CN202336371U - Micro-powder preparing system - Google Patents
Micro-powder preparing system Download PDFInfo
- Publication number
- CN202336371U CN202336371U CN2011203676569U CN201120367656U CN202336371U CN 202336371 U CN202336371 U CN 202336371U CN 2011203676569 U CN2011203676569 U CN 2011203676569U CN 201120367656 U CN201120367656 U CN 201120367656U CN 202336371 U CN202336371 U CN 202336371U
- Authority
- CN
- China
- Prior art keywords
- casing
- chamber
- grading
- crushing
- rotoclone collector
- 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
Images
Landscapes
- Crushing And Pulverization Processes (AREA)
Abstract
The utility model provides a micro-powder preparing system which has the advantages of wide application scope, reliable operation, and capability of producing stable-quality products, reducing equipment energy consumption and guaranteeing product granularity. The micro-powder preparing system comprises an ultrafine crusher, a rotoclone collector, and a draught fan; the ultrafine crusher comprises a casing and a feeding pipe connected with the casing, the casing is provided with an inlet chamber at the lower part and a crushing and grading chamber at the upper part, a rotatable grading impeller is installed in the crushing and grading chamber; the grading impeller is provided with a grading chamber at the upper part and a crushing chamber at the lower part; a rotary crushing disc which has a blade is installed in the crushing chamber; a shunting ring is installed between the crushing disc and the grading impeller; the central part of the shunting ring is provided with a feeding pipe outlet used for delivering the pre-crushed material into the crushing chamber; a discharge port is arranged at the upper part of the grading chamber; the discharge port of the ultrafine crusher is connected with an air inlet located at the side of the rotoclone collector, an air outlet located at the upper part of the rotoclone collector is connected with the draught fan. The micro-powder preparing system further comprises a deslagging device installed on the casing of the ultrafine crush and used for discharging material which cannot be crushed out of the crushing chamber.
Description
Technical field
The utility model relates to the micro mist preparation system.
Background technology
At present, powder deep processing abrasive dust device category is a lot of both at home and abroad, and purposes and specific energy consumption difference are very big, and service life is limited, inconvenient maintenance.
Summary of the invention
The purpose of the utility model provides a kind of applied widely, reliable, constant product quality, reduction equipment energy consumption, guarantees the micro mist preparation system of product granularity.
The micro mist preparation system of the utility model comprises ultrafine crusher, rotoclone collector, air-introduced machine; Ultrafine crusher comprises casing, be connected feed pipe on the casing, have the inlet plenum of bottom, the pulverizing and the grading room on top in the casing, pulverize and grading room in be provided with rotating classifying turbine; The top of classifying turbine is that grading room, bottom are pulverizing chamber; Be provided with the grating disk of rotation in the pulverizing chamber, have blade on the grating disk; Between grating disk and classifying turbine, be provided with flow splitter; Be used for sending into the central part of the feed pipe outlet of pulverizing chamber to the material of precomminution at flow splitter; Discharging opening is opened the top at grading room; The air outlet on top that the discharging opening of ultrafine crusher connects sidepiece air inlet, the rotoclone collector of rotoclone collector connects air-introduced machine; It also comprises being used on the casing that is arranged on ultrafine crusher discharges the material that can not pulverize from pulverizing chamber deslagging device.
The beneficial effect of the utility model: the ultra-fine grinding function is accomplished material simultaneously and is pulverized and micro mist sorting twice powder manufacturing procedure.During ultrafine crusher work, discharging opening links to each other with air-introduced machine through rotoclone collector.The indoor grating disk (and blade) of pulverizing chamber is used for the material of being sent into by feed pipe is smashed into fine powder; Classifying turbine is divided into qualified fine powder of granularity and underproof meal to fine powder, and qualified fine powder gets into rotoclone collector through discharging opening, and qualified little micro mist is collected the micro mist that obtains needs through the rewinding mouth of the bottom of rotoclone collector.The waste gas of dust-laden is discharged by air-introduced machine.In the ultrafine crusher, grating disk and classifying turbine are driven respectively by two concentric shafts respectively, and the rotating speed adjustable of classifying turbine is in order to regulate the granularity of product.Underproof meal falls back to pulverizing chamber along the flow splitter inwall, continues to pulverize, till reaching release mesh.With ultrafine crusher to material pulverize, sorting because grating disk, blade etc. are higher with the direct parts in contact hardness of material, it is very little wear and tear, does not have in the impurity entering material that impurity has only minute quantity in other words; Simultaneously, powder is collected, also do not had impurity and get into rotoclone collector.In addition, parts wears such as grating disk, blade are very little in the ultrafine crusher; And rotoclone collector can not be worn basically, so the long service life of this preparation facilities, and is not fragile.The utility model is particularly useful for Mohs' hardness less than 6 material ultra-fine grinding; Like calcium carbonate, talcum powder, bauxite, kaolin, quartz, calcite, bolognian stone, White Cloud Mountain, mica etc.; Can obtain the micro mist that the 200-4000 order does not wait, it is applied widely, energy consumption is low, long service life, easy to maintenance.Through deslagging device, can in time discharge the material that can not pulverize, pass through crushing process once more so as not to it, reduced equipment energy consumption, also guaranteed the granularity of product.
Above-mentioned micro mist preparation system, it also comprises bagroom, the air outlet on the top of rotoclone collector connects the sidepiece air inlet of bagroom; The air outlet of bagroom connects air-introduced machine.Bagroom can filter the dust in the gas that the rotoclone collector air outlet is discharged, and so just can prevent direct discharge of dust and contaminated environment.
Above-mentioned micro mist preparation system, feed pipe are provided with the by-pass valve control of control mass flow.Can control the flow of the material that gets into pulverizing chamber through by-pass valve control; Prevent that runner is excessive and stop up feed pipe, can make that also to get in the pulverizing chamber material ratio more even, at the uniform velocity get into pulverizing chamber; The material crushing process is steady, and the material grinding degree big fluctuation can not occur.
Above-mentioned micro mist preparation system, deslagging device comprises conveying worm, the import of conveying worm is at the casing inner wall place in the flow splitter outside.
Above-mentioned micro mist preparation system, it also comprises the belt conveyor that is used for sending into the material that needs are pulverized feed pipe.
Description of drawings
Fig. 1 is the sketch map of micro mist preparation facilities.
Fig. 2 is the sketch map of ultrafine crusher.
Fig. 3 is the enlarged drawing of grading room 82, classification rotating shaft 13 among Fig. 2 etc.
Fig. 4 be among Fig. 2 blade 11, pulverize belt pulley 16, pulverize the enlarged drawing of rotating shaft 15 etc.
Fig. 5 be among Fig. 2 inlet plenum 7, blade 11, pulverize the enlarged drawing of rotating shaft 15 etc.
Fig. 6 is the side view of ultrafine crusher.
Fig. 7 is the enlarged drawing of grading room 82, classification rotating shaft 13 among Fig. 6 etc.
Fig. 8 is the enlarged drawing of blade 11, conveying worm 100 among Fig. 6 etc.
Fig. 9 is the enlarged drawing of pulverizing chamber 81, conveying worm 100 among Fig. 6 etc.
The specific embodiment
To combine accompanying drawing and embodiment that the utility model is described further below.
Referring to micro mist preparation system shown in Figure 1, comprise ultrafine crusher 1, rotoclone collector 2, bagroom 3, air-introduced machine 4.
Pulverizing and grading room 8 comprise pulverizing chamber 81, grading room 82.In pulverizing and the grading room 8 classifying turbine 9 is set.The top of classifying turbine is that grading room 82, bottom are pulverizing chamber 81.Grating disk 10 is set in the pulverizing chamber.Have blade 11 on the grating disk; Between grating disk and classifying turbine, be provided with flow splitter 17.Classifying turbine 9 joins with the classification rotating shaft 13 of passing grading room, and the top of classification rotating shaft 13 links to each other with split-pole motor 14.Grating disk 10 joins with the pulverizing rotating shaft 15 of passing inlet plenum, and the lower end of pulverizing rotating shaft is fixed with pulverizes belt pulley 16.Pulverizing belt pulley 16 links to each other with pulverizing motor 18 through belt.The axis of pulverizing rotating shaft 15, grating disk 10, classification rotating shaft 13, classifying turbine 9 all overlaps.
The outlet of feed pipe 5 communicates with pulverizing chamber 81 at the central part of flow splitter.Feed pipe is provided with the by-pass valve control 51 of control mass flow.Discharging opening 6 is opened the upper lateral part at grading room.
Be fixed on the casing inner wall place of the import of the conveying worm (deslagging device) 100 on the ultrafine crusher casing in the flow splitter outside; The slag notch 101 of conveying worm is below the conveying worm middle part; Drive motors 102 actions of conveying worm can be discharged the material that can not pulverize from pulverizing chamber.
The air outlet 22 on top that the discharging opening 6 of ultrafine crusher connects sidepiece air inlet 21, the rotoclone collector of rotoclone collector 2 connects the sidepiece air inlet 31 of bagroom 3; The air outlet 32 of bagroom connects air-introduced machine 4.
Grating disk 10 and blade 11 be high speed rotating under the drive of pulverizing belt pulley 16, pulverizing rotating shaft 15.Material is injected pulverizing chamber through feed pipe 5, and material is fluidization, produces violent collision, friction, shearing with grating disk that runs up and blade 11, and grating disk (and blade) will smash into fine powder by the material that feed pipe is sent into, and accomplish the ultra-fine grinding of particle.Material after the pulverizing is entered into from inlet plenum 7 in the pulverizing chamber 81 and the air-flow that rises is delivered in the grading room 82.The classifying turbine 9 that rotates under by the drive of split-pole motor 14, classification rotating shaft 13 is divided into qualified fine powder of granularity and underproof meal to fine powder, qualified fine powder by 4 through discharging opening 6 sucking-offs.That is to say, under the effect of classifying turbine centrifugal force and air-introduced machine draft, realized the separation of thickness powder.Underproof meal falls back to pulverizing chamber because of the gravity of self along flow splitter 17 inwalls, continues to pulverize, till reaching release mesh.
Qualified fine powder gets into rotoclone collectors 2 with air-flow through discharging opening 6, and qualified fine powder descends while rotate along the madial wall of rotoclone collector, and discharging opening 23 discharges of final bottom from rotoclone collector promptly obtain qualified micro mist.The dusty gas that contains the fine dust more small than qualified fine powder is inhaled into the sidepiece air inlet 31 of bagroom 3 by the top air outlet 23 of rotoclone collector.Fine dust by bagroom 3 is collected is regularly discharged by the discharging opening 33 of bagroom 3 bottoms.Gas through bagroom 3 purifies is extracted out by air-introduced machine 4 by the air outlet 32 of bagroom, discharges through the discharge line 41 of air-introduced machine.
Grating disk and classifying turbine pass through to pulverize belt pulley and split-pole motor single driving by two concentric pulverizing rotating shafts and classification rotating shaft respectively.The rotating speed adjustable of classifying turbine is in order to regulate the granularity of product.
Claims (5)
1. a micro mist preparation system comprises ultrafine crusher, rotoclone collector, air-introduced machine; Ultrafine crusher comprises casing, be connected feed pipe on the casing, have the inlet plenum of bottom, the pulverizing and the grading room on top in the casing, pulverize and grading room in be provided with rotating classifying turbine; The top of classifying turbine is that grading room, bottom are pulverizing chamber; Be provided with the grating disk of rotation in the pulverizing chamber, have blade on the grating disk; Between grating disk and classifying turbine, be provided with flow splitter; Be used for sending into the central part of the feed pipe outlet of pulverizing chamber to the material of precomminution at flow splitter; Discharging opening is opened the top at grading room; It is characterized in that: the air outlet on top that the discharging opening of ultrafine crusher connects sidepiece air inlet, the rotoclone collector of rotoclone collector connects air-introduced machine; It also comprises being used on the casing that is arranged on ultrafine crusher discharges the material that can not pulverize from pulverizing chamber deslagging device.
2. micro mist preparation system as claimed in claim 1 it is characterized in that: further comprising bagroom, and the air outlet on the top of rotoclone collector connects the sidepiece air inlet of bagroom; The air outlet of bagroom connects air-introduced machine.
3. micro mist preparation system as claimed in claim 1 is characterized in that: feed pipe is provided with the by-pass valve control of control mass flow.
4. micro mist preparation system as claimed in claim 1, it is characterized in that: deslagging device comprises conveying worm, the import of conveying worm is at the casing inner wall place in the flow splitter outside.
5. micro mist preparation system as claimed in claim 1 it is characterized in that: further comprising the belt conveyor that is used for sending into the material that needs are pulverized feed pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203676569U CN202336371U (en) | 2011-09-30 | 2011-09-30 | Micro-powder preparing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203676569U CN202336371U (en) | 2011-09-30 | 2011-09-30 | Micro-powder preparing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202336371U true CN202336371U (en) | 2012-07-18 |
Family
ID=46485077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203676569U Expired - Fee Related CN202336371U (en) | 2011-09-30 | 2011-09-30 | Micro-powder preparing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202336371U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113843001A (en) * | 2021-09-08 | 2021-12-28 | 山东惟远新材料装备有限公司 | Vertical crusher |
-
2011
- 2011-09-30 CN CN2011203676569U patent/CN202336371U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113843001A (en) * | 2021-09-08 | 2021-12-28 | 山东惟远新材料装备有限公司 | Vertical crusher |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103028473A (en) | Uniform-granularity micro-powder preparation system | |
| CN103567046B (en) | Carbon fiber disintegrating apparatus | |
| CN106955774A (en) | A kind of use gas shock mode carries out the micronizer of sub-material | |
| CN103028474A (en) | Micro-powder preparing device | |
| CN202336373U (en) | Micro powder preparing system | |
| CN101838019A (en) | Method and device for preparing battery-grade low-ferrous cobaltosic oxide powder | |
| CN203355824U (en) | Rotor mill | |
| CN102380447A (en) | Superfine crushing machine | |
| CN202336372U (en) | Uniform-granularity micro-powder preparation system | |
| CN201553612U (en) | Gas flow vortex powder refining machine for producing spherical graphite | |
| CN202336374U (en) | Ultrafine smashing machine | |
| CN202336368U (en) | Superfine grinder with slag remover | |
| CN202336371U (en) | Micro-powder preparing system | |
| CN205129600U (en) | Circulating carborundum granule plastic equipment | |
| CN106944231A (en) | A kind of medicinal material pulverizer of high-efficiency precision refinement | |
| CN104289277A (en) | Energy-saving low-carbon environment-friendly European-type grinding machine | |
| CN202336369U (en) | Superfine crusher | |
| CN103028472A (en) | Superfine grinder with slag remover | |
| CN201728145U (en) | Vertical grinder high-fineness dynamic-static combined separator device | |
| CN102441474A (en) | Cyclonic jet mill | |
| CN103028476A (en) | Micro-powder preparing system | |
| CN106622597B (en) | A method of for producing the pulverizer system and production nano particle of nano particle | |
| CN202143852U (en) | Raymond mill | |
| CN202169197U (en) | Scattering grader | |
| CN201694856U (en) | Battery-level low-iron cobaltosic oxide powder preparing device |
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: 20120718 Termination date: 20130930 |