CN205761642U - Silicon ash ore reduction separation system - Google Patents
Silicon ash ore reduction separation system Download PDFInfo
- Publication number
- CN205761642U CN205761642U CN201620704586.4U CN201620704586U CN205761642U CN 205761642 U CN205761642 U CN 205761642U CN 201620704586 U CN201620704586 U CN 201620704586U CN 205761642 U CN205761642 U CN 205761642U
- Authority
- CN
- China
- Prior art keywords
- vibrosieve
- conveyer device
- elevator
- separation system
- screen cloth
- 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
- 238000000926 separation method Methods 0.000 title claims abstract description 17
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 229910052710 silicon Inorganic materials 0.000 title claims abstract description 14
- 239000010703 silicon Substances 0.000 title claims abstract description 14
- 239000004744 fabric Substances 0.000 claims abstract description 13
- 239000000428 dust Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 2
- 239000010456 wollastonite Substances 0.000 abstract description 15
- 229910052882 wollastonite Inorganic materials 0.000 abstract description 15
- 238000013461 design Methods 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000012545 processing Methods 0.000 abstract description 3
- 238000004513 sizing Methods 0.000 abstract 1
- 238000010298 pulverizing process Methods 0.000 description 5
- 239000012141 concentrate Substances 0.000 description 4
- 235000019738 Limestone Nutrition 0.000 description 3
- 239000006028 limestone Substances 0.000 description 3
- 229910021532 Calcite Inorganic materials 0.000 description 2
- 239000002223 garnet Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 238000007885 magnetic separation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000004308 accommodation Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
Landscapes
- Combined Means For Separation Of Solids (AREA)
Abstract
The utility model discloses a kind of silicon ash ore reduction separation system, including jaw crusher, vibrosieve, elevator and whirlwind disintegrating machine, described jaw crusher exit connects described vibrosieve by pipeline, described vibrosieve is provided with inside top discharge mouth and lower discharge port and described vibrosieve and is provided with screen cloth and is positioned at the first conveyer device below screen cloth, described screen cloth correspondence connects described top discharge mouth, described first conveyer device correspondence connects described lower discharge port, the second conveyer device is set at described top discharge mouth, the 3rd transporter is set at described lower discharge port, described second conveyer device connects described elevator, elevator upper end connects described whirlwind disintegrating machine.This utility model belongs to ore sizing processing technique field, by optimizing the operation of wollastonite mine sorting, reduce follow-up broken, separate the design requirement to equipment in producing, saved cost of equipment maintenance.
Description
Technical field
This utility model relates to Ore sorting processing technique field, is specifically related to a kind of wollastonite mine crushing-separating apparatus.
Background technology
Wollastonite is widely used in the industries such as pottery, metallurgy, building, machinery, electronics and papermaking, as rubber, plastics, tree
The filler of fat, paint, coating etc., gas filtering material, heat-barrier material or flux etc..
Wollastonite mine is the nonmetallic minerals of a kind of metasilicate, and mainly originate in Intermediate-acid Intrusive and limestone contacts change
Matter band, mineral mostly are wollastonite, and association product has quartz, calcite etc..Ore dressing mode commonly uses picking, magnetic separation, flotation and color choosing.
Beneficiation method commonly used by wollastonite has, and in unit for inertial conic pulverizer or autogenous tumbling mill, ore deposit is carried out dry type pulverizing and air
1.0mm and 0.071mm classification is pressed in finishing, and grade is that the carrying out of+1.0mm is pulverized again, and grade is the conduct of-0.071mm
Final wollastonite product, grade be-1.0+0.071mm carry out magnetic separation, obtain garnet concentrate.Extracting wollastonite
Before concentrate, non-magnetic product experience triboelectrification, electric tube furnace is heated to 150-170 DEG C, then at oscillating feeder
It is cooled to 100-110 DEG C on dish, sets electric field density as 3.5*105-3.9*105V/m, extracts wollastonite by electrostatic separation
Concentrate and simultaneously extraction calcite concentrate and quartz products.The method is complex, and processing conditions is harsh, and commercial application becomes
This height.
The patent of publication number CN101003026A discloses a kind of grinder for needle tabular spar, and jaw crusher is by promoting
Machine and pipeline are connected with making hammer pulverizer, and the discharging opening making hammer pulverizer is connected with sucking spiral multiple-stage separator by pipeline
Connect, spiral multiple-stage separator be provided above air-introduced machine.This invention achieves the multiple stage separation of Ore, improves work effect
Rate.But adding and beat hammer disintegrating machine and the burden of multiple-stage separator, the product design of air exercise hammer disintegrating machine and multiple-stage separator is wanted
Ask higher, not so can not meet separation requirement.
