CN202555111U - Automatically-controlled pulse-type dust removal system - Google Patents
Automatically-controlled pulse-type dust removal system Download PDFInfo
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- CN202555111U CN202555111U CN2012202114094U CN201220211409U CN202555111U CN 202555111 U CN202555111 U CN 202555111U CN 2012202114094 U CN2012202114094 U CN 2012202114094U CN 201220211409 U CN201220211409 U CN 201220211409U CN 202555111 U CN202555111 U CN 202555111U
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- dust
- tracheae
- automatic control
- dust removal
- compressed air
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Abstract
The utility model discloses an automatically-controlled pulse-type dust removal system. The automatically-controlled pulse-type dust removal system mainly comprises a dust air inlet pipe, a dust collector, an air passing pipe and a purified air outlet pipe. A pulse-type compressed air inlet pipe is arranged inside the air passing pipe. One end of the pulse-type compressed air inlet pipe extends into the dust collector and the other end of the pulse-type compressed air inlet pipe is connected with an air compression machine. The automatically-controlled pulse-type dust removal system has the advantages of simple structure, good dust removal effect, low energy consumption and low production cost.
Description
Technical field
The utility model relates to dust pelletizing system, specifically is meant automatic control impuls formula dust pelletizing system.
Background technology
Deduster is that the equipment from flue gas, separated dust is deduster or cleaner.The performance of deduster with accessible gas flow, gas drag losses and the efficiency of dust collection during through deduster express.Simultaneously, the price of deduster, operation and maintenance cost, service life length and operational administrative difficulty or ease also be to consider the key factor of its performance.Purposes is that deduster is a facility commonly used in boiler and the commercial production.
Deduster is divided into following five types by its action principle.
(1) mechanical precipitator comprises gravitational precipitator, inertial dust separator, centrifugal deduster etc.
(2) the washing type deduster comprises water-bath type dust cleaner, foam type deduster, venturi tube duster, water film type duster etc.
(3) filtration dust catcher comprises sack cleaner and gravel bed filter etc.
(4) electrostatic precipitator.
(5) magnetic dust collector.
Use in the industry now many be electric bag compound type dust remover and sack cleaner.
Electric bag combined dedusting technology.Electric-bag complex dust collector is promptly in a casing, and front end is installed a short electric field, and the filter bag field is installed in the rear end, and flue dust is introduced from left end, at first passes through electric field region, and grit is charged and have 80% ~ 90% dust to be collected at electric field region.(advantage of performance electric precipitation reduces a bag load).Flue gas through electric field is partly distinguished through getting into bag behind the electric field region, gets into the filter bag inner chamber through the filter bag outer surface, and dust is delayed at the filter bag outer surface, and pure gas is discharged from flue from the inner chamber exhaust uptake.Electric bag compound type dust remover has combined electric cleaner and both advantages of pure sack cleaner; It is the dedusting technology of a new generation; Domestic Fujian Longjing Environment Protection Co., Ltd has realized first commercial Application in 2002, at present domestic total 200 electric bag compound type dust remover nearly comes into operation.
Description in foregoing, the complex structure of various dedusters uses input cost high in market, and its energy waste is serious.For this reason we need design a kind of simple in structure, good dedusting effect.Energy resource consumption is low, the dust pelletizing system that production cost is low.
The utility model content
It is a kind of simple in structure that the purpose of the utility model is to provide, good dedusting effect.Energy resource consumption is low, the automatic control impuls formula dust pelletizing system that production cost is low.
The implementation of the utility model is following: automatic control impuls formula dust pelletizing system; Mainly constitute by the dirt gas air inlet pipe that connects successively, dust removal machine, mistake tracheae, pure qi (oxygen) escape pipe; The said tracheae inside of crossing also is provided with pulsed compressed air and crosses tracheae, and said pulsed compressed air crosses that tracheae one end extends into dust removal machine inside, the other end is connected with air compressor.
Said dust removal machine comprises support body and is arranged on the dust cleaning case on the support body, and said dust cleaning case mainly is made up of outlet chamber, overcurrent chamber, dust hopper, and said outlet chamber is arranged on top, overcurrent chamber, and said overcurrent chamber is arranged on the dust hopper top.
Said overcurrent chamber set inside has some filter cylinders, and two end faces of said filter cylinder are respectively towards outlet chamber and dust hopper.
Said filter cylinder is closed end face near the end face of dust hopper, and said filter cylinder is the open type end face near the end face of crossing outlet chamber.
