CN105435956B - A kind of method that falcon centrifugal reselections are combined recycling wulfenite with flotation - Google Patents
A kind of method that falcon centrifugal reselections are combined recycling wulfenite with flotation Download PDFInfo
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- CN105435956B CN105435956B CN201610001937.XA CN201610001937A CN105435956B CN 105435956 B CN105435956 B CN 105435956B CN 201610001937 A CN201610001937 A CN 201610001937A CN 105435956 B CN105435956 B CN 105435956B
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- wulfenite
- flotation
- falcon
- centrifugal
- molybdenum
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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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- 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
-
- 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
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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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/04—Frothers
-
- 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; specified applications
- B03D2203/02—Ores
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Abstract
The invention discloses a kind of method that falcon centrifugal reselections are combined recycling wulfenite with flotation, it is that raw ore is milled to the fineness that 0.074mm accounts for 70%~80% so that wulfenite is dissociated with gangue mineral;Sorted using falcon centrifugal ore separators, obtain wulfenite gravity concentrate;Sulfuric acid cleaned mineral, vulcanized sodium activation wulfenite in terms of centrifugation tailing per ton, will be sequentially added after falcon centrifugal reselection Tailing thickenings, then add collecting agent and foaming agent 730A effects carry out flotation wulfenite, scrape foam and obtain wulfenite flotation concentrate;The method of the present invention is generally applicable to wulfenite and is separated with gangue mineral, falcon centrifugal ore separators can more effectively recycle the wulfenite of Li Du≤10 micron, and flotation can be with the wulfenite of 10 microns of recovery size ﹤, so as to greatly improve the rate of recovery of wulfenite.
Description
Technical field
The invention belongs to mineral separation technical field, and in particular to one kind is combined using falcon centrifugal reselections with flotation
Technique recycling wulfenite method.
Background technology
Molybdenum is a kind of important rare metal, and tool has been widely used:With China's expanding economy, to bases such as steels
The demand of material is more and more, production various steel alloy, cast steel, tool steel and stainless steels etc. is widely used in, to strengthen steel
Intensity, toughness and corrosion resistance;Molybdenum oxide and molybdate are the excellent catalysts in chemistry and petroleum industry;As molybdenum is other
The application of alloy field and chemical field also constantly expands, also increasing to the demand of molybdenum, therefore improves the ore dressing of Molybdenum Mine
Level, improves the comprehensive utilization ratio of Mo resource, provides high-quality molybdenum product more, keeps economic sustainable and stable development to have in China important
Meaning.Present molybdenum is mainly what is extracted from sulphide ore, but oxidizing molybdenum ore is also the important sources of molybdenum, and wulfenite is also known as molybdenum lead
Ore deposit, yellow lead ore, are the important sources for extracting molybdenum, and since it is than great, native floatability is poor, commonly use gravity treatment or sulphur
Change flotation to be sorted.But though traditional gravitational separation equipment such as spiral chute, shaking table etc. can effectively recycle larger particles ore deposit
Stone, is but difficult to recycle the smitham in ore, causes recovery rate in ore-dressing low;Traditional sulfide flotation method, can only also sort can
The good wulfenite of buoyancy.Therefore in order to improve the dressing level of wulfenite, accelerate the utilization of such ore, just have very much
Necessity researches and develops a kind of ore-dressing technique of more efficient wulfenite.
The content of the invention
The present invention's is to provide a kind of technique recycling wulfenite being combined using falcon centrifugal reselections with flotation
Method.
The purpose of the present invention is realized by following proposal:
1. raw ore is milled to the fineness that -0.074mm accounts for 70%~80% so that wulfenite is dissociated with gangue mineral;
2. use falcon centrifugal ore separators in recoil water flow for 2600~3200ml/min, 220~300g of centrifugal force
Under conditions of sorted, obtain wulfenite gravity concentrate;
3. falcon centrifugal reselection Tailing thickenings are dehydrated to the concentration of mass percent 30%~35%;
4. in terms of centrifugation tailing per ton, 260~500g sulfuric acid cleaned mineral surfaces, 2~4min, 1500~3000g sulphur are added
Change sodium activation 3~6min of wulfenite, then add 100~250g of collecting agent isoamyl xanthate and foaming agent 730A40~50g
1~2min of effect carrys out flotation wulfenite, scrapes foam and obtains wulfenite flotation concentrate.
