CN107398323A - A kind of pneumatic breaking sifter - Google Patents
A kind of pneumatic breaking sifter Download PDFInfo
- Publication number
- CN107398323A CN107398323A CN201710776191.4A CN201710776191A CN107398323A CN 107398323 A CN107398323 A CN 107398323A CN 201710776191 A CN201710776191 A CN 201710776191A CN 107398323 A CN107398323 A CN 107398323A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- casing
- ash
- sifter
- sieving plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000007873 sieving Methods 0.000 claims abstract description 30
- 238000012856 packing Methods 0.000 claims description 11
- 239000004744 fabric Substances 0.000 claims description 8
- 238000012216 screening Methods 0.000 claims description 8
- 239000002893 slag Substances 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 6
- 239000010959 steel Substances 0.000 claims description 6
- 241000761557 Lamina Species 0.000 claims description 5
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 239000002245 particle Substances 0.000 abstract description 12
- 239000000463 material Substances 0.000 abstract description 11
- 230000001360 synchronised effect Effects 0.000 abstract description 3
- 238000009825 accumulation Methods 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract description 2
- 230000003245 working effect Effects 0.000 abstract description 2
- 239000002956 ash Substances 0.000 description 28
- 239000000428 dust Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001033 granulometry Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 239000010882 bottom ash Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C1/00—Crushing or disintegrating by reciprocating members
- B02C1/005—Crushing or disintegrating by reciprocating members hydraulically or pneumatically operated
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
- B02C2023/165—Screen denying egress of oversize material
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Disintegrating Or Milling (AREA)
Abstract
The present invention discloses a kind of pneumatic breaking sifter, including casing, cylinder, air cylinder support, dental lamina and sieving plate;First fine ash and the mixture of slagging are separated with sieving plate, two dental lamina synchronous workings will need broken material attrition crushing, the bulk lime-ash for being not easy Geldart-D particle participates in conveying after crushing again, all materials into below sieving plate can be pooled to sifter outlet by deflector, the situation of solid accumulation will not be formed, it is of the invention safe and reliable, it is simple to operate, operation is convenient, solves the problems such as slagging ash block can not convey the plugging of generation, coordinate pneumatic ash transmitting system, target bin is delivered to after can directly lime-ash be crushed.
Description
Technical field
The invention belongs to lime-ash processing technology fields such as pulverized coal fired boiler, CFB fluidized-bed combustion boilers, gasification furnaces, it is related to firepower
Power plant or coal-burning boiler power station, the residue treatment plant of power houses, more particularly to a kind of pneumatic breaking sifter.
Background technology
At present, the bottom ash of domestic boiler furnace bottom discharge needs to set two level slag crusher to break when using Geldart-D particle
Broken, the clinker of bulk is crushed to below 10mm particle could be sent into storehouse pump conveying.One-level slag crusher is rotated using double teeth roller
Engagement is broken, and two level slag crusher rotates attrition crushing using yankee roll.
Device has compared popularization at the Geldart-D particle of boiler back end ductwork ash discharge, but because burner hearth coking etc. is various
Slagging is lumpd after flying dust solidification in back-end ductwork caused by reason, can be allowed Geldart-D particle that plugging occurs and the feelings such as can not be conveyed
Condition, it is reachable according to investigation, its agglomerate diameter at the dust stratification for especially occurring mainly in the equipment such as the economizer, air preheater, denitration of boiler
To 100mm., can not because slag crusher weight of equipment and volume are larger and boiler back end ductwork ash bucket ash discharge is when there is bulk
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 using opening conveying storehouse pump manhole door
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 personnel daily and carries up and down, labor intensity is larger.
The content of the invention
To solve the defects of prior art is present, present invention aims at a kind of pneumatic breaking sifter is provided, solve
The defects of plugging easily occurs for bulk particle when Dual-Phrase Distribution of Gas olid conveys, crushes to thermal power plant slagging ash block, reaches it
To the method for Geldart-D particle requirement.
To reach above-mentioned purpose, the present invention, which adopts the following technical scheme that, to be achieved:
A kind of pneumatic breaking sifter, including casing, cylinder, air cylinder support, dental lamina and sieving plate;
Casing upper and lower opens up lime-ash inlet and outlet respectively, and sieving plate is horizontally set in casing, and two cylinders pass through cylinder
Support is arranged on the relative both sides of casing external position, two pieces of dental laminas for being used for crashing steel (iron) slag block are oppositely arranged in casing,
On sieving plate, each dental lamina is connected by the stroke shaft through wall box with a cylinder, and work is driven by cylinder
Make, the lime-ash outlet port below casing is provided with the deflector being obliquely installed.
