CN2656009Y - Circulating crusher - Google Patents
Circulating crusher Download PDFInfo
- Publication number
- CN2656009Y CN2656009Y CN 200320106057 CN200320106057U CN2656009Y CN 2656009 Y CN2656009 Y CN 2656009Y CN 200320106057 CN200320106057 CN 200320106057 CN 200320106057 U CN200320106057 U CN 200320106057U CN 2656009 Y CN2656009 Y CN 2656009Y
- Authority
- CN
- China
- Prior art keywords
- belt conveyor
- boiler
- sieve
- bruising
- uniform thickness
- 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.)
- Expired - Fee Related
Links
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
The utility model discloses a circulating washer breaking device for the solid material breaking, particularly suitable for the bruising of boiler fuel materials (such as a gangue, middle coal and the like), comprising a 1<#> belt transmission device (2), a steel removing device (4), a breaking device (5) under a material exhaustion end of the 1<#> belt transmission device (2), an equal thickness sieve (6), a 2<#> belt transmission device (7) under the equal thickness sieve (6) and a lifting device (3) equipped on the material exhaustion end of the equal thickness sieve (6) and the like. Fuels are sieved by a bruising sieve, big particle fuels are sent to the 1<#> belt transmission device (2) through the lifting device (3) then performs bruising and forms cycling, thereby the utility model can has the features of good bruising effect, avoiding big particle fuels from going inlet the boiler, then the fuel is burnt more fully, thereby ensuring the stable operation of the boiler.
Description
One, affiliated technical field
The utility model is the cycle crushing device that a kind of solid material carries out broken usefulness, and is specifically a kind of when being mainly used in boiler operatiopn, its fuel coal (as gangue, middle coal etc.) carried out the cycle crushing device of broken usefulness.
Two, background technology
At present, the most circulating fluidized bed boilers that adopt of China steam power plant, such boiler requires very strict to the granular size of fuel, gangue, middle coal are in burning, if the bad fuel particle of crushing effect is too big, in the combustion process fuel sulfuration bad, it is insufficient to burn, increased energy loss greatly, when serious even can cause boiler coke.In addition because burning is insufficient, the coal ash particle after the burning increases, wearing and tearing have been strengthened with boiler plants such as burner hearth inside, cyclone dust collector, economizer, air preheaters, increased the load of pressure fan, air-introduced machine, also influence dust removing effects, thereby influenced the safety and economic operation of boiler.
Three, summary of the invention
The purpose of this utility model provides a kind of broken cycle crushing device that can circulate.Its fragmentation that the macro particles fuel after the fragmentation can be circulated enters boiler to avoid macro particles fuel, thereby guarantees the normal operation of boiler.
The technical scheme that the utility model is taked is: former breaker is improved, uniform thickness sieve is arranged on disintegrating machine after, set up a lifting device.Be that the utility model is by 1
#Belt conveyor, tramp iron separator, disintegrating machine, uniform thickness sieve, elevator, 2
#Compositions such as belt conveyor.Tramp iron separator is located at 1
#The appropriate position of belt conveyor, disintegrating machine is located at 1
#The delivery end downside of belt conveyor, the uniform thickness sieve is located at the downside of disintegrating machine, 2
#Belt conveyor is located at the downside of uniform thickness sieve, and the lower end of elevator is located at the material that removes of uniform thickness sieve and holds, and the upper end of elevator is located at 1
#The delivery end of belt conveyor.
Fall into the uniform thickness sieve after disintegrating machine is with fuel (as gangue, middle coal etc.) fragmentation, the uniform thickness sieve is discharged into 2 with the satisfactory fuel of the particle that sifts out
#Belt conveyor is by 2
#Belt conveyor is delivered to boiler for use, and the macro particles fuel that uniform thickness sifts out unloads to elevator except that the material end from it, is carried to 1 by elevator
#The delivery end of belt conveyor enters disintegrating machine again and carries out fragmentation, so forms circulation.
