CN202087436U - Core separating type cyclone dust collector - Google Patents
Core separating type cyclone dust collector Download PDFInfo
- Publication number
- CN202087436U CN202087436U CN2011200006866U CN201120000686U CN202087436U CN 202087436 U CN202087436 U CN 202087436U CN 2011200006866 U CN2011200006866 U CN 2011200006866U CN 201120000686 U CN201120000686 U CN 201120000686U CN 202087436 U CN202087436 U CN 202087436U
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- separator
- core
- cyclone
- dust collector
- cyclone separator
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Abstract
The utility model relates to a dust collector, in particular to a core separating type cyclone dust collector, which comprises a fan and a circulating connecting pipe and is characterized in that the dust collector comprises a core separator and a cyclone separator which are connected through the connecting pipe, the core separator comprises a core separator inner cylinder and a core separator outer cylinder, and the cyclone separator comprises a cyclone separator outer cylinder and a cyclone separator inner cylinder. A screw conveyer is arranged under the core separator and the cyclone separator. The core separating type cyclone dust collector is novel in structure, low in pressure reduction, small in amplification effect, high in separating efficiency, low in energy consumption, resistant in high temperature, capable of meeting dust collecting requirements in different occasions better and more fine, low in investment and operating cost and wide in applied range, changes a gas flow path of traditional dust collectors, enables gas to be forcedly separated through a plurality of times of circulation, and achieves dust collecting efficiency of an electrostatic dust collector and a bag-type dust collector.
Description
Technical field
The utility model relates to a kind of deduster, is specifically related to a kind of core separate type cyclone dust collectors, is widely used in Industrial Boiler, civil boiler, and various kilns and stove are specially adapted to the kiln of cement production enterprise.
Background technology
In building material industry and various boiler, stove processing enterprise, traditional cyclone dust collectors are only through the first separation dedusting, wherein form along the limit wall from bottom to top with along the axle center top-down two eddy flows, the flow spiral angle is big.Have easily that eddy current, air-flow are wagged the tail, efficiency of dust collection not high (to capturing fine dust and the density of dust little dust of particle diameter less than 5 μ m, efficient is lower), the glide path of fluid is long, velocity gradient is big, so pressure drop is big, energy consumption height, poor stability.Though traditional cyclone dust collectors efficiency of dust collection is not high, but the advantage that mechanical gatherer is arranged: simple, reliable, compact, can control high solid concentration and relative low initial investment and maintenance cost, so the version of cyclone dust collectors is improved with suitable method, eddy current and secondary stream can be eliminated with other mechanical separator combination, just efficiency of dust collection can be improved greatly.
Summary of the invention
The purpose of this utility model is for overcoming above-mentioned the deficiencies in the prior art part, a kind of core separate type cyclone dust collectors are provided, this deduster includes blower fan, the circulation tube connector, described deduster includes core separator and is connected by tube connector with cyclone separator, and core separator is the container of column type, and a tangential import and two relative outlets are arranged, an outlet is used for row's cleaning gas, and another outlet connects the recycle gas outlet.The flue gas of solids laden thing is introduced the import of core separator by blower fan, because the result of swirling motion, particle is shifted to periphery from the centre, its center is right after the cleaning gas tream outlet, this zone does not cause eddy current and the secondary stream that particle returns, and the gas of cleaning leaves by outlet, carries particle periphery stream and is discharged to cyclone dust collectors, then, loop back core separator.It is independently to finish in different parts that separation process is collected with solids, core separator purifying gas flow, and the particle in the scavenge system, and particle can not leave system, but circulation again and again all harvests them up to cyclone collector.Two independently interactions between the parts make this system can obtain higher collection efficiency in this system.
The utility model is realized with following technical scheme: a kind of core separate type cyclone dust collectors, this deduster includes blower fan, the circulation tube connector, it is characterized in that: described deduster includes core separator and is connected by tube connector with cyclone separator, and described core separator includes core separator inner core, core separator urceolus; Described cyclone separator includes cyclone separator urceolus, cyclone separator inner core; Below described core separator and the cyclone separator conveying worm is arranged.
The core separator ash bucket is arranged at described core separator bottom, and first unloading valve is arranged on the core separator ash bucket; Radish is arranged at described cyclone separator bottom, and second unloading valve is arranged on the radish.
Described blower fan is connected with cyclone separator with core separator successively by the circulation tube connector.
The utility model has the advantages that: core separate type cyclone duster structure novelty, changed the gas flow path of traditional deduster, allow gas repeatedly circulate and strengthen separation, pressure drop is low, enlarge-effect is little, separative efficiency is high, energy consumption is low, high temperature resistant, the dedusting needs that can adapt to different occasions better finer and smoothlyer, reached the efficiency of dust collection of electrostatic precipitator and sack cleaner, and small investment, low, the applied range of operating cost.