Further, the position of stroke shaft through casing is provided with seal disc, and packing sleeve, packing are provided with the outside of seal disc
Sleeve is used to support stroke shaft, and packing cartridge exterior is additionally provided with closure.
Further, stroke shaft is provided with cloth bag sleeve with dental lamina link position and stroke shaft with seal disc link position.
Further, in addition to PLC control system, the extreme position of each cylinder moving are provided with travel switch, work as generation
When cylinder is failure to actuate or can not acted in place, signal can be timely fed back to PLC control system.
Further, stroke shaft is connected with cylinder by spacing shaft joint, and spacing shaft joint and cylinder are threaded connection, spacing
Shaft joint and stroke shaft are pin connection.
Further, the screening board mount of two triangles is installed, sieving plate is arranged on by sieving board mount in casing
Casing lime-ash outlet top, two deflectors are separately mounted on two screening board mounts.
Further, cylinder is fixed on air cylinder support by cylinder foot stool.
Further, sieving plate is added using 12Mn steel plates and formed.
Further, casing is not provided with offering manhole in a side wall of cylinder.
The pneumatic breaking sifter of the present invention, including casing, cylinder, air cylinder support, dental lamina and sieving plate;First by fine ash
Separated with the mixture of slagging with sieving plate, two dental lamina synchronous workings will need broken material attrition crushing, be not easy strength
The bulk lime-ash of conveying is participated in conveying after crushing again, and all materials into below sieving plate can be pooled to screening by deflector
Device exports, and will not form the situation of solid accumulation, and the present invention is safe and reliable, simple to operate, and operation is convenient, solves slagging ash block
The problems such as plugging of generation can not be conveyed, coordinate pneumatic ash transmitting system, target bin is delivered to after can directly lime-ash be crushed.
Further, stroke shaft is provided with cloth bag sleeve, cloth with dental lamina link position and stroke shaft with seal disc link position
Equipped with sealing cloth bag on bag sleeve, sealing cloth bag is flexible connection, the dust that can be leaked is isolated, sealing means simply may be used
Lean on, practical, convertibility is good.
Further, in place whether the stroke of cylinder, be monitored signal by travel switch and deliver to Geldart-D particle control system,
Line position monitoring switch dental lamina position, when dental lamina occurs being failure to actuate or can not act in place, send fault alarm, signal energy and
When feed back to program;When cylinder has situation about excessively walking to occur, spacing shaft joint can protect dental lamina, not allow it that steel occurs
Property extruding.
Further, manhole is offered in one side wall of casing, equipment facilitates maintainer to enter internal examine when breaking down
Repair.
Brief description of the drawings
Fig. 1 is the structural representation of apparatus of the present invention;
In figure:1- casings, 2- seal discs, 3- packings sleeve, 4- closures, 5- stroke shafts, the spacing shaft joints of 6-, 7- gas
Cylinder, 8- cylinders foot stool, 9- air cylinder supports, 10- cloth bags sleeve, 11- dental laminas, 12- sieving plates, 13- screening board mount, 14- packings,
15- manholes, 16- deflectors.
Embodiment
With reference to the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Description, embodiment described herein is only the part of the embodiment of the present invention, and not all embodiment.Based on this hair
Embodiment in bright, the every other embodiment that those of ordinary skill in the art are obtained under the premise of no creative work,
Belong to the scope of the present invention.
As shown in figure 1, the pneumatic breaking sifter of the present invention includes casing 1, cylinder 7, air cylinder support 9, the and of dental lamina 11
Sieving plate 12.
The upper and lower of casing 1 opens up lime-ash inlet and outlet respectively, and sieving plate 12 is horizontally set in casing 1, and two cylinders 7 are logical
Cross air cylinder support 9 and be oppositely arranged installation installed in the relative both sides of the external position of casing 1, two pieces of dental laminas 11 for being used for crashing steel (iron) slag block
In casing 1, on sieving plate 12, each dental lamina 11 is connected by the stroke shaft 5 through the side wall of casing 1 and a cylinder 7
Connect, work is driven by cylinder, the lime-ash outlet port of the lower section of casing 1 is provided with the deflector 16 being obliquely installed.
The position of stroke shaft 5 through casing 1 is provided with seal disc 2, and the outside of seal disc 2 is provided with packing sleeve 3, packing set
Cylinder 3 is used to support stroke shaft 5, and closure 4 is additionally provided with outside packing sleeve 3.Stroke shaft 5 and the link position of dental lamina 11 and stroke shaft
5 are provided with cloth bag sleeve 10 with the link position of seal disc 2.
After ash and slagging enter chamber from charging aperture, fine ash and slagging will be sized plate 12 and separate, and sieving plate is used
12Mn plates are process, and intensity is high, can prop up the impulsive force of grey block and indeformable.Fine ash is entered to put in storage by sieving plate from discharging opening
Pump, slagging are then stayed on sieving plate 12, and now, cylinder 7 drives the synchronous extruding of dental lamina 11, and slagging is crushed.After being pressed into place, OK
Cheng Kaiguan sends signal, and one travel switch of every cylinder, cylinder is withdrawn, into next working cycles.
Further, in addition to PLC control system, the extreme position that each cylinder 7 moves are provided with travel switch, work as generation
When cylinder 7 is failure to actuate or can not acted in place, signal can be timely fed back to PLC control system.
Further, stroke shaft 5 is connected with cylinder 7 by spacing shaft joint 6, and spacing shaft joint 6 and cylinder are threaded connection,
Spacing shaft joint 6 and stroke shaft 5 are pin connection.The gap on the screened plate 12 of slagging after broken is fallen on deflector 16, from
Discharging opening enters the pump that puts in storage, and participates in conveying.
Further, the screening board mount 13 of two triangles is installed, sieving plate 12 is by sieving board mount 13 in casing 1
Top is exported installed in the lime-ash of casing 1, two deflectors 16 are separately mounted on two screening board mounts 13.Cylinder 7 passes through gas
Cylinder foot stool 8 is fixed on air cylinder support 9.
Cylinder and dental lamina are connected with spacing shaft joint 6, wherein spacing shaft joint and cylinder are threaded connection, and dental lamina is pin
Connection.
Further, casing 1 is not provided with offering manhole 15 in a side wall of cylinder 7.
In control aspect, cylinder switchs equipped with line position, and signal enters in Geldart-D particle PLC control system, may participate in whole
In individual induction system.Meanwhile line position monitoring switch dental lamina position, when such as generation dental lamina is failure to actuate or can not acted in place, all
Fault alarm can be sent, operation is all controlled by PLC, while solving lime-ash, realizes full-automatic work.
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 11 is failure to actuate or can not acted in place, it can all send fault alarm.Dental lamina 11 run all by
Programme-control, realize full-automatic work.
The course of work of the present invention is:
A) first the material for entering pneumatic breaking sifter is sieved, separates its thickness material;
B) the screened plate 12 of material for being not up to Geldart-D particle granulometry separates, and sieving plate works independently, and is served only for sieving
Point, it would be desirable to broken material is stayed on sieving plate.Two dental laminas 11 work asynchronously, it would be desirable to broken material attrition crushing.
C) all materials into the lower section of deflector 16 of slagging after crushing are pooled to sifter outlet;
D) material for reaching Geldart-D particle granulometry is directly entered storehouse pump;
It is that system is safe and reliable using the advantages 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.
Above example is merely to illustrate technical scheme rather than its limitations, although with reference to above-described embodiment pair
The present invention is described in detail, and those of ordinary skill in the art can still be carried out to specific embodiments of the present invention
Modification or equivalent substitution, and these are without departing from any modification of spirit and scope of the invention or equivalent substitution, it exists
Within the claims of the present invention.
Claims (9)
- A kind of 1. pneumatic breaking sifter, it is characterised in that:Including casing (1), cylinder (7), air cylinder support (9), dental lamina And sieving plate (12) (11);Casing (1) upper and lower opens up lime-ash inlet and outlet respectively, and sieving plate (12) is horizontally set in casing (1), two cylinders (7) the relative both sides of casing (1) external position, two pieces of dental laminas (11) for being used for crashing steel (iron) slag block are arranged on by air cylinder support (9) It is oppositely arranged in the casing (1), on sieving plate (12), each dental lamina (11) is by through casing (1) side wall Stroke shaft (5) is connected with a cylinder (7), and by cylinder driving work, the lime-ash outlet port below casing (1), which is provided with, inclines The deflector (16) tiltedly set.
