CN203620754U - Phosphorite grinding system - Google Patents
Phosphorite grinding system Download PDFInfo
- Publication number
- CN203620754U CN203620754U CN201320855507.6U CN201320855507U CN203620754U CN 203620754 U CN203620754 U CN 203620754U CN 201320855507 U CN201320855507 U CN 201320855507U CN 203620754 U CN203620754 U CN 203620754U
- Authority
- CN
- China
- Prior art keywords
- ball mill
- wake flow
- flow groove
- phosphorite
- cyclosizer
- 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 - Lifetime
Links
- 239000002367 phosphate rock Substances 0.000 title abstract description 7
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 title abstract 6
- 238000007599 discharging Methods 0.000 claims abstract description 8
- 239000011574 phosphorus Substances 0.000 claims description 29
- 229910052698 phosphorus Inorganic materials 0.000 claims description 29
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 27
- 230000008676 import Effects 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 7
- 239000011707 mineral Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 4
- 239000002562 thickening agent Substances 0.000 abstract 3
- 239000004570 mortar (masonry) Substances 0.000 abstract 2
- 239000002002 slurry Substances 0.000 description 16
- 238000000498 ball milling Methods 0.000 description 6
- 238000004062 sedimentation Methods 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 150000003017 phosphorus Chemical class 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Images
Abstract
The utility model discloses a phosphorite grinding system, which belongs to the technical field of mineral processing. The phosphorite grinding system comprises a phosphorite storage hopper, a ball mill, a wake flow groove, a cyclone classifier, an overflow collection groove and a thickener, wherein the phosphorite storage hopper is connected with a feeding hole of the ball mill, a discharging hole of the ball mill is connected with an inlet of the wake flow groove, an outlet of the wake flow groove is connected with a feeding hole of the cyclone classifier, a discharging hole of the cyclone classifier is connected with the feeding hole of the ball mill, an overflow hole of the cyclone classifier is connected with an inlet of the overflow collection groove, an outlet of the overflow collection groove is connected with a feeding hole of the thickener, and an overflow hole of the thickener is connected with a liquid inlet of the phosphorite storage hopper and a liquid inlet of the wake flow groove respectively. By additionally arranging the cyclone classifier, the granularity and uniformity of the mortar can be controlled, the quality of the mortar can be improved, and the subsequent processing effect can be guaranteed.
Description
Technical field
The utility model belongs to mineral processing technology field, particularly a kind of phosphorus ore defibrination system.
Background technology
In prior art, can a whole set of mineral treatment system be set at harbour, comprise conveyer belt, mineral crushing system, mineral defibrination system and slurry storage tank etc.Existing mineral defibrination system generally include ball mill and concentrator for the slip that is met requirement for the production of.Applicant's discovery, the pulp particle that adopts the combination of ball mill and concentrator to obtain is thin not and even, and the poor quality of slurry is unfavorable for the production of subsequent handling.
Summary of the invention
In order to improve the quality of slurry, ensure the production of subsequent handling, the utility model embodiment provides a kind of phosphorus ore defibrination system.Described technical scheme is as follows: the utility model embodiment provides a kind of phosphorus ore defibrination system, this phosphorus ore defibrination system comprises phosphorus ore hopper, ball mill, wake flow groove, cyclosizer, overflow feeder and concentrator, described phosphorus ore hopper is connected with the charging aperture of described ball mill, the discharging opening of described ball mill is connected with the entrance of described wake flow groove, the outlet of described wake flow groove is connected with the charging aperture of described cyclosizer, the discharging opening of described cyclosizer is connected with the charging aperture of described ball mill, the overfall of described cyclosizer is connected with the import of described overflow feeder, the outlet of described overflow feeder is connected with the charging aperture of described concentrator, the overfall of described concentrator is connected with the inlet of described wake flow groove with the inlet of described phosphorus ore hopper respectively.