Utility model content
The utility model discloses a kind of silicon ash ore reduction separation system, it is intended to reduce broken in Ore production process and
The burden of separation equipment, optimizes separable programming to improve product quality.
Silicon ash ore reduction separation system, including jaw crusher, vibrosieve, elevator and whirlwind disintegrating machine, described Hubei Province
Formula disintegrating machine exit connects described vibrosieve by pipeline, described vibrosieve be provided with top discharge mouth and lower discharge port and described in shake
Dynamic sieve is internal to be provided with screen cloth and is positioned at the first conveyer device below screen cloth, and described screen cloth correspondence connects described top discharge mouth, institute
State the first conveyer device correspondence and connect described lower discharge port, at described top discharge mouth, set the second conveyer device, described lower discharge port
Place sets the 3rd transporter, and described second conveyer device connects described elevator, and elevator upper end connects described whirlwind disintegrating machine.
More excellent, it is provided with skewed slot in the middle of the tail end at described dark pavilion.
More excellent, described whirlwind disintegrating machine is connected by dust outlet tube dust settling pocket.
More excellent, described screen slope is arranged.
More excellent, described vibrosieve is ore classification vibrosieve.
A kind of silicon ash ore reduction separation system that this utility model provides, Ore i.e. carries out after tentatively pulverizing sieving for the first time
Choosing, reduce follow-up broken, separate the design requirement to equipment in producing, saved cost of equipment maintenance.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is only
It is embodiments more of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
Fig. 1 is principle schematic of the present utility model.
Detailed description of the invention
A kind of silicon ash ore reduction separation system that the utility model discloses, excellent by Ore being sorted the design of operation
Change, reduce follow-up broken, separate the design requirement to equipment in producing, saved cost of equipment maintenance.
Below in conjunction with the accompanying drawing in this utility model, the technical scheme in this utility model is carried out clearly and completely
Describe, it is clear that described is only a part of embodiment of this utility model rather than whole embodiments.Based on this practicality
Embodiment in novel, it is every other that those of ordinary skill in the art are obtained on the premise of not making creative work
Embodiment, broadly falls into the scope of this utility model protection.
As it is shown in figure 1, include jaw crusher 1, vibrosieve 3, elevator 8 and whirlwind disintegrating machine 9, described jaw crusher
1 exit connects described vibrosieve 3 by pipeline 2, and described vibrosieve 3 is provided with top discharge mouth and lower discharge port and described vibrosieve
3 inside are provided with screen cloth 7 and are positioned at the first conveyer device 4 below screen cloth 7, and described screen cloth 7 is corresponding connects described top discharge mouth, institute
State the first conveyer device 4 described lower discharge port of corresponding connection, at described top discharge mouth, set the second conveyer device 6, described bottom discharge
Setting the 3rd transporter 5 at Kou, described second conveyer device 6 connects described elevator 8, and elevator 8 upper end connects described whirlwind
Disintegrating machine 9.
Preferably, described vibrosieve 3 is ore classification vibrosieve, and described screen cloth 7 is obliquely installed, and is provided with angle and adjusts
Regulating device, range of accommodation is 8 °～25 °, and described whirlwind disintegrating machine upper end is connected by dust outlet tube 11 dust settling pocket 10.
Operation principle of the present utility model:
Wollastonite mine enters vibrosieve 3 after jaw crusher 1 is tentatively pulverized, and after preliminary pulverizing, the Ore of bulk is sent to
Second conveyer device 6, the powder body after preliminary pulverizing is sent to the 3rd conveyer device 5 and carries out subsequent treatment, at the second conveyer device 6
On by the bulk silicon lime stone of picking separation high-quality, remaining Ore is sent to whirlwind disintegrating machine 9 after entering elevator 8 and carries out secondary
Broken, the dust produced after whirlwind disintegrating machine 9 is broken enters dust settling pocket to reduce dust recycling.
Wollastonite mine carries out classification after primary comminution, and color selects the wollastonite of high-quality, removes the wollastonite sheet of low content,
The Ore that remaining ore particles is bigger enters in whirlwind disintegrating machine pulverize with the second conveyer device, elevator, and granule is less
Ore is ground pulverizing.