- A kind of 2. pneumatic breaking sifter according to claim 1, it is characterised in that:Stroke shaft (5) passes through casing (1) Position be provided with seal disc (2), packing sleeve (3) is installed, packing sleeve (3) is used to support stroke on the outside of seal disc (2) Axle (5), packing sleeve (3) is outside to be additionally provided with closure (4).
- A kind of 3. pneumatic breaking sifter according to claim 2, it is characterised in that:Stroke shaft (5) and dental lamina (11) Link position and stroke shaft (5) are provided with cloth bag sleeve (10) with seal disc (2) link position.
- A kind of 4. pneumatic breaking sifter according to claim any one of 1-3, it is characterised in that:Also include PLC to control System processed, the extreme position of each cylinder (7) motion is provided with travel switch, when generation cylinder (7) is failure to actuate or can not be moved When making in place, signal can be timely fed back to PLC control system.
- A kind of 5. pneumatic breaking sifter according to claim any one of 1-3, it is characterised in that:Stroke shaft (5) with Cylinder (7) is connected by spacing shaft joint (6), and spacing shaft joint (6) and cylinder are threaded connection, spacing shaft joint (6) and row Journey axle (5) is pin connection.
- A kind of 6. pneumatic breaking sifter according to claim any one of 1-3, it is characterised in that:Pacify in casing (1) Screening board mount (13) equipped with two triangles, sieving plate (12) are arranged on casing (1) lime-ash by sieving board mount (13) Outlet top, two deflectors (16) are separately mounted on two screening board mounts (13).
- A kind of 7. pneumatic breaking sifter according to claim any one of 1-3, it is characterised in that:Cylinder (7) passes through Cylinder foot stool (8) is fixed on air cylinder support (9).
- A kind of 8. pneumatic breaking sifter according to claim any one of 1-3, it is characterised in that:Sieving plate (12) is adopted Added with 12Mn steel plates and formed.
- A kind of 9. pneumatic breaking sifter according to claim any one of 1-3, it is characterised in that:Casing (1) is not set Put and manhole (15) is offered in a side wall of cylinder (7).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710776191.4A CN107398323A (en) | 2017-08-31 | 2017-08-31 | A kind of pneumatic breaking sifter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710776191.4A CN107398323A (en) | 2017-08-31 | 2017-08-31 | A kind of pneumatic breaking sifter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107398323A true CN107398323A (en) | 2017-11-28 |
Family
ID=60397995
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710776191.4A Pending CN107398323A (en) | 2017-08-31 | 2017-08-31 | A kind of pneumatic breaking sifter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107398323A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115532351A (en) * | 2022-11-15 | 2022-12-30 | 涿州市烽合机械设备有限公司 | Vibration screening device for coal ash conveying and working method thereof |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2193329A5 (en) * | 1972-07-21 | 1974-02-15 | Nicolas Jean | |
CN204208599U (en) * | 2014-11-09 | 2015-03-18 | 高忠青 | A kind of medical waste vial automatic pressing crushing device |
JP2015117373A (en) * | 2013-11-15 | 2015-06-25 | 三菱日立パワーシステムズ株式会社 | Slag discharge device and method |
CN204523156U (en) * | 2015-01-05 | 2015-08-05 | 杨灵芝 | The semi-automatic disintegrating machine of a kind of medical waste bottle |
CN205236127U (en) * | 2015-11-05 | 2016-05-18 | 嘉善兴亚有色金属铸造有限公司 | Extrusion crushing apparatus with bearing structure |
CN205650281U (en) * | 2016-03-17 | 2016-10-19 | 丁小伟 | Quick comminution device of bar -shaped traditional chinese medicine |
CN106861875A (en) * | 2017-03-21 | 2017-06-20 | 郑世珍 | A kind of petroleum coke efficiency crushing device |
CN106902913A (en) * | 2017-05-14 | 2017-06-30 | 南昌诺义弘科技有限公司 | A kind of sieving approach device for carbonated rare earth |
JP6173508B1 (en) * | 2016-03-04 | 2017-08-02 | 三菱日立パワーシステムズ株式会社 | Slug crusher |
CN207169823U (en) * | 2017-08-31 | 2018-04-03 | 中国电力工程顾问集团西北电力设计院有限公司 | A kind of pneumatic breaking sifter |
-
2017
- 2017-08-31 CN CN201710776191.4A patent/CN107398323A/en active Pending
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2193329A5 (en) * | 1972-07-21 | 1974-02-15 | Nicolas Jean | |
JP2015117373A (en) * | 2013-11-15 | 2015-06-25 | 三菱日立パワーシステムズ株式会社 | Slag discharge device and method |
CN204208599U (en) * | 2014-11-09 | 2015-03-18 | 高忠青 | A kind of medical waste vial automatic pressing crushing device |
CN204523156U (en) * | 2015-01-05 | 2015-08-05 | 杨灵芝 | The semi-automatic disintegrating machine of a kind of medical waste bottle |
CN205236127U (en) * | 2015-11-05 | 2016-05-18 | 嘉善兴亚有色金属铸造有限公司 | Extrusion crushing apparatus with bearing structure |
JP6173508B1 (en) * | 2016-03-04 | 2017-08-02 | 三菱日立パワーシステムズ株式会社 | Slug crusher |
CN205650281U (en) * | 2016-03-17 | 2016-10-19 | 丁小伟 | Quick comminution device of bar -shaped traditional chinese medicine |
CN106861875A (en) * | 2017-03-21 | 2017-06-20 | 郑世珍 | A kind of petroleum coke efficiency crushing device |
CN106902913A (en) * | 2017-05-14 | 2017-06-30 | 南昌诺义弘科技有限公司 | A kind of sieving approach device for carbonated rare earth |
CN207169823U (en) * | 2017-08-31 | 2018-04-03 | 中国电力工程顾问集团西北电力设计院有限公司 | A kind of pneumatic breaking sifter |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115532351A (en) * | 2022-11-15 | 2022-12-30 | 涿州市烽合机械设备有限公司 | Vibration screening device for coal ash conveying and working method thereof |
CN115532351B (en) * | 2022-11-15 | 2024-04-30 | 涿州市烽合机械设备有限公司 | Vibration screening device for coal ash conveying and working method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN208683586U (en) | Coal bunker total management system | |
CN105773835A (en) | Ceramic raw material mixed-grinding concentrated preparation process and device | |
CN207169823U (en) | A kind of pneumatic breaking sifter | |
CN202303358U (en) | CFB (Circulating Fluidized Bed) boiler coal feeding system for co-combustion of middling coals | |
CN107398323A (en) | A kind of pneumatic breaking sifter | |
CN103134059B (en) | A kind of Integrated Processing System and method thereof improving coal-burning boiler utilization of ash and slag value | |
CN206488272U (en) | A kind of continual and steady coal feeder in stokehold | |
CN102506421B (en) | Circulating fluid bed (CFB) boiler coal supply system for blending combustion of middling coal | |
CN108659909A (en) | A kind of efficient upgrading system of lignite and its method for upgrading of sub-prime classification | |
CN205480966U (en) | A circulating fluidized bed boiler bed material addition system for bed is put to outband | |
CN111520735A (en) | Step-by-step decrement coal preparation system | |
CN111256112A (en) | Continuous feeding system suitable for direct blending burning of wet sludge of circulating fluidized bed boiler | |
CN108686807B (en) | Terminal circulating device for screening and crushing coal as fired | |
CN110360570A (en) | A kind of TDI coke burn before pretreatment system | |
CN110437859A (en) | One kind can continuous garbage cracking rotary processing equipment | |
CN206604548U (en) | Pneumatic breaking sifter | |
CN206215311U (en) | Coal pulverizer charging hopper hydraulic braking upset maintenance door | |
CN104879768A (en) | Crushed coal screener of coal spraying machine | |
CN106833692A (en) | A kind of oil-sand distillation system | |
CN104633692B (en) | System and method for clearing powder deposits in pulverized coal bunkers using adjacent boiler negative pressure | |
CN104848212A (en) | Method for sulfur fixation temperature control burning of coal gangue and efficient coupling and utilizing of lime ash | |
CN2304093Y (en) | Gas fully-automatic multi-function cube-producing furnace | |
CN213170162U (en) | Transportation system is smashed to heavy matter soda ash | |
CN205085131U (en) | Broken dust collecting system of powder | |
CN114700349B (en) | Biofuel shaft kiln, red mud magnetizing device and red mud magnetizing method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171128 |
|
RJ01 | Rejection of invention patent application after publication |