The beneficial effect that the technical scheme that the utility model embodiment provides is brought is: the utility model embodiment provides a kind of phosphorus ore defibrination system, this system has increased by a cyclosizer and has carried out classification for the slurry to after ball milling between ball mill and concentrator, coarse granule slurry is returned to ball mill and carry out ball milling again, and outputing to concentrator from the overfall of cyclosizer, the slurry meeting the demands carries out sedimentation concentration, after sedimentation concentration, the slurry meeting the demands being sent into pulp storing tank stores, return to phosphorus ore hopper for adjusting the moisture of feeding of ball mill and returning to wake flow groove for adjusting the moisture of cyclosizer charging from the clear liquid of concentrator overfall output, ensure the effect of ball milling and cyclone classification.In the utility model, by the adding of cyclosizer, control granular size and the uniformity coefficient of slurry, improved the quality of slurry, ensured the effect of subsequent treatment.
Brief description of the drawings
Fig. 1 is the structured flowchart of the phosphorus ore defibrination system that provides of the utility model embodiment;
Fig. 2 is the part-structure schematic diagram of the ball mill that provides of the utility model embodiment and cyclosizer combination.
In figure: 1 phosphorus ore hopper, 2 measuring belts, 3 ball mills, 4 cyclosizers, 5 overflow feeders, 6 wake flow grooves, 7 transmission belts, 8 mono beam overhead cranes.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawing, the utility model is described in further detail.
Referring to Fig. 1, the utility model embodiment provides a kind of phosphorus ore defibrination system, and this phosphorus ore defibrination system comprises phosphorus ore hopper, ball mill, wake flow groove, cyclosizer, overflow feeder and concentrator.Wherein, the import of phosphorus ore hopper is connected with ground phosphate rock crushing device by transmission belt, and the outlet of phosphorus ore hopper is connected with the charging aperture of ball mill by measuring belt.The discharging opening of ball mill is connected with the entrance of wake flow groove, and the outlet of wake flow groove is connected with the charging aperture of cyclosizer.The discharging opening of cyclosizer is connected with the charging aperture of ball mill, and the overfall of cyclosizer is connected with the import of overflow feeder, and the outlet of overflow feeder is connected with the charging aperture of concentrator.The underflow opening of concentrator is connected with slurry storage tank, and the overfall of concentrator is connected with the inlet of wake flow groove for adjusting respectively the moisture of input ball mill and cyclosizer mineral aggregate with the inlet of phosphorus ore hopper respectively.Wherein, between aforementioned each structure, be connected by pipeline or conveyer belt, on pipeline, need to increase the structures such as pump, valve or flowmeter according to transmitting.Wake flow groove and overflow feeder, all for being arranged on ground trough body structure, are equipped with and stir on it.
Preferably, in the present embodiment, be equipped with the use in parallel of three groups of ball mills and cyclosizer.
Referring to Fig. 2, the concrete set-up mode of the phosphorus ore defibrination system that the utility model embodiment provides is: transmission belt 7 is located at phosphorus ore hopper 1(has certain altitude apart from ground) directly over, between the 1 below outlet of phosphorus ore hopper and the charging aperture of ball mill machine 3, be provided with horizontally disposed measuring belt 2, the ground of measuring belt 2 belows is provided with overflow feeder 5.The top of measuring belt 2 and the rear that is positioned at phosphorus ore hopper 1 are provided with cyclosizer 4, and cyclosizer 4 is connected with wake flow groove 6, overflow feeder 5 and concentrator (not shown) by pipeline.On the ground at phosphorus ore hopper 1 rear, be provided with successively ball mill 3 and wake flow groove 6, ball mill 3 is adjacent with wake flow groove 6 and be connected by pipeline.The top of ball mill 3 is provided with mono beam overhead crane 8 for R and M ball mill 3.