Because the utility model improves former breaker, to wait sieve to be arranged on the disintegrating machine downside, and set up elevator, it is broken to have formed circulation, therefore it is good to the utlity model has crushing effect, avoid macro particles fuel to enter boiler, made burning more abundant, and guaranteed the characteristics such as stable of boiler.
Four, description of drawings
Accompanying drawing is the utility model schematic diagram.
Five, specific implementation method
As shown in the figure, the utility model is by 1
#Belt conveyor 2, tramp iron separator 4, disintegrating machine 5, uniform thickness sieve 6, elevator 3,2
#Belt conveyor 7 compositions such as grade.Elevator 3 is a bucket elevator.Tramp iron separator 4 is installed in 1
#The upside of belt conveyor 2 delivery ends, disintegrating machine 5 is located at 1
#The downside of belt conveyor 2 delivery ends, uniform thickness sieve 6 is located at the downside of disintegrating machine 5,2
#Belt conveyor 7 is arranged on the downside of uniform thickness sieve 6.The charging aperture of elevator 3 lower ends is arranged on removing of uniform thickness sieve 6 and expects the end place, and the discharge port of elevator 3 upper ends is arranged on 1
#The delivery end place of belt conveyor 2.
The feeder 1 of Bunker unloads fuel (as gangue, middle coal) to 1
#Belt conveyor 2 is discharged into disintegrating machine 5 after tramp iron separator 4 deironing, be discharged into uniform thickness sieve 6 after fragmentation, and the fuel after 6 pairs of fragmentations of uniform thickness sieve carries out vibration screening, and the satisfactory fuel of particle unloads to 2
#Belt conveyor 7 is by 2
#Belt conveyor 7 is delivered to boiler for using.Oarse-grained fuel then unloads to elevator 3 from the material end that removes of uniform thickness sieve 6, and elevator 3 is with its lifting and unload to 1
#Belt conveyor 2 carries out second-time breakage again, and so circulation has guaranteed crushing effect.This shows that it is good to the utlity model has crushing effect, avoided macro particles fuel to deliver to boiler and used, make fuel combustion more abundant, thereby guaranteed characteristics such as boiler operatiopn is steady.
Claims (1)
- A kind ofly include 1 #Belt conveyor (2), tramp iron separator (4), disintegrating machine (5), uniform thickness sieve (6), 2 #The cycle crushing device of belt conveyor (7) is characterized in that also including elevator (3); Tramp iron separator (4) is located at 1 #The appropriate position of belt conveyor (2), disintegrating machine (5) is located at 1 #The delivery end downside of belt conveyor (3), uniform thickness sieve (6) is located at the downside of disintegrating machine (5), 2 #Belt conveyor (7) is located at the downside of uniform thickness sieve (6), and the lower end of elevator (3) is located at the material that removes of uniform thickness sieve (6) and holds, and the upper end of elevator (3) is located at 1 #The delivery end of belt conveyor (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320106057 CN2656009Y (en) | 2003-10-10 | 2003-10-10 | Circulating crusher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320106057 CN2656009Y (en) | 2003-10-10 | 2003-10-10 | Circulating crusher |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2656009Y true CN2656009Y (en) | 2004-11-17 |
Family
ID=34341460
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200320106057 Expired - Fee Related CN2656009Y (en) | 2003-10-10 | 2003-10-10 | Circulating crusher |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2656009Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218364A (en) * | 2011-01-13 | 2011-10-19 | 抚州聚源硅业有限公司 | Preparation process of silicon metal powder with high chemical activity and low fine powder rate and special equipment |
| CN103292341A (en) * | 2013-05-30 | 2013-09-11 | 太原钢铁(集团)有限公司 | Smashing, screening and circulating coal feeding system |
| CN104117420A (en) * | 2014-07-10 | 2014-10-29 | 浙江瑞泰耐火材料科技有限公司 | A castable material grading arrangement device |
| CN104549700A (en) * | 2014-12-17 | 2015-04-29 | 河南广进塑业有限公司 | Circular grinding equipment |
| CN105318316A (en) * | 2014-06-23 | 2016-02-10 | 天津市红鼎数控锅炉制造有限公司 | Numerical control boiler with fuel screening mechanism |
| CN108686807A (en) * | 2018-05-04 | 2018-10-23 | 四川重盟电力设备制造有限公司 | As-fired coal sieving approach terminal circulator |
| CN114558670A (en) * | 2022-02-22 | 2022-05-31 | 碎得机械(北京)有限公司 | Material pretreatment system |
-
2003
- 2003-10-10 CN CN 200320106057 patent/CN2656009Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218364A (en) * | 2011-01-13 | 2011-10-19 | 抚州聚源硅业有限公司 | Preparation process of silicon metal powder with high chemical activity and low fine powder rate and special equipment |
| CN102218364B (en) * | 2011-01-13 | 2013-05-08 | 抚州聚源硅业有限公司 | Preparation process of silicon metal powder with high chemical activity and low fine powder rate and special equipment |
| CN103292341A (en) * | 2013-05-30 | 2013-09-11 | 太原钢铁(集团)有限公司 | Smashing, screening and circulating coal feeding system |
| CN105318316A (en) * | 2014-06-23 | 2016-02-10 | 天津市红鼎数控锅炉制造有限公司 | Numerical control boiler with fuel screening mechanism |
| CN104117420A (en) * | 2014-07-10 | 2014-10-29 | 浙江瑞泰耐火材料科技有限公司 | A castable material grading arrangement device |
| CN104117420B (en) * | 2014-07-10 | 2016-06-08 | 浙江瑞泰耐火材料科技有限公司 | A kind of mould material classification collator |
| CN104549700A (en) * | 2014-12-17 | 2015-04-29 | 河南广进塑业有限公司 | Circular grinding equipment |
| CN108686807A (en) * | 2018-05-04 | 2018-10-23 | 四川重盟电力设备制造有限公司 | As-fired coal sieving approach terminal circulator |
| CN114558670A (en) * | 2022-02-22 | 2022-05-31 | 碎得机械(北京)有限公司 | Material pretreatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4861318B2 (en) | Method and system for separating heavy ash and light ash and reducing unburned matter content | |
| CN101705132B (en) | Drying and dry separation combination device as well as dry separation and drying combination device | |
| CN209524539U (en) | A kind of biological particles burning boiler | |
| CN101983942B (en) | Drying and quality improvement apparatus for slime and sludge and technology thereof | |
| CN2656009Y (en) | Circulating crusher | |
| CN212408675U (en) | Novel sludge drying and incinerating system | |
| CN104327866A (en) | Domestic garbage fluidized bed anaerobic splitting decomposition device | |
| CN101717653A (en) | Treatment method before carbonizing coking coal | |
| CN201711181U (en) | Thermal power station coal-slurry sludge and raw coal mixed fuel feeding breaking system | |
| CN111649334A (en) | Novel sludge drying and incinerating system and method | |
| CN201560180U (en) | Dry separation and drying combination device | |
| CN107233989B (en) | Baking, grinding, spraying and burning integrated coal powder machine | |
| CN202253709U (en) | Coaling system of boiler | |
| CN201873599U (en) | Drying and upgrading device for coal slim and sludge | |
| CN209371225U (en) | Biomass rotary fire grate combustor | |
| CN208408011U (en) | A kind of solid waste treatment device | |
| CN112624637B (en) | High-activity steel slag micro powder preparation system | |
| CN101629775A (en) | Fully bubbling fluidized bed drier and novel process thereof for loading and preparing furnace coal | |
| CN2711552Y (en) | Dry type cooling conveyer and system for high temperature slag of coal boiler in electric power factory | |
| CN209721597U (en) | A kind of active carbon produces feeding system automatically | |
| CN114046497A (en) | Circulating fluidized bed boiler capable of reducing NOX discharge amount | |
| CN207555589U (en) | A kind of boiler to be burnt using biological particles | |
| CN105674256A (en) | Quick-start system and method for circulating fluidized bed boilers | |
| CN206768038U (en) | A kind of more class A fuel A biomass gasifying furnaces | |
| CN106810036A (en) | A kind of coal slime, drying sludge device for improving quality and technique |
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: 20041117 Termination date: 20091110 |