By above description, silicon ash ore reduction separation system disclosed in this utility model, tentatively pulverize at Ore
After, it is processed after Ore being sorted by classifying screen, the wollastonite mine of available different qualities, decreases garnet, Fang Xie
Stone etc. are mixed into the content of high quality silicon lime stone, and different grades of wollastonite mine can break up process, provide convenient to the screening of Ore later stage.
Above content is to combine concrete preferred implementation further detailed description of the utility model, it is impossible to
Assert that of the present utility model being embodied as is confined to these explanations.Ordinary skill for this utility model art
For personnel, without departing from the concept of the premise utility, it is also possible to make some simple deduction or replace, all should regard
For belonging to protection domain of the present utility model.
Claims (4)
1. silicon ash ore reduction separation system, including jaw crusher, vibrosieve, elevator and whirlwind disintegrating machine, its feature exists
In, described jaw crusher exit connects described vibrosieve by pipeline, and described vibrosieve is provided with top discharge mouth and bottom discharge
Being provided with screen cloth inside mouth and described vibrosieve and be positioned at the first conveyer device below screen cloth, described screen cloth correspondence connects on described
Discharging opening, described first conveyer device correspondence connects described lower discharge port, sets the second conveyer device at described top discharge mouth, described
Setting the 3rd transporter at lower discharge port, described second conveyer device connects described elevator, and elevator upper end connects described rotation
Wind disintegrating machine.
Silicon ash ore reduction separation system the most according to claim 1, it is characterised in that described whirlwind disintegrating machine passes through
Dirt pipe connects dust settling pocket.
Silicon ash ore reduction separation system the most according to claim 1, it is characterised in that described screen slope is arranged.
Silicon ash ore reduction separation system the most according to claim 1, it is characterised in that described vibrosieve is ore classification
Vibrosieve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620704586.4U CN205761642U (en) | 2016-07-06 | 2016-07-06 | Silicon ash ore reduction separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620704586.4U CN205761642U (en) | 2016-07-06 | 2016-07-06 | Silicon ash ore reduction separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205761642U true CN205761642U (en) | 2016-12-07 |
Family
ID=58124054
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620704586.4U Expired - Fee Related CN205761642U (en) | 2016-07-06 | 2016-07-06 | Silicon ash ore reduction separation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205761642U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106964469A (en) * | 2017-05-16 | 2017-07-21 | 连州市新渝合矿产品有限公司 | Wollastonite processing production line |
| CN107413495A (en) * | 2017-07-14 | 2017-12-01 | 望江县金峰矿产品科技有限公司 | A kind of silica multi-stage crushing screening machine |
| CN109110792A (en) * | 2018-09-18 | 2019-01-01 | 邵阳金拓科技开发有限公司 | Production line is brightened in a kind of purification of anhydrous gypsum |
| CN111843811A (en) * | 2020-08-05 | 2020-10-30 | 卢昌敏 | Silica processing preprocessing device |
| CN112076870A (en) * | 2020-09-06 | 2020-12-15 | 陈丽萍 | Copper extraction and deironing equipment for copper ore acid leaching solution |
-
2016
- 2016-07-06 CN CN201620704586.4U patent/CN205761642U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106964469A (en) * | 2017-05-16 | 2017-07-21 | 连州市新渝合矿产品有限公司 | Wollastonite processing production line |
| CN106964469B (en) * | 2017-05-16 | 2023-08-15 | 连州市新渝合矿产品有限公司 | Wollastonite ore dressing production line |
| CN107413495A (en) * | 2017-07-14 | 2017-12-01 | 望江县金峰矿产品科技有限公司 | A kind of silica multi-stage crushing screening machine |
| CN109110792A (en) * | 2018-09-18 | 2019-01-01 | 邵阳金拓科技开发有限公司 | Production line is brightened in a kind of purification of anhydrous gypsum |
| CN111843811A (en) * | 2020-08-05 | 2020-10-30 | 卢昌敏 | Silica processing preprocessing device |
| CN112076870A (en) * | 2020-09-06 | 2020-12-15 | 陈丽萍 | Copper extraction and deironing equipment for copper ore acid leaching solution |
| CN112076870B (en) * | 2020-09-06 | 2022-04-19 | 北京黎登盛荣科技有限公司 | Copper extraction and deironing equipment for copper ore acid leaching solution |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 Termination date: 20200706 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |