CN206604548U - Pneumatic breaking sifter - Google Patents
Pneumatic breaking sifter Download PDFInfo
- Publication number
- CN206604548U CN206604548U CN201621309613.4U CN201621309613U CN206604548U CN 206604548 U CN206604548 U CN 206604548U CN 201621309613 U CN201621309613 U CN 201621309613U CN 206604548 U CN206604548 U CN 206604548U
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- cabin
- crushing shell
- pneumatic
- main cabin
- dental lamina
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Abstract
The utility model discloses a kind of pneumatic breaking sifter, including main cabin, secondary cabin, sieving plate, crushing shell and deflector, after ash and slagging enter main cabin from charging aperture, fine ash and slagging will be sized plate separation, fine ash enters the pump that puts in storage by sieving plate from discharging opening, slagging then enters secondary cabin, fall on crushing shell, it is broken through pneumatic breaker, slagging after broken is fallen on deflector through the gap on crushing shell, enter the pump that puts in storage from discharging opening, participate in conveying, this equipment safety is reliable, it is simple to operate, operation is convenient, solve the problems such as grey block of slagging can not convey the plugging of generation.
Description
【Technical field】
The utility model belongs to the lime-ash processing technology fields such as pulverized coal fired boiler, CFB fluidized-bed combustion boilers, gasification furnace, is related to
A kind of pneumatic breaking sifter.
【Background technology】
At present, the bottom ash of domestic boiler furnace bottom discharge needs to set two grades of slag crushers to break when using Geldart-D particle
Broken, the particle that the clinker of bulk is crushed into below 10mm could send into storehouse pump conveying.One-level slag crusher is rotated using double teeth roller
Engagement is broken, and two grades of slag crushers rotate attrition crushing using yankee roll.
Device has compared popularization at the Geldart-D particle of boiler back end ductwork ash discharge, but is due to that burner hearth coking etc. is various
Slagging is lumpd after flying dust solidification caused by reason in back-end ductwork, and Geldart-D particle can be allowed to occur plugging and the feelings such as can not convey
At condition, the dust stratification for especially occurring mainly in the equipment such as the economizer, air preheater, denitration of boiler, according to investigation, its agglomerate diameter is reachable
To 100mm.And boiler back end ductwork ash bucket ash discharge is when there is bulk, because slag crusher weight of equipment and volume are larger, it is impossible to
Economizer, air preheater, denitration ash bucket lower section are arranged in, it is general there is presently no the grey block after a set of effective method processing slagging
The bulk fallen into the pump of storehouse is carried out manual cleaning or set in storehouse pump ash tube to sieve all over storehouse pump manhole door is conveyed using opening
The modes such as the net bypass regular artificial treatment of bulk, easily cause the unsafe factors such as equipment fault and local pollution, particularly save coal
The ash bucket such as device, denitration ash discharge point is typically located at the region of boiler 20m~60m height, and the bulk lime-ash cleared needs people
Work is transported to zero meter, is required to carry above and below personnel daily, labor intensity is larger.
【Utility model content】
The utility model aims to overcome that the not enough there is provided the pneumatic breaking sifter of one kind of prior art,
The problem of flying dust air-transport system can not convey bulk lime-ash is fundamentally solved, coordinates pneumatic ash transmitting system, can be direct
Target bin is delivered to after lime-ash is crushed.
To reach above-mentioned purpose, the utility model patent, which is adopted the following technical scheme that, to be achieved：
Pneumatic breaking sifter, including main cabin, secondary cabin, sieving plate, crushing shell and deflector；Main cabin and secondary cabin
Room is arranged side by side, and main cabin upper end is that charging aperture, lower end are discharging openings, sieving plate be inclined at charging aperture and discharging opening it
Between, it is provided with above secondary cabin in the middle part of pneumatic breaker, secondary cabin and is provided with the crushing shell with hole, crushing shell is less than master
Secondary cabin is divided into upper bin and lower bin, upper bin and sieving plate in main cabin by the height of sieving plate in cabin, crushing shell
Top is connected, and lower bin is connected with the lower section of sieving plate in main cabin, and deflector is arranged in secondary cabin, under crushing shell
Side, deflector is obliquely installed to main cabin.