Description of drawings
Below in conjunction with drawings and Examples the utility model is described in further detail:
Accompanying drawing is the utility model structural representation:
Among the figure: 1, blower fan, 2, the circulation tube connector, 3, core separator, 4, cyclone separator, 5, the core separator inner core, 6, the core separator urceolus, 7, core separator ash bucket, 8, first unloading valve, 9, conveying worm, 10, radish, 11, cyclone separator urceolus, 12, cyclone separator inner core, 13 tube connectors, 14, second unloading valve.
The specific embodiment
As shown in the figure: a kind of core separate type cyclone dust collectors, this deduster includes blower fan 1, circulation tube connector 2, described deduster includes core separator 3 and is connected by tube connector 13 with cyclone separator 4, and described core separator 3 includes core separator inner core 5, core separator urceolus 6; Described cyclone separator 4 includes cyclone separator urceolus 11, cyclone separator inner core 12; Below described core separator 3 and the cyclone separator 4 conveying worm 9 is arranged.
Core separator ash bucket 7 is arranged at described core separator 3 bottoms, and first unloading valve 8 is arranged on the core separator ash bucket; Radish 10 is arranged at described cyclone separator 4 bottoms, and second unloading valve 14 is arranged on the radish.
Described blower fan 1 is connected with cyclone separator 4 with core separator 3 successively by circulation tube connector 2.
The course of work: described deduster includes core separator and is connected by tube connector with cyclone separator, core separator is the container of column type, a tangential import and two relative outlets are arranged, and an outlet is used for row's cleaning gas, and another outlet connects the recycle gas outlet.The flue gas of solids laden thing is introduced the import of core separator by blower fan, because the result of swirling motion, particle is shifted to periphery from the centre, its center is right after the cleaning gas tream outlet, this zone does not cause eddy current and the secondary stream that particle returns, and the gas of cleaning leaves by outlet, carries particle periphery stream and is discharged to cyclone dust collectors, then, loop back core separator.It is independently to finish in different parts that separation process is collected with solids, core separator purifying gas flow, and the particle in the scavenge system, and particle can not leave system, but circulation again and again all harvests them up to cyclone collector.Two independently interactions between the parts make this system can obtain higher collection efficiency in this system.
Claims (3)
1. core separate type cyclone dust collectors, this deduster includes blower fan (1), circulation tube connector (2), it is characterized in that: described deduster includes core separator (3) and is connected by tube connector (13) with cyclone separator (4), and described core separator (3) includes core separator inner core (5), core separator urceolus (6); Described cyclone separator (4) includes cyclone separator urceolus (11), cyclone separator inner core (12); Below described core separator (3) and the cyclone separator (4) conveying worm (9) is arranged.
2. a kind of core separate type cyclone dust collectors according to claim 1 is characterized in that: core separator ash bucket (7) is arranged at described core separator (3) bottom, and first unloading valve (8) is arranged on the core separator ash bucket; Radish (10) is arranged at described cyclone separator (4) bottom, and second unloading valve (14) is arranged on the radish.
3. a kind of core separate type cyclone dust collectors according to claim 1 is characterized in that: described blower fan (1) is connected with cyclone separator (4) with core separator (3) successively by circulation tube connector (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200006866U CN202087436U (en) | 2011-01-04 | 2011-01-04 | Core separating type cyclone dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200006866U CN202087436U (en) | 2011-01-04 | 2011-01-04 | Core separating type cyclone dust collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202087436U true CN202087436U (en) | 2011-12-28 |
Family
ID=45362537
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200006866U Expired - Fee Related CN202087436U (en) | 2011-01-04 | 2011-01-04 | Core separating type cyclone dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202087436U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102580409A (en) * | 2012-03-14 | 2012-07-18 | 无锡光初科技服务有限公司 | Surface engineering rust removal air purification core separation system |
| CN103285995A (en) * | 2013-05-22 | 2013-09-11 | 南通三鑫重工机械有限公司 | Material grading method |
| CN109247013A (en) * | 2018-04-04 | 2019-01-18 | 太平洋工程株式会社 | Dispensing package |
-
2011
- 2011-01-04 CN CN2011200006866U patent/CN202087436U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102580409A (en) * | 2012-03-14 | 2012-07-18 | 无锡光初科技服务有限公司 | Surface engineering rust removal air purification core separation system |
| CN103285995A (en) * | 2013-05-22 | 2013-09-11 | 南通三鑫重工机械有限公司 | Material grading method |
| CN109247013A (en) * | 2018-04-04 | 2019-01-18 | 太平洋工程株式会社 | Dispensing package |
| CN109247013B (en) * | 2018-04-04 | 2021-07-16 | 太平洋工程株式会社 | Dispensing device |
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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: 20111228 Termination date: 20130104 |