CN103484668A - Weathering crust illuviation-type rare-earth ore leaching agent and method for extracting rare earths by using same - Google Patents
Weathering crust illuviation-type rare-earth ore leaching agent and method for extracting rare earths by using same Download PDFInfo
- Publication number
- CN103484668A CN103484668A CN201310481335.5A CN201310481335A CN103484668A CN 103484668 A CN103484668 A CN 103484668A CN 201310481335 A CN201310481335 A CN 201310481335A CN 103484668 A CN103484668 A CN 103484668A
- Authority
- CN
- China
- Prior art keywords
- rare
- earth
- citrate
- ore
- leaching
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention provides a weathering crust illuviation-type rare-earth ore leaching agent and a method for extracting rare earths by using the same, particularly a leaching agent solution for weathering crust illuviation-type rare-earth ores. The active component is citrate, wherein the citrate is any one of ammonium citrate, sodium citrate, potassium citrate and magnesium citrate, or mixture of sodium citrate, potassium citrate and magnesium citrate. The method for extracting rare earths from weathering crust illuviation-type rare-earth ores comprises the following steps: leaching by using the citrate as the active component of the leaching agent to obtain a rare-earth leaching mother solution, removing impurities, and adding a precipitant to obtain a rare-earth enriched substance. In the weathering crust illuviation-type rare-earth extraction process, cation exchange interaction and anion (citrate ion) complex action exist, and the two actions can cooperate to enhance the rare-earth recovery rate and lower the concentration and consumption of the leaching agent.
Description
Technical field
The invention belongs to the hydrometallurgy field, be specifically related to a kind of method that weathered superficial leaching rare-earth ore soaks ore deposit agent and Extraction of rare earth thereof.
Background technology
Weathered superficial leaching rare-earth ore is a kind of special rare earth mineral, and middle heavy rare earths partition is high, is the strategic mineral of national development.The weathered superficial leaching rare-earth ore rare earth elements mainly is adsorbed on clay mineral with the form of hydration or hydroxyl hydrated ion, and the rare earth grade is low, is only 0.05~0.3%.Ore grain size is superfine, the rare earth more than 50% be stored in productive rate be 24~32%-the 0.78mm grade in, it is corresponding rare earth ore concentrate that conventional physical concentration can't make rare-earth enrichment, so can only adopt chemical leaching technology.
When weathered superficial leaching rare-earth ore is used the drip washing of salt electrolyte solution, rare earth ion will exchanged get off, and is similar to ion exchange process.No matter be highly basic, strong acid, salt of weak acid, strong acid weak base salt, high price salt or low price salt or organic acid, and can form the alkali of title complex with rare earth, when strength of solution is suitable, all can effectively leach the Ion Phase rare earth in weathered superficial leaching rare-earth ore.
In order to improve leaching efficiency, reduce resource consumption, reduce environmental pollution, realize the efficient utilization of weathered superficial leaching rare-earth resource, people start with from every side its leaching technology are improved, and wherein, the selection of soaking the ore deposit agent directly has influence on the height of leaching yield, produces required cost, therefore very important, be the problem of the current primary study of a lot of scientists.The ore deposit agent of soaking of generally using at present is generally 1~4% ammonium sulfate, has higher rare earth yield, but in south, produces lessly, and ore dressing of rare earth is very large to its demand, therefore usually cause that supply falls short of demand.Therefore, find a kind of alternative ammonium sulfate to soak the ore deposit agent very necessary.
Summary of the invention
The object of the invention is to provide a kind of new weathered superficial leaching rare-earth ore to soak the ore deposit agent, this Novel immersion ore deposit agent is in the process of leaching rare earth, not only exist cationic exchange interaction also to exist the cooperation of negatively charged ion to help the effect of soaking, soak the ore deposit agent with the ammonium sulfate generally used at present and compare, there are the characteristics of lower leaching concentration and less consumption.
For achieving the above object, adopt technical scheme as follows:
A kind of for weathered superficial leaching rare-earth ore soak the ore deposit agent solution, its activeconstituents is Citrate trianion.
Press such scheme, described Citrate trianion be ammonium citrate, Trisodium Citrate, Tripotassium Citrate and magnesium citrate any one or mix arbitrarily.
Press such scheme, described Citrate trianion active component content is 0.5-2.0wt%.
Press such scheme, the described ore deposit agent solution pH value of soaking is between 3.0-8.0.
A kind of from weathered superficial leaching rare-earth ore the method for Extraction of rare earth, comprise and use Citrate trianion to obtain rare earth leaching mother liquor as soaking ore deposit agent activeconstituents, removal of impurities, add precipitation agent to obtain rareearth enriching material.