Said pulsed compressed air is crossed the inside that a end that tracheae extends into dust removal machine is positioned at outlet chamber, and said pulsed compressed air crosses tracheae and also be connected with some gas branch pipes that go out, and said some gas outlets that go out gas branch pipe are positioned at directly over the filter cylinder.
Said air compressor is connected with automatic controller.
Distance between said adjacent two filter cylinders is 10mm-100mm.
In the utility model; The gas that has dust gets into from dirt gas air inlet pipe; And entering into dust removal machine inside, the position of dirty air between adjacent two filter cylinders gets into cartridge interior, under the filter cylinder effect; Dust particle is attracted to cartridge exine, purified gas through cartridge interior flow through outlet chamber, cross tracheae, the pure qi (oxygen) escape pipe is discharged from.
After the dust removal machine work regular hour; Automatic controller sends instruction; Air after making the air compressor discharging compress; Compressed air is crossed tracheae and is gone out gas branch pipe and spurted into cartridge interior through pulsed compressed air, and the dust particle that under compressed-air actuated effect, is adsorbed on cartridge exine is by the cartridge exine that blows off, and drops and enter into dust hopper.
The advantage of the utility model is: simple in structure, and good dedusting effect.Energy resource consumption is low, and production cost is low.
Description of drawings
Fig. 1 is the utility model overall structure sketch map.
Label among the figure is expressed as respectively: 1, dirt gas air inlet pipe; 2, dust removal machine; 8, cross tracheae; 9, pure qi (oxygen) escape pipe; 7, pulsed compressed air is crossed tracheae; 10, air compressor; 3, outlet chamber; , 6, the overcurrent chamber; , 4, dust hopper; 5, filter cylinder; 11, automatic controller.
The specific embodiment
Embodiment one
As shown in Figure 1.
Automatic control impuls formula dust pelletizing system; Mainly constitute by the dirt gas air inlet pipe 1 that connects successively, dust removal machine 2, mistake tracheae 8, pure qi (oxygen) escape pipe 9; Said tracheae 8 inside of crossing also are provided with pulsed compressed air and cross tracheae 7, and said pulsed compressed air crosses that tracheae 7 one ends extend into dust removal machine 2 inside, the other end is connected with air compressor 10.
Said dust removal machine 2 comprises support body and is arranged on the dust cleaning case on the support body, and said dust cleaning case mainly is made up of outlet chamber 3, overcurrent chamber 6, dust hopper 4, and said outlet chamber 3 is arranged on 6 tops, overcurrent chamber, and said overcurrent chamber 6 is arranged on dust hopper 4 tops.
Said overcurrent chamber 6 set inside have some filter cylinders 5, and two end faces of said filter cylinder 5 are respectively towards outlet chamber 3 and dust hopper 4.
Said filter cylinder 5 is closed end face near the end face of dust hopper 4, and said filter cylinder 5 is the open type end face near the end face of crossing outlet chamber 3.
Said pulsed compressed air is crossed the end that tracheae 7 extends into dust removal machine 2 and is positioned at outlet chamber 3 inside, and said pulsed compressed air crosses tracheae 7 and also be connected with some gas branch pipes that go out, and said some gas outlets that go out gas branch pipe are positioned at directly over the filter cylinder 5.
Said air compressor 10 is connected with automatic controller 11.
Distance between said adjacent two filter cylinders 5 is 10mm-100mm.
In the utility model; The gas that has dust gets into from dirt gas air inlet pipe 1; And entering into dust removal machine 2 inside, the position of dirty air between adjacent two filter cylinders 5 gets into filter cylinder 5 inside, under filter cylinder 5 effects; Dust particle is attracted to filter cylinder 5 outer walls, purified gas flow through through cartridge filter 5 inside outlet chamber 3, cross tracheae 8, pure qi (oxygen) escape pipe 9 is discharged from.
After dust removal machine 2 is worked the regular hours; Automatic controller 11 sends instruction; Air after making air compressor 10 dischargings compress; Compressed air is crossed tracheae 7 and is gone out gas branch pipe and spurted into filter cylinder 5 inside through pulsed compressed air, the dust particle that under compressed-air actuated effect, is adsorbed on filter cylinder 5 outer walls filter cylinder 5 outer walls that blown off, and drop and enter into dust hopper 4.
As stated, then can well realize the utility model.
Claims (7)
1. automatic control impuls formula dust pelletizing system; It is characterized in that: mainly constitute by the dirt gas air inlet pipe (1) that connects successively, dust removal machine (2), mistake tracheae (8), pure qi (oxygen) escape pipe (9); Said tracheae (8) inside of crossing also is provided with pulsed compressed air and crosses tracheae (7), and said pulsed compressed air is crossed tracheae (7) one ends and extended into that dust removal machine (2) is inner, the other end is connected with air compressor (10).
