CN102600987B - Lithium oxide mineral separation collecting agent and application method thereof - Google Patents
Lithium oxide mineral separation collecting agent and application method thereof Download PDFInfo
- Publication number
- CN102600987B CN102600987B CN201210085129.8A CN201210085129A CN102600987B CN 102600987 B CN102600987 B CN 102600987B CN 201210085129 A CN201210085129 A CN 201210085129A CN 102600987 B CN102600987 B CN 102600987B
- Authority
- CN
- China
- Prior art keywords
- collecting agent
- soap
- lithia
- mineral separation
- lithium oxide
- 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
Landscapes
- Detergent Compositions (AREA)
Abstract
The invention relates to a lithium oxide mineral separation collecting agent and an application method thereof, in particular to a metal lithium oxide mineral separation collecting agent and a preparation method thereof, which are characterized in that the metal lithium oxide mineral separation collecting agent includes, by weight, from 40 to 55% of oxyparaffin soap, from 40 to 55% of sulfonated soap, from 10 to 20% of naphthenic acid and from 3 to 6% of active agent. The lithium oxide mineral separation collecting agent is fine in selectivity, the grade of concentration obtained by the aid of the collecting agent is higher than that of concentration obtained by the aid of an original collecting agent, the collecting agent is low-temperature-resistant and can be used for ore pulp without heating the ore pulp, when the collecting agent is used for the ore pulp at the temperature ranging from 11 DEG C to 15 DEG C, recycling rate of the collecting agent is increased about 6.5% as compared with the original collecting agent, and accordingly the collecting agent is low-temperature-resistant. Mineral separation cost can be greatly reduced, and the lithium oxide mineral separation collecting agent can be more widely applicable to raw ores with high argillization degree.
Description
Technical field
A kind of lithia mineral beneficiation collecting agent and using method, particularly a kind of collecting agent for the ore dressing of burning lithium minerals and preparation method thereof.
Background technology
The collecting agent that current domestic lithia ore deposit Mineral Processing Industry uses is mainly the series products taking oxidized paraffin wax soap and sulfonation soap as primary raw material, there is poor selectivity in such collecting agent, not low temperature resistant, to sludge sensitivity, the shortcomings such as concentrate grade is low, in ore dressing process, need ore pulp to carry out heat treated, power consumption is large, cost is high.And the current lithium mineral resources overwhelming majority is in the area of high height above sea level low temperature, lean ore is many, rich ore is few, difficult ore dressing is many, for ore-dressing technique has increased difficulty, not former collecting agent not low temperature resistant and just particularly outstanding to the sensitivity of sludge, cause lithium concentrate grade low, production process is unstable, and these difficult points make it be badly in need of at present a kind of can application in the invention of cryogenic conditions and selective good lithium ore deposit collecting agent.
Summary of the invention
Object of the present invention is exactly the deficiency existing for above-mentioned prior art, provides a kind of low temperature resistant, selectively good, to sludge insensitive lithia mineral beneficiation collecting agent and using method thereof.
The object of the invention is to be achieved through the following technical solutions.
A kind of lithia mineral beneficiation collecting agent, is characterized in that its components by weight percent comprises oxidized paraffin wax soap 40% ~ 55%, sulfonation soap 40% ~ 55%, aphthenic acids 10% ~ 20%, activating agent 3% ~ 6%.
A kind of lithia mineral beneficiation collecting agent of the present invention, is characterized in that described activating agent is a kind of or two or more in dodecyl sodium sulfate, sodium cetanesulfonate, DTAC.
The using method of a kind of lithia mineral beneficiation collecting agent of the present invention, it is characterized in that use procedure mixes in proportion oxidized paraffin wax soap, sulfonation soap, aphthenic acids and activating agent, add again water to stir evenly, then after heating, add again sodium hydroxide solution to be saponified into paste, be used further to ore dressing process.
The using method of a kind of lithia mineral beneficiation collecting agent of the present invention, is characterized in that its amount that adds water is 40% of oxidized paraffin wax soap, sulfonation soap, aphthenic acids and active agent intermixture total amount.
