CN106391296B - A kind of gravity ore dressing method of particulate antimony oxide ore - Google Patents
A kind of gravity ore dressing method of particulate antimony oxide ore Download PDFInfo
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- CN106391296B CN106391296B CN201611143175.3A CN201611143175A CN106391296B CN 106391296 B CN106391296 B CN 106391296B CN 201611143175 A CN201611143175 A CN 201611143175A CN 106391296 B CN106391296 B CN 106391296B
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- ore
- antimony oxide
- antimony
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B7/00—Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage
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- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
A kind of gravity ore dressing method of particulate antimony oxide ore, by the antimony oxide raw ore after selecting antimony tailing or grinding, coarse-grained material first is removed with Vibration Screen, then remove sludge with hydrocyclone, last material is once sorted from suspended vibrating concentrating machine with conical surface is flowed into, and obtains antimony concentrate and true tailings.The recovery rate in ore-dressing of the final gained antimony concentrate of the method for the present invention may be up to 49.25%, and grade is up to 20.0%, and recovery rate in ore-dressing is high, and high production efficiency is easy to operate, labor intensity, energy consumption and at low cost, operating environment close friend.
Description
Technical field
The present invention relates to a kind of gravity ore dressing methods, and in particular to a kind of gravity ore dressing method of particulate antimony oxide ore.
Background technique
Antimony Oxide Ores are the important source materials of antimony product production, and shared specific gravity is quite big in China's antimonial resources,
In the produced antimony ore in tinnery North, the content of antimony trisulfide and antimony oxide respectively accounts for 50%.Study the efficient of antimony oxide ore ore dressing
Recycling is of great significance to the utilization rate for improving China's antimony resource.
The ore dressing of Antimony Oxide Ores especially particulate Antimony Oxide Ores is recycled, and is the problem in the outer ore dressing field of Now Domestic
One of.For many years, it although having conducted extensive research both at home and abroad, does not make a breakthrough.Industrial application is still with weight at present
It is selected as leading, but the rate of recovery of jigging, shaking table operation is low, and is difficult to recycle particulate oxide ore.Domestic ore dressing worker is centrifuged
Ore separators adds belt chute, and runout belt chute, spiral chute, tower swivel chute etc. handle the research of antimony oxide thin mud, as a result
It is undesirable.A kind of beneficiation method and process equipment for particulate antimony oxide ore high efficiente callback is found, to obtain optimal warp
Ji benefit and social benefit are an urgent demands of antimony mineral ore dressing field.
CN104226463A discloses a kind of high tin-polymetallic sulphide ore beneficiation method, and this method is using outstanding vibration conical surface disk
The mineral of ore separators recycling are stanniferous sulphide ore；Its ore pre-classification is using spiral classifier and large tilting plate board concentrating box point
Grade concentration；But rough concentrate also needs table concentration, the ore size fraction range of processing is 10~40 μm, relatively narrow.
Summary of the invention
The technical problem to be solved by the present invention is to overcome drawbacks described above of the existing technology, provide a kind of ore dressing time
High income, high production efficiency, low energy consumption, the gravity ore dressing method of the particulate antimony oxide ore of operating environment close friend.
The technical solution adopted by the present invention to solve the technical problems is as follows: a kind of gravity separation side of particulate antimony oxide ore
Method is the antimony oxide raw ore after selecting antimony tailing or grinding, first removes coarse-grained material with Vibration Screen, then removed with hydrocyclone
Sludge, last material are once sorted from suspended vibrating concentrating machine with conical surface is flowed into, and obtain antimony concentrate and true tailings.
Preferably, the antimony oxide raw ore is antimony oxide ore or sulphur and oxygen mixed antimony ore.Described that antimony tailing is selected to refer to, ore dressing is raw
The low-grade floating (weight) containing antimony discharged in production selects the tailing containing antimony and low-grade antimony oxide ore object of tailing, Tailings Dam stockpiling, antimony oxygen
Rate reaches as high as 100%.
Preferably, the tailing or to grind the fineness of rear raw ore be mass content under 200 meshes is 50~75%(more excellent
Select 55~65%), grade containing antimony is 0.3~1.2%, antimony oxygenation efficiency >=85%.
Preferably, the coarse-grained material that the Vibration Screen removes is 200 mesh oversize of fineness.The part oversize grade is low,
Or more preferably recycled using other preparation equipments, and containing sundries such as wooden slags, if will affect sorting result into subsequent process.
Preferably, the sludge of the hydrocyclone removing is 800 mesh screenings of fineness.If the part screenings enters outstanding
The rate of recovery that vibrating concentrating machine with conical surface will lead to antimony is low, and interferes ore dressing process.