Advantages of the present invention and technique effect:
The wulfenite of Li Du≤10 micron can be more effectively recycled using centrifugal ore separator falcon, and flotation can return
The wulfenite of 10 microns of granularity ﹤ is received, the combination of both can greatly improve the rate of recovery of wulfenite.
Embodiment
With reference to embodiment, the present invention is further illustrated, but the present invention must not be limited in any way
System, based on present invention teach that any changes and modifications made, belong to protection scope of the present invention.
As shown in the Examples:1. raw ore is milled to the fineness that -0.074mm accounts for 70%~80% by the present invention so that wulfenite
Dissociated with gangue mineral;2. use falcon centrifugal ore separators(Model falcon-SB40)Recoil water flow for 2600~
Sorted under conditions of 3200ml/min, 220~300g of centrifugal force, obtain wulfenite gravity concentrate;3. by falcon from
The thickening of heart gravity tailings to mass percent 30%~35% concentration;4. in terms of centrifugation tailing per ton, sequentially add 260~
2~4min of 500g sulfuric acid cleaned mineral surfaces, 1500~3000g vulcanized sodium activation 3~6min of wulfenite, then add collecting
100~250g of agent isoamyl xanthate and foaming agent 730A40~50g acts on 1~2min and carrys out flotation wulfenite, scrapes foam i.e.
Obtain wulfenite flotation concentrate.
Embodiment 1
By taking Henan Province's wulfenite sample as an example, which is milled to -0.074mm and accounts for 75% fineness, makes wulfenite and gangue
Dissociation, obtains containing molybdenum through falcon after centrifugal reselection under the conditions of recoil water flow is 2700mL/min, potential of centrifugal force 240g
8.62%, molybdenum recovery is also up to 62.76% gravity treatment molybdenum concntrate, and the ore pulp of falcon centrifugal reselections Tailing thickening to 30% is dense
When spending, in terms of centrifugation tailing per ton, 260g sulfuric acid cleaned mineral surfaces 2min, 1600g vulcanized sodium activation wulfenite are added
3min, then adds collecting agent isoamyl xanthate 150g and foaming agent 730A40g effects 1min and carrys out flotation wulfenite, obtain
Contain molybdenum 20.25%, molybdenum recovery 18.52% in flotation concentrate, the total rate of recovery of molybdenum has been recycled in sample ore well up to 81.28%
Molybdenum.
Embodiment 2
By taking Shaanxi Province's wulfenite sample as an example, which is milled to -0.074mm and accounts for 70% fineness, makes wulfenite and gangue
Dissociation, obtains containing molybdenum through falcon after centrifugal reselection under the conditions of recoil water flow is 2900mL/min, potential of centrifugal force 260g
10.25%, molybdenum recovery is also up to 65.45% gravity treatment molybdenum concntrate, and the ore pulp of falcon centrifugal reselections Tailing thickening to 33% is dense
When spending, in terms of centrifugation tailing per ton, 500g sulfuric acid cleaned mineral surfaces 4min, 2800g vulcanized sodium activation wulfenite are added
5min, then adds collecting agent isoamyl xanthate 220g and foaming agent 730A50g effects 2min and carrys out flotation wulfenite, obtain
Contain molybdenum 19.32%, molybdenum recovery 14.63% in flotation concentrate, the total rate of recovery of molybdenum has been recycled in sample ore well up to 80.08%
Molybdenum.
Embodiment 3
By taking Jiangxi Province's wulfenite sample as an example, which is milled to -0.074mm and accounts for 80% fineness, makes wulfenite and gangue
Dissociation, obtains containing molybdenum through falcon after centrifugal reselection under the conditions of recoil water flow is 2600mL/min, potential of centrifugal force 220g
7.83%, molybdenum recovery is also up to 63.29% gravity treatment molybdenum concntrate, and the ore pulp of falcon centrifugal reselections Tailing thickening to 30% is dense
When spending, in terms of centrifugation tailing per ton, 400g sulfuric acid cleaned mineral surfaces 2min, 3000g vulcanized sodium activation wulfenite are added
6min, then adds collecting agent isoamyl xanthate 250g and foaming agent 730A50g effects 2min and carrys out flotation wulfenite, obtain
Contain molybdenum 18.31%, molybdenum recovery 18.78% in flotation concentrate, the total rate of recovery of molybdenum has been recycled in sample ore well up to 82.07%
Molybdenum.
Embodiment 4
By taking Shandong Province's wulfenite sample as an example, which is milled to -0.074mm and accounts for 70% fineness, makes wulfenite and gangue
Dissociation, obtains containing molybdenum through falcon after centrifugal reselection under the conditions of recoil water flow is 3200mL/min, potential of centrifugal force 300g
11.32%, molybdenum recovery is also up to 59.44% gravity treatment molybdenum concntrate, and the ore pulp of falcon centrifugal reselections Tailing thickening to 33% is dense
When spending, in terms of centrifugation tailing per ton, 350g sulfuric acid cleaned mineral surfaces 4min, 2500g vulcanized sodium activation wulfenite are added
4min, then adds collecting agent isoamyl xanthate 200g and foaming agent 730A40g effects 1min and carrys out flotation wulfenite, obtain
Contain molybdenum 16.32%, molybdenum recovery 17.33% in flotation concentrate, the total rate of recovery of molybdenum has been recycled in sample ore well up to 76.77%
Molybdenum.
Embodiment 5
By taking Jilin Province's wulfenite sample as an example, which is milled to -0.074mm and accounts for 80% fineness, makes wulfenite and gangue
Dissociation, obtains containing molybdenum through falcon after centrifugal reselection under the conditions of recoil water flow is 3100mL/min, potential of centrifugal force 270g
10.63%, molybdenum recovery is also up to 58.84% gravity treatment molybdenum concntrate, and the ore pulp of falcon centrifugal reselections Tailing thickening to 35% is dense
When spending, in terms of centrifugation tailing per ton, 300g sulfuric acid cleaned mineral surfaces 3min, 1500g vulcanized sodium activation wulfenite are added
3min, then adds collecting agent isoamyl xanthate 100g and foaming agent 730A40g effects 1min and carrys out flotation wulfenite, obtain
Contain molybdenum 15.21%, molybdenum recovery 16.10% in flotation concentrate, the total rate of recovery of molybdenum has been recycled in sample ore well up to 74.94%
Molybdenum.
Claims (1)
1. a kind of falcon centrifugal reselections with flotation be combined recycling wulfenite method, it is characterised in that as follows into
OK:
1. raw ore is milled to the fineness that -0.074mm accounts for 70%~80% so that wulfenite is dissociated with gangue mineral;
2. use falcon centrifugal ore separators in recoil water flow for 2600~3200mL/min, the bar of 220~300g of centrifugal force
Sorted under part, obtain wulfenite gravity concentrate;
3. falcon centrifugal reselection Tailing thickenings are dehydrated to the concentration of mass percent 30%~35%;
4. in terms of centrifugation tailing per ton, 260~500g sulfuric acid cleaned mineral surfaces, 2~4min, 1500~3000g sulphur are sequentially added
Change sodium activation 3~6min of wulfenite, then add 100~250g of collecting agent isoamyl xanthate and foaming agent 730A40~50g
1~2min of effect carrys out flotation wulfenite, scrapes foam and obtains wulfenite flotation concentrate.
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CN110038718B (en) * | 2019-04-19 | 2021-03-26 | 赣州金环磁选设备有限公司 | Process for efficiently separating micro-fine tungsten ore by using centrifugal machine and flotation |
CN114405657B (en) * | 2022-01-04 | 2022-09-27 | 长沙矿山研究院有限责任公司 | Method for separating molybdenite and galena through gravity-flotation combination |
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CN101134180A (en) * | 2007-10-11 | 2008-03-05 | 广西大学 | High iron pelitization wulfenite floatation method |
CN104209183A (en) * | 2014-08-30 | 2014-12-17 | 广东省工业技术研究院(广州有色金属研究院) | Beneficiation method for color molybdenum lead ores |
CN104772217A (en) * | 2015-04-22 | 2015-07-15 | 昆明冶金研究院 | Flotation separation process for mixed copper and lead concentrate |
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