Press such scheme, described Citrate trianion be ammonium citrate, Trisodium Citrate, Tripotassium Citrate and magnesium citrate any one or mix arbitrarily.
Press such scheme, described Citrate trianion active component content is 0.5-2wt%.
Press such scheme, also comprise and regulate the pH value to 3.0-8.0 to soaking the ore deposit agent solution.
Press such scheme, adopt hydrochloric acid while regulating the pH value.
Press such scheme, described precipitation agent is oxalic acid or bicarbonate of ammonia.
Weathered superficial leaching rare-earth ore leaching essence is an ion exchange reaction, the clay Rare Earth Ion with soak cationic exchange process in the agent of ore deposit.The chemical equation of ammonium sulfate when soaking the ore deposit agent is as follows:
[Al
4(Si
4O
10)(OH)
8]
m·nRE
3+ (s)+3nNH
4 + (aq)=[Al
4(Si
4O
10)(OH)
8]
m·3nNH
4 + (s)+nRE
(aq)
Thereby the exchange cation-adsorption occurs to mineral surface in the rare earth ion of leaching exchange cation and mineral surface, and rare earth ion enters in solution.Soak the ore deposit agent while being Citrate trianion when used, following chemical reaction occur:
[Al
4(Si
4O
10)(OH)
8]
m·nRE
3+ (s)+nC
6H
5O
7 3-+3nM
(aq)=[Al
4(Si
4O
10)(OH)
8]
m·3nM
(s)+nC
6H
5O
7REM=NH
4 +,Na
+,K
+,Mg
2+/2
From above reaction, in soaking the ore deposit process, the positively charged ion of citric acid has played the ion exchange with rare earth ion, and negatively charged ion (citrate ion) participates in the mating reaction of rare earth ion, having promoted to soak the ore deposit reaction carries out to the right, promote the leaching of rare earth, thereby improved rare earth yield.
Beneficial effect of the present invention is:
1) the present invention use in Citrate trianion a kind of or wherein several mixture as soaking the ore deposit agent, soaking the ore deposit agent with other of current use compares, in the process that weathered superficial leaching rare-earth extracts, except there being cationic exchange interaction also to have the mating reaction of negatively charged ion (citrate ion), two kinds of collaborative rare earth yields that can improve of effect reduce working concentration and the consumption that soaks the ore deposit agent.
2) Citrate trianion used, containing containing the ammonium root on a small quantity or not, can reduce ammonia nitrogen waste water and pollute, and can eliminate ammonia nitrogen waste water if use without ammonium salt and pollute.
Embodiment
Below in conjunction with example, the invention will be further described, but do not limit the present invention.
The mensuration of Ion Phase rare earth total content: the weathered superficial leaching rare-earth ore 250.0g that takes oven dry, the ammoniumsulphate soln that is 2% by mass percent is for soaking the ore deposit agent, weathered superficial leaching rare-earth ore is carried out to post to be soaked, until almost do not have rare earth to leach, merge and collect leaching liquid, the total Ion Phase content of rare earth of EDTA volumetric determination is the REO1.139mmol/250g rare-earth mineral.
Embodiment 1
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, the ammonium citrate ((NH that the preparation mass percent is 0.5%
4)
3c
6h
5o
7) solution is for soaking the ore deposit agent, ratio in solid-to-liquid ratio (solid masses with soak ore deposit agent volume ratio) 1:2, regulate flow rate control at 0.4mL/min, weathered superficial leaching rare-earth ore is carried out to post to be soaked, obtaining rare earth leaching mother liquor employing EDTA volumetric determination content of rare earth is the REO1.119mmol/250g rare-earth mineral, with the oxalate precipitation method enrichment, filter calcination under 900 ℃ of conditions after washing after removal of impurities.
Measure by analysis, rare earth yield be 94.3%(calcination thing directly weigh be recycled rate with total Ion Phase content of rare earth contrast), purity is that 92.6%(adopts GB/T14635-2008).
Embodiment 2
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, the magnesium citrate (Mg that the preparation mass percent is 1.5%
2(C
6h
5o
7)
3) solution is for soaking the ore deposit agent, add salt acid for adjusting pH to 5.0, ratio in solid-to-liquid ratio 1:2, regulate flow rate control at 0.4mL/min, weathered superficial leaching rare-earth ore is carried out to post to be soaked, obtaining rare earth leaching mother liquor, to adopt EDTA volumetric determination content of rare earth be the REO0.0962mmol/250g rare-earth mineral, after removal of impurities with the oxalate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, rare earth yield is 92.3%, and purity is 92.3%.
Embodiment 3
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, the Trisodium Citrate (Na that the preparation mass percent is 1.0%
3c
6h
5o
72H
2o) solution is for soaking the ore deposit agent, ratio in solid-to-liquid ratio 1:2, regