 1.3～1.6 times of separator tube (3) interior diameter; Described circular arc awl section lower port (7) interior diameter is 0.5～0.7 times of separator tube (3) interior diameter; Described circular arc awl section lower port (7) interior diameter is 0.9～1.2 times of blast pipe (4) interior diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009200181410U CN201366382Y (en) | 2009-01-13 | 2009-01-13 | Cyclone separator with orifice plate exhaust structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009200181410U CN201366382Y (en) | 2009-01-13 | 2009-01-13 | Cyclone separator with orifice plate exhaust structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201366382Y true CN201366382Y (en) | 2009-12-23 |
Family
ID=41485283
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2009200181410U Expired - Fee Related CN201366382Y (en) | 2009-01-13 | 2009-01-13 | Cyclone separator with orifice plate exhaust structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201366382Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104084322A (en) * | 2014-07-11 | 2014-10-08 | 江苏华泰重工装备有限公司 | Particle separation device |
| CN109549565A (en) * | 2018-12-03 | 2019-04-02 | 珠海格力电器股份有限公司 | Gas-dust separation mesh enclosure, gas-dust separation system and dust collector |
-
2009
- 2009-01-13 CN CNU2009200181410U patent/CN201366382Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104084322A (en) * | 2014-07-11 | 2014-10-08 | 江苏华泰重工装备有限公司 | Particle separation device |
| CN109549565A (en) * | 2018-12-03 | 2019-04-02 | 珠海格力电器股份有限公司 | Gas-dust separation mesh enclosure, gas-dust separation system and dust collector |
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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: 20091223 Termination date: 20120113 |