2. automatic control impuls formula dust pelletizing system according to claim 1; It is characterized in that: said dust removal machine (2) comprises support body and is arranged on the dust cleaning case on the support body; Said dust cleaning case mainly is made up of outlet chamber (3), overcurrent chamber (6), dust hopper (4); And said outlet chamber (3) is arranged on top, overcurrent chamber (6), and said overcurrent chamber (6) is arranged on dust hopper (4) top.
3. automatic control impuls formula dust pelletizing system according to claim 2 is characterized in that: said overcurrent chamber (6) set inside has some filter cylinders (5), and two end faces of said filter cylinder (5) are respectively towards outlet chamber (3) and dust hopper (4).
4. automatic control impuls formula dust pelletizing system according to claim 3 is characterized in that: said filter cylinder (5) is closed end face near the end face of dust hopper (4), and said filter cylinder (5) is the open type end face near the end face of crossing outlet chamber (3).
5. according to claim 3 or 4 described automatic control impuls formula dust pelletizing systems; It is characterized in that: said pulsed compressed air is crossed the end that tracheae (7) extends into dust removal machine (2) and is positioned at outlet chamber (3) inside; And said pulsed compressed air is crossed tracheae (7) and also is connected with some gas branch pipes that go out, and said some gas outlets that go out gas branch pipe are positioned at directly over the filter cylinder (5).
6. automatic control impuls formula dust pelletizing system according to claim 5, it is characterized in that: said air compressor (10) is connected with automatic controller (11).
7. automatic control impuls formula dust pelletizing system according to claim 5, it is characterized in that: the distance between said adjacent two filter cylinders (5) is 10mm-100mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012202114094U CN202555111U (en) | 2012-05-11 | 2012-05-11 | Automatically-controlled pulse-type dust removal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012202114094U CN202555111U (en) | 2012-05-11 | 2012-05-11 | Automatically-controlled pulse-type dust removal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202555111U true CN202555111U (en) | 2012-11-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012202114094U Expired - Fee Related CN202555111U (en) | 2012-05-11 | 2012-05-11 | Automatically-controlled pulse-type dust removal system |
Country Status (1)
| Country | Link |
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| CN (1) | CN202555111U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386235A (en) * | 2012-05-11 | 2013-11-13 | 四川优的科技有限公司 | Automatic control pulse type dedusting system |
| CN103463896A (en) * | 2013-09-09 | 2013-12-25 | 佛山市人居环保工程有限公司 | Dust collector with dust layer having controllable thickness, sorting property and continuity and operation method thereof |
| CN103830979A (en) * | 2014-02-25 | 2014-06-04 | 中国矿业大学 | Integrated control system and integrated control method for mining dry dust remover |
| CN106512594A (en) * | 2016-10-08 | 2017-03-22 | 南昌大学 | Filter type dust removal system teaching demonstration experimental platform |
-
2012
- 2012-05-11 CN CN2012202114094U patent/CN202555111U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386235A (en) * | 2012-05-11 | 2013-11-13 | 四川优的科技有限公司 | Automatic control pulse type dedusting system |
| CN103463896A (en) * | 2013-09-09 | 2013-12-25 | 佛山市人居环保工程有限公司 | Dust collector with dust layer having controllable thickness, sorting property and continuity and operation method thereof |
| CN103463896B (en) * | 2013-09-09 | 2016-01-27 | 佛山市人居环保工程有限公司 | A kind of long-pending rack-layer thickness is controlled, sorting, continuous print deduster method of operating |
| CN103830979A (en) * | 2014-02-25 | 2014-06-04 | 中国矿业大学 | Integrated control system and integrated control method for mining dry dust remover |
| CN106512594A (en) * | 2016-10-08 | 2017-03-22 | 南昌大学 | Filter type dust removal system teaching demonstration experimental platform |
| CN106512594B (en) * | 2016-10-08 | 2018-09-25 | 南昌大学 | A kind of filtering type dust pelletizing system teaching demonstration experiment porch |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: SICHUAN RUITENG ELECTRONICS CO., LTD. Assignor: Sichuan Youdi Science & Technology Co., Ltd. Contract record no.: 2012510000195 Denomination of utility model: Automatic control pulse type dedusting system Granted publication date: 20121128 License type: Exclusive License Record date: 20121226 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121128 Termination date: 20140511 |