Further, the pneumatic breaker includes cylinder and dental lamina, and dental lamina is located at setting in parallel above crushing shell,
Cylinder and dental lamina are connected with shaft coupling, and wherein shaft coupling and cylinder are threaded connection, and shaft coupling and dental lamina are pin connection.
Further, the cylinder is provided with travel switch.
Further, the dental lamina is made of high hardness material.
Further, the sieving plate and crushing shell are processed using 12Mn plates.
The utility model includes main cabin, secondary cabin, sieving plate, crushing shell and deflector, when ash and slagging are from charging aperture
Into after main cabin, fine ash and slagging will be sized plate separation, and fine ash enters the pump that puts in storage by sieving plate from discharging opening, and slagging is then
Into secondary cabin, fall on crushing shell, broken through pneumatic breaker, the slagging after crushing is fallen on through the gap on crushing shell to be led
Flow on plate, the pump that puts in storage is entered from discharging opening, participate in conveying, this equipment safety is reliable, simple to operate, and operation is convenient, solves slagging
The problems such as grey block can not convey the plugging of generation.
Pneumatic breaking sifter is used to handle the lime-ash containing larger influence induction system operation in conveying material
Grain.The equipment normal work and should be able to ensure the stabilization of its mechanical structure and durable under severe operating mode.Its principle is to utilize
The grain sorting that baffle plate in sifter will be greater than certain diameter comes out, and delivers in crushing mechanism, broken using physical impact
Mode the lime-ash of bulky grain is broken into the little particle lime-ash that disclosure satisfy that conveying is required, then delivery system is entered by cylinder manifold
In system.
【Brief description of the drawings】
Fig. 1 is structural representation of the present utility model；
In figure：Main cabin 1, secondary cabin 2, charging aperture 3, discharging opening 4, sieving plate 5, crushing shell 6, dental lamina 7, deflector 8, connection
Axle device 9, cylinder 10.
【Embodiment】
The utility model is described in further detail below in conjunction with the accompanying drawings.
As shown in figure 1, pneumatic breaking sifter is made up of main cabin 1 and secondary cabin 2, main cabin 1 and secondary cabin 2 are independent
Work, is arranged side by side, is independent of each other, and main cabin 1 allows the fine ash less than screen cloth grid directly to pass through, and secondary 2 pairs of cabin is more than sieve
The grey solid impurity particle of net grid is crushed.The main upper end of cabin 1 is that charging aperture 3, lower end are discharging openings 4, and sieving plate 5 is inclined at
Between charging aperture 3 and discharging opening 4, the screen cloth grid that sieving plate 5 is provided with can be sieved to lime-ash, and sieving plate 5 simultaneously will be big
Block lime-ash is guided on the crushing shell 6 in secondary cabin 2.
The secondary top of cabin 2 is provided with pneumatic breaker, and the secondary middle part of cabin 2 is provided with the crushing shell 6 with hole, crushed
Plate 6 is less than the height of sieving plate 5 in main cabin 1, and 2 points of secondary cabin is upper bin and lower bin by crushing shell 6, upper bin and main cabin
The top connection of sieving plate 5 in room 1, lower bin is connected with the lower section of sieving plate 5 in main cabin 1, and deflector 8 is arranged on secondary cabin
In 2, positioned at the lower section of crushing shell 6, deflector 8 is obliquely installed to main cabin 1.Crushing shell 6 will can not only break lime-ash with dental lamina 7
It is broken, while to ensure compliance with the ash of transport condition can just fall on deflector 8.
The pneumatic breaker includes cylinder 10 and dental lamina 7, and dental lamina 7 is located at the setting in parallel of the top of crushing shell 6, gas
Cylinder 10 and dental lamina 7 are connected with shaft coupling 9, and wherein shaft coupling 9 and cylinder 10 are threaded connection, and shaft coupling 9 and dental lamina are pin connection.
The cylinder 10 is provided with travel switch, and signal delivers to Geldart-D particle control system, travel switch monitoring dental lamina 7
Put, when generation dental lamina 7 is failure to actuate or can not acted in place, send fault alarm.
The dental lamina 7 is made of high hardness material, and sieving plate 5 is processed using 12Mn plates, and sieving plate intensity is high, energy
It is indeformable to the impulsive force of main grey block；, crushing shell 6 also uses 12Mn plate machine-shapings, and intensity has absolute guarantee.Dental lamina 7 is used
The type of drive of cylinder 10, drive dental lamina about 7 straight reciprocating motion crushed.The stroke of cylinder 10 whether in place, by stroke
Switch is monitored, when breaking down, and signal can be timely fed back to program.
After ash and slagging enter main cabin from charging aperture 3, fine ash and slagging will be sized plate 5 and separate, and fine ash is passed through
Sieving plate enters the pump that puts in storage from discharging opening 4, and slagging then enters secondary cabin, fallen on crushing shell 6.Now, cylinder 10 drive dental lamina 7 to
Lower extruding, slagging is crushed.After being pressed into place, travel switch sends signal, and one travel switch of every cylinder, cylinder is withdrawn,
Into next working cycles.Cylinder and dental lamina shaft coupling 9 are connected, and wherein shaft coupling and cylinder are to be threadedly coupled, and dental lamina
For pin connection.Slagging after broken is fallen on deflector 8 through the gap on crushing shell, and the pump that puts in storage is entered from discharging opening, participates in conveying.
In control aspect, cylinder is furnished with travel switch, and signal is delivered in Geldart-D particle control system, travel switch monitoring tooth
Board position, when generation dental lamina 7 is failure to actuate or can not acted in place, can all send fault alarm.Dental lamina 7 is run all by journey
Sequence is controlled, and realizes full-automatic work.
It is that system is safe and reliable using the advantage of this equipment, operation is convenient, and caused plugging can not be conveyed by solving lime-ash
Situation, at the same without specially be lime-ash the problem of arrange work personnel exclude lime-ash manually the problem of.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements done etc. should be included in the utility model
Within the scope of.
Claims (5)
1. pneumatic breaking sifter, it is characterised in that：Including main cabin (1), secondary cabin (2), sieving plate (5), crushing shell (6)
With deflector (8)；
Main cabin (1) and secondary cabin (2) are arranged side by side, and main cabin (1) upper end is that charging aperture (3), lower end are discharging opening (4), sieve
Divide plate (5) to be inclined between charging aperture (3) and discharging opening (4), pneumatic breaker is provided with above secondary cabin (2), it is secondary
The crushing shell (6) with hole is provided with the middle part of cabin (2), crushing shell (6) is less than the height of sieving plate (5) in main cabin (1),
Secondary cabin (2) are divided into upper bin and lower bin by crushing shell (6), and upper bin in main cabin (1) above sieving plate (5) with connecting
Logical, lower bin is connected with the lower section of sieving plate (5) in main cabin (1), and deflector (8) is arranged in secondary cabin (2), positioned at broken
Below plate (6), deflector (8) is obliquely installed to main cabin (1).
2. pneumatic breaking sifter according to claim 1, it is characterised in that：The pneumatic breaker includes cylinder
(10) and dental lamina (7), dental lamina (7) be located at it is in parallel above crushing shell (6) set, cylinder (10) and dental lamina (7) use shaft coupling
(9) connect, wherein shaft coupling (9) and cylinder (10) are threaded connection, shaft coupling (9) and dental lamina are pin connection.
3. pneumatic breaking sifter according to claim 2, it is characterised in that：The cylinder (10) is provided with stroke and opened
Close.
4. pneumatic breaking sifter according to claim 2, it is characterised in that：The dental lamina (7) uses high rigidity material
Material is made.
5. the pneumatic breaking sifter according to claim 1,2 or 3, it is characterised in that：The sieving plate (5) and broken
Plate (6) is processed using 12Mn plates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621309613.4U CN206604548U (en) | 2016-11-30 | 2016-11-30 | Pneumatic breaking sifter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621309613.4U CN206604548U (en) | 2016-11-30 | 2016-11-30 | Pneumatic breaking sifter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206604548U true CN206604548U (en) | 2017-11-03 |
Family
ID=60172182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621309613.4U Active CN206604548U (en) | 2016-11-30 | 2016-11-30 | Pneumatic breaking sifter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206604548U (en) |
-
2016
- 2016-11-30 CN CN201621309613.4U patent/CN206604548U/en active Active
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