The utility model embodiment provides a kind of phosphorus ore defibrination system, this system has increased by a cyclosizer and has carried out classification for the slurry to after ball milling between ball mill and concentrator, coarse granule slurry is returned to ball mill and carry out ball milling again, and outputing to concentrator from the overfall of cyclosizer, the slurry meeting the demands carries out sedimentation concentration, after sedimentation concentration, the slurry meeting the demands being sent into pulp storing tank stores, return to phosphorus ore hopper for adjusting the moisture of feeding of ball mill and returning to wake flow groove for adjusting the moisture of cyclosizer charging from the clear liquid of concentrator overfall output, ensure the effect of ball milling and cyclone classification.In the utility model, by the adding of cyclosizer, control granular size and the uniformity coefficient of slurry, improved the quality of slurry, ensured the effect of subsequent treatment.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any amendment of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (1)
1. a phosphorus ore defibrination system, it is characterized in that, comprise phosphorus ore hopper, ball mill, wake flow groove, cyclosizer, overflow feeder and concentrator, described phosphorus ore hopper is connected with the charging aperture of described ball mill, the discharging opening of described ball mill is connected with the entrance of described wake flow groove, the outlet of described wake flow groove is connected with the charging aperture of described cyclosizer, the discharging opening of described cyclosizer is connected with the charging aperture of described ball mill, the overfall of described cyclosizer is connected with the import of described overflow feeder, the outlet of described overflow feeder is connected with the charging aperture of described concentrator, the overfall of described concentrator is connected with the inlet of described wake flow groove with the inlet of described phosphorus ore hopper respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320855507.6U CN203620754U (en) | 2013-12-24 | 2013-12-24 | Phosphorite grinding system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320855507.6U CN203620754U (en) | 2013-12-24 | 2013-12-24 | Phosphorite grinding system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203620754U true CN203620754U (en) | 2014-06-04 |
Family
ID=50807281
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320855507.6U Expired - Lifetime CN203620754U (en) | 2013-12-24 | 2013-12-24 | Phosphorite grinding system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203620754U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106914332A (en) * | 2017-04-18 | 2017-07-04 | 云南佳贝节能科技有限公司 | A kind of system of processing of rock phosphate in powder |
-
2013
- 2013-12-24 CN CN201320855507.6U patent/CN203620754U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106914332A (en) * | 2017-04-18 | 2017-07-04 | 云南佳贝节能科技有限公司 | A kind of system of processing of rock phosphate in powder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103100475B (en) | High-efficiency concentrate ore pulp processing device suitable for long-distance pipeline transportation | |
| CN105363275A (en) | A thickening and dewatering method for tailings and applications thereof | |
| CN102716799A (en) | Process method for removing phosphate impurities by combining gravity, centrifugal force and flotation | |
| CN203620754U (en) | Phosphorite grinding system | |
| CN203033769U (en) | Phosphate-pulp producing and breaking system | |
| CN202199415U (en) | Pretreatment device for rare earth processing flotation and magnetic separation | |
| CN102861659B (en) | Selective flocculation multi-section desliming process capable of being used for beneficiation | |
| CN204911641U (en) | Be applied to feeding device of upright mill | |
| CN206027827U (en) | Immediately, grind feed arrangement | |
| CN206688887U (en) | A kind of fine grinding hierarchical composition device systems sorted for micro fine particle magnetite stone | |
| CN204138680U (en) | A kind of orthoscopic blast furnace ore coke groove feeding system | |
| CN202893485U (en) | Ore pulp technology frequency conversion regulation and control device of thickener underflow pump | |
| CN106959606B (en) | Dynamic equalization in concentrate sorting system regulates and controls method | |
| CN204620062U (en) | Gathering dust and recycle device of a kind of building block raw material crushing system | |
| CN204182455U (en) | Lapping device | |
| CN203196719U (en) | Efficient processing device for concentrate slurry applicable to long-distance pipeline transportation | |
| CN108097447A (en) | A kind of middle phosphorus ore method for separating and separation system | |
| CN204724312U (en) | The high silicon bloodstone that silicon falls in a kind of upgrading smelts preprocessing system | |
| CN202967472U (en) | Ore separation device capable of conveniently regulating ore feeding quantity | |
| CN203546120U (en) | Conglomeration iron concentrate fine-grinding and pelletizing system | |
| CN103433097B (en) | Accurate ball loading and adding method in dry ore grinding | |
| CN203291811U (en) | Automatic reducing agent compounding system | |
| CN203155280U (en) | Coating crushing cabin | |
| CN203159480U (en) | Sintered lime discharging system | |
| CN204769206U (en) | Categorised recycle system of scum fine grinding |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140604 |
|
| CX01 | Expiry of patent term |