The using method of a kind of lithia mineral beneficiation collecting agent of the present invention, is characterized in that it adds the temperature heating after water is 100 ~ 130 DEG C, and the heat time is 2 hours.
The using method of a kind of lithia mineral beneficiation collecting agent of the present invention, is characterized in that its mass concentration that adds sodium hydroxide solution is 30% to carry out saponification, and saponification time is 2 hours.
A kind of lithia mineral beneficiation collecting agent of the present invention, collecting agent is selectively good, can obtain the concentrate grade higher than former collecting agent; Relatively low temperature resistant, can not heat ore pulp and use, in the time that 11 ~ 15 DEG C of slurry temperatures use, index is compared with former collecting agent, and the rate of recovery improves approximately 6.5%, and the feature that it is low temperature resistant has been described.Can greatly reduce beneficiation cost; The higher raw ore of argillization degree is had to adaptability widely.
Detailed description of the invention
A kind of lithia mineral beneficiation collecting agent, its components by weight percent comprises oxidized paraffin wax soap 35% ~ 50%, sulfonation soap 35% ~ 50%, aphthenic acids 10% ~ 25%, activating agent 3% ~ 6%.Use procedure mixes in proportion oxidized paraffin wax soap, sulfonation soap, aphthenic acids and activating agent, then adds water to stir evenly, and after then heating, then adds sodium hydroxide solution to be saponified into paste, is used further to ore dressing process.
Embodiment 1
Taking preparation 1000kg product of the present invention as example:
1. oxidized paraffin wax soap 350kg, sulfonation soap 500 kg, aphthenic acids 100kg, activator 50 kg its preparation methods are: oxidized paraffin wax soap, sulfonation soap, naphthenic soap, activator are poured into after weighing in heatable stirred autoclave, pour again clear water 400kg into, together be heated with stirring to thawing, 100 ~ 120 DEG C of temperature.
The sodium hydroxide solution that is 30% by mass concentration, slowly adds in reactor, weight approximately 500 kg;
3.after adding alkali reaction, become paste, this course of reaction is about 2 hours.New collector gets product.
Embodiment 2
Taking preparation 1000kg product of the present invention as example:
1. oxidized paraffin wax soap 500kg, sulfonation soap 350 kg, aphthenic acids 170kg, activator 30 kg its preparation methods are: oxidized paraffin wax soap, sulfonation soap, naphthenic soap, activator are poured into after weighing in heatable stirred autoclave, pour again clear water 400 kg into, together be heated with stirring to thawing, 100 ~ 120 DEG C of temperature.
The sodium hydroxide solution that is 30% by mass concentration, slowly adds in reactor, weight approximately 500 kg;
3.after adding alkali reaction, become paste, this course of reaction is about 2 hours.New collector gets product.
Embodiment 2
Taking preparation 1000kg product of the present invention as example:
1. oxidized paraffin wax soap 350kg, sulfonation soap 350kg, aphthenic acids 250kg, activator 50 kg its preparation methods are: oxidized paraffin wax soap, sulfonation soap, naphthenic soap, activator are poured into after weighing in heatable stirred autoclave, pour again clear water 500 kg into, together be heated with stirring to thawing, 100 ~ 120 DEG C of temperature.
The sodium hydroxide solution that is 30% by mass concentration, slowly adds in reactor, weight approximately 500 kg;
3.after adding alkali reaction, become paste, this course of reaction is about 2.5 hours.New collector gets product.
Collecting agent service condition of the present invention: this collecting agent and former collecting agent carry out the comparative result of lithium ore floatation as table
Medicine administered to bring out the cold agent Contrast on effect
Can be found out by table, the collecting agent of this patent invention in the time of flotation spodumene at relatively-high temperature: can obtain ratio
Agent, rate of recovery index high approximately 6.5%.
Claims (5)
1. a lithia mineral beneficiation collecting agent, is characterized in that its components by weight percent comprises oxidized paraffin wax soap 35% ~ 50%, sulfonation soap 35% ~ 50%, aphthenic acids 10% ~ 25%, activating agent 3% ~ 6%; Described activating agent is a kind of or two or more in dodecyl sodium sulfate, sodium cetanesulfonate, DTAC.
2. the using method of a kind of lithia mineral beneficiation collecting agent according to claim 1, it is characterized in that use procedure mixes in proportion oxidized paraffin wax soap, sulfonation soap, aphthenic acids and activating agent, add again water to stir evenly, then after heating, add again sodium hydroxide solution to be saponified into paste, be used further to ore dressing process.
3. the using method of a kind of lithia mineral beneficiation collecting agent according to claim 2, is characterized in that its amount that adds water is 40%～50% of oxidized paraffin wax soap, sulfonation soap, aphthenic acids and active agent intermixture total amount.
4. the using method of a kind of lithia mineral beneficiation collecting agent according to claim 2, is characterized in that it adds the temperature heating after water is 100 ~ 130 DEG C, and the heat time is 2～3 hours.
5. the using method of a kind of lithia mineral beneficiation collecting agent according to claim 2, is characterized in that it adds mass concentration is that 30% sodium hydroxide solution carries out saponification, and the time is 2～3 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210085129.8A CN102600987B (en) | 2012-03-28 | 2012-03-28 | Lithium oxide mineral separation collecting agent and application method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210085129.8A CN102600987B (en) | 2012-03-28 | 2012-03-28 | Lithium oxide mineral separation collecting agent and application method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102600987A CN102600987A (en) | 2012-07-25 |
| CN102600987B true CN102600987B (en) | 2014-06-11 |
Family
ID=46518972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210085129.8A Expired - Fee Related CN102600987B (en) | 2012-03-28 | 2012-03-28 | Lithium oxide mineral separation collecting agent and application method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102600987B (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102921559B (en) * | 2012-10-31 | 2014-11-05 | 中南大学 | Selective flotation collector for spodumene and application thereof |
| CN105013620B (en) * | 2015-06-25 | 2017-07-07 | 西南科技大学 | A kind of spodumene efficient combination collecting agent and its preparation method and application |
| CN106040437B (en) * | 2016-05-27 | 2018-08-21 | 四川省地质矿产勘查开发局成都综合岩矿测试中心 | Flotation collector for lithium-containing minerals and preparation method thereof |
| CN106583051B (en) * | 2016-12-23 | 2019-08-23 | 中国地质科学院矿产综合利用研究所 | Method for full-sludge flotation co-enrichment recovery of lithium niobium tantalum multi-metal resources |
| CN108057526A (en) * | 2017-12-27 | 2018-05-22 | 大连地拓环境科技有限公司 | A combined collector for improving the grade of potassium feldspar and its preparation method |
| CN110433958A (en) * | 2019-06-18 | 2019-11-12 | 中国地质科学院矿产综合利用研究所 | Niobium-tantalum-containing lithium polymetallic ore step non-tailing recovery process |
| CN110369146B (en) * | 2019-07-19 | 2020-09-25 | 中南大学 | Spodumene ore flotation collector, preparation method thereof and spodumene ore flotation method |
| CN113351373B (en) * | 2021-06-04 | 2023-05-12 | 中国地质科学院矿产综合利用研究所 | Floatation collector for diaspore ore and preparation method and application thereof |
| CN115709128A (en) * | 2022-10-31 | 2023-02-24 | 四川省有色矿冶科技有限公司 | Flotation method of spodumene ore |
| EP4389291A1 (en) | 2022-12-20 | 2024-06-26 | ArrMaz Products Inc. | Collector composition for lithium ore beneficiation |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3710934A (en) * | 1970-06-29 | 1973-01-16 | Canadian Patents Dev | Concentration of spodumene using flotation |
| KR100541465B1 (en) * | 2004-04-14 | 2006-01-11 | 한국지질자원연구원 | Redodolite Screening Method by Floating Screening |
| CN101181700A (en) * | 2007-12-17 | 2008-05-21 | 中国铝业股份有限公司 | Preparation method of hybrid collector for oxide ore flotation |
| CN101884954B (en) * | 2010-06-17 | 2012-11-14 | 新疆有色金属研究所 | Novel Li-Be flotation regulator and preparation method and using method thereof |
| CN102284373A (en) * | 2011-08-29 | 2011-12-21 | 江西理工大学 | Process for floating lepidolite |
-
2012
- 2012-03-28 CN CN201210085129.8A patent/CN102600987B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN102600987A (en) | 2012-07-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102600987B (en) | Lithium oxide mineral separation collecting agent and application method thereof | |
| CN104107762B (en) | Low-temperature-resistant collophanite reverse flotation collecting agent and preparation method thereof | |
| CN102247935B (en) | Ore dressing collector and preparation method thereof | |
| CN105537003B (en) | Drainage oil type collophanite reverse flotation collecting agent and preparation method thereof | |
| CN103350035B (en) | A collophosite positive flotation collector and preparation method thereof | |
| CN106076653B (en) | A kind of preparation method of modified fat acid type Collophane anti-floatation collector | |
| CN104741244B (en) | Silicon-calcium collophanite normal-temperature direct flotation collecting agent and preparation method thereof | |
| CN111672636A (en) | Spodumene ore flotation collector and preparation method and application method thereof | |
| CN103056036A (en) | Collophanite normal-temperature direct flotation collecting agent and preparation method thereof | |
| CN106179768A (en) | A kind of modified fat acid fluorite collector agent and preparation method thereof | |
| CN104056724A (en) | Reverse flotation collector for hematite and preparation and use method thereof | |
| CN106944263B (en) | A kind of Collophane anti-floatation collector and its preparation method and application method | |
| CN109369056A (en) | A kind of method of sodium sulphate content in reduction naphthalene series high-efficiency water-reducing agent | |
| CN105344492A (en) | Collophanite direct-reverse flotation collecting agent and preparation method and application thereof | |
| CN109772590B (en) | A kind of collector for magnesite flotation decalcification and its application | |
| CN105855063B (en) | The preparation method of anionic collector | |
| CN103920596B (en) | Collophanite combination flotation collector and preparation method and application thereof | |
| CN106269286A (en) | A kind of preparation method of alpha-sulfonated fatty acid phosphate reverse flotation collecting agent | |
| CN107140718A (en) | A kind of utilize couples the method that external field treatment red mud prepares iron aluminium flocculating agent | |
| CN109881019A (en) | A kind of method of resource utilization desulfurization slag containing vanadium | |
| Wu et al. | Removing boron from metallurgical grade silicon by a high basic slag refining technique | |
| CN104998761A (en) | Carbonate-type collecting agent reverse flotation drug and preparation method thereof | |
| CN102600985A (en) | Mineral separation collector and using method thereof | |
| CN106824546A (en) | A kind of magnesite ore puies forward the method that silicon drops in magnesium | |
| CN102921556A (en) | Iron ore reverse flotation mixed collector and preparation and application thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C53 | Correction of patent for invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Yan Zhiming Inventor after: Tang Xiaojun Inventor after: Guan Changping Inventor after: Zhou Yimei Inventor after: Chen Jinhua Inventor after: Dan Zhaogui Inventor after: Zheng Min Inventor before: Yan Zhiming Inventor before: Tang Xiaojun Inventor before: Guan Changping Inventor before: Zhou Yimei Inventor before: Chen Jinhua Inventor before: Zheng Min |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: YAN ZHIMING TANG XIAOJUN GUAN CHANGPING ZHOU YIMEI CHEN JINHUA ZHENG MIN TO: YAN ZHIMING TANG XIAOJUN GUAN CHANGPING ZHOU YIMEI CHEN JINHUA DAN ZHAOGUI ZHENG MIN |
|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140611 Termination date: 20170328 |