Preferably, the rotational frequency of the suspended vibrating concentrating machine with conical surface is 8~12Hz, 15~25Hz of vibration frequency, treating capacity
For every 400~800kg/h.The suspended vibrating concentrating machine with conical surface of the preferred model DSLXZ-4000 of suspended vibrating concentrating machine with conical surface.Outstanding vibration
Concentrating machine with conical surface is to shear loose theoretical and film concentration as the gravitational separation equipment of theoretical foundation, especially suitable for fine using Bai Genuo
Grain metalliferous mineral sorts.After the method for the present invention first pre-processes raw material, is separated, then select the equipment it is described rotation or
It is sorted under vibration frequency, obtains preferable mineral processing index.
It is highly preferred that the rotational frequency of the suspended vibrating concentrating machine with conical surface is 10Hz, 18~20Hz of vibration frequency, treating capacity is
Every 550~750kg/h.
The method of the present invention will contain low-grade antimony ore object or antimony tailing is selected first to be carried out with high frequency vibrating fine screen and hydrocyclone
Pretreatment, then sorted with suspended vibrating concentrating machine with conical surface, the recovery rate in ore-dressing of final gained antimony concentrate may be up to 49.25%, grade
Up to 20.0%, recovery rate in ore-dressing is high, and high production efficiency is easy to operate, labor intensity, energy consumption and at low cost, operating environment friend
It is good.
Specific embodiment
Below with reference to embodiment, the invention will be further described.
Embodiment 1
By the low-grade flotation tailing of antimony that contains discharged in certain ore dressing produced on-site, (fineness is the mass content under 200 meshes
It is 56.0%, grade containing antimony is 1.10%, and antimony oxygenation efficiency is 91.0%), first to screen out 200 mesh oversize of fineness with high frequency shale shaker
Coarse-grained material, then with the sludge of hydrocyclone removing 800 mesh screenings of fineness, last material is outstanding from DSLXZ-4000 type is flowed into
Vibrating concentrating machine with conical surface is 560kg/h in every treating capacity, and rotational frequency 10Hz, vibration frequency is once to be divided under 20Hz
Choosing, obtains antimony concentrate and true tailings.
Recovery rate in ore-dressing is 49.25%, and the grade of antimony concentrate is 15.0%.
Embodiment 2
By the tailing of certain antimony ore plant tailing library stockpiling, (fineness is that the mass content under 200 meshes is 65.0%, product containing antimony
Position is 0.65%, and antimony oxygenation efficiency is 86.0%), the coarse-grained material of 200 mesh oversize of fineness first to be screened out with high frequency shale shaker, then use water
Power cyclone removes the sludge of 800 mesh screenings of fineness, and last material flows into DSLXZ-4000 type suspended vibrating concentrating machine with conical surface certainly,
Every treating capacity is 710kg/h, and rotational frequency 10Hz, vibration frequency is once to be sorted under 18Hz, obtains antimony concentrate and most
Finality mine.
Recovery rate in ore-dressing is 47.65%, and the grade of antimony concentrate is 20.0%.
Embodiment 3
By the tailing of certain antimony sulfide ore flotation mill discharge, (fineness is that the mass content under 200 meshes is 62.0%, product containing antimony
Position is 0.30%, and antimony oxygenation efficiency is 88.0%), the coarse-grained material of 200 mesh oversize of fineness first to be screened out with high frequency shale shaker, then use water
Power cyclone removes the sludge of 800 mesh screenings of fineness, and last material flows into DSLXZ-4000 type suspended vibrating concentrating machine with conical surface certainly,
Every treating capacity is 690kg/h, and rotational frequency 10Hz, vibration frequency is once to be sorted under 18Hz, obtains antimony concentrate and most
Finality mine.
Recovery rate in ore-dressing is 43.65%, and the grade of antimony concentrate is 18.0%.
Claims (9)
1. a kind of gravity ore dressing method of particulate antimony oxide ore, it is characterised in that: the antimony oxide after selecting antimony tailing or grind is former
Mine first removes coarse-grained material with Vibration Screen, then removes sludge with hydrocyclone, and last material flows into suspended vibrating concentrating machine with conical surface certainly
It is once sorted, obtains antimony concentrate and true tailings；The tailing or the fineness for grinding rear raw ore are that the quality under 200 meshes contains
Amount is 50~75%, and grade containing antimony is 0.3~1.2%, antimony oxygenation efficiency >=85%；The rotational frequency of the suspended vibrating concentrating machine with conical surface is 8
~12Hz, 15~25Hz of vibration frequency, treating capacity are every 400~800kg/h.
2. the gravity ore dressing method of particulate antimony oxide ore according to claim 1, it is characterised in that: the antimony oxide raw ore
For antimony oxide ore or sulphur and oxygen mixed antimony ore.
3. the gravity ore dressing method of particulate antimony oxide ore according to claim 1 or claim 2, it is characterised in that: the Vibration Screen
The coarse-grained material removed is 200 mesh oversize of fineness.
4. the gravity ore dressing method of particulate antimony oxide ore according to claim 1 or claim 2, it is characterised in that: the hydraulic cyclone
The sludge of device removing is 800 mesh screenings of fineness.
5. the gravity ore dressing method of particulate antimony oxide ore according to claim 3, it is characterised in that: the hydrocyclone
The sludge of removing is 800 mesh screenings of fineness.
6. the gravity ore dressing method of particulate antimony oxide ore according to claim 1 or claim 2, it is characterised in that: the outstanding vibration conical surface
The rotational frequency of ore separators is 10Hz, and 18~20Hz of vibration frequency, treating capacity is every 550~750kg/h.
7. the gravity ore dressing method of particulate antimony oxide ore according to claim 3, it is characterised in that: the outstanding vibration conical surface choosing
The rotational frequency of mine machine is 10Hz, and 18~20Hz of vibration frequency, treating capacity is every 550~750kg/h.
8. the gravity ore dressing method of particulate antimony oxide ore according to claim 4, it is characterised in that: the outstanding vibration conical surface choosing
The rotational frequency of mine machine is 10Hz, and 18~20Hz of vibration frequency, treating capacity is every 550~750kg/h.
9. the gravity ore dressing method of particulate antimony oxide ore according to claim 5, it is characterised in that: the outstanding vibration conical surface choosing
The rotational frequency of mine machine is 10Hz, and 18~20Hz of vibration frequency, treating capacity is every 550~750kg/h.
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| CN108262155A (en) * | 2018-03-27 | 2018-07-10 | 中国恩菲工程技术有限公司 | The method for recycling particulate antimony oxide ore |
| CN108405172A (en) * | 2018-03-27 | 2018-08-17 | 中国恩菲工程技术有限公司 | The method for recycling particulate antimony oxide ore |
| CN108499722A (en) * | 2018-03-27 | 2018-09-07 | 中国恩菲工程技术有限公司 | The system for recycling particulate antimony oxide ore |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1374016A (en) * | 1972-09-25 | 1974-11-13 | Bleiberger Bergwerks Union Ag | Process and plant for dressing storage battery scrap |
| CN1117406A (en) * | 1995-04-25 | 1996-02-28 | 郑萍 | Gravity method for separation of zinc oxide ore |
| RU123689U1 (en) * | 2012-06-19 | 2013-01-10 | ООО "Хара-Шибирьский сурьмяной комбинат" | FLOW LINE FOR PROCESSING ANTIMONY GOLD-CONTAINING ORE |
| CN103691568A (en) * | 2013-12-17 | 2014-04-02 | 广西大学 | Micro-fine particle antimony oxide ore recycling method |
| CN104226463A (en) * | 2014-07-28 | 2014-12-24 | 蒙自矿冶有限责任公司 | Beneficiation method for high-tin-content multi-metal sulfide ores |
| CN104624389A (en) * | 2015-01-09 | 2015-05-20 | 临武县南方矿业有限责任公司 | Gravitation separation tailing cassiterite flotation method |
-
2016
- 2016-12-13 CN CN201611143175.3A patent/CN106391296B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1374016A (en) * | 1972-09-25 | 1974-11-13 | Bleiberger Bergwerks Union Ag | Process and plant for dressing storage battery scrap |
| CN1117406A (en) * | 1995-04-25 | 1996-02-28 | 郑萍 | Gravity method for separation of zinc oxide ore |
| RU123689U1 (en) * | 2012-06-19 | 2013-01-10 | ООО "Хара-Шибирьский сурьмяной комбинат" | FLOW LINE FOR PROCESSING ANTIMONY GOLD-CONTAINING ORE |
| CN103691568A (en) * | 2013-12-17 | 2014-04-02 | 广西大学 | Micro-fine particle antimony oxide ore recycling method |
| CN104226463A (en) * | 2014-07-28 | 2014-12-24 | 蒙自矿冶有限责任公司 | Beneficiation method for high-tin-content multi-metal sulfide ores |
| CN104624389A (en) * | 2015-01-09 | 2015-05-20 | 临武县南方矿业有限责任公司 | Gravitation separation tailing cassiterite flotation method |
Non-Patent Citations (3)
| Title |
|---|
| 东安锑矿难选氧化锑矿选矿试验研究;郑剑洪等;《矿业工程研究》;20090630;第24卷(第2期);第68-70页 |
| 低品位氧化锑矿回收新工艺研究与应用;张汉平等;《有色金属》;20060228(第1期);第1-5页 |
| 白钨精选尾矿综合回收钨、锡新工艺改造;肖文工等;《中国钨业》;20150630;第30卷(第3期);第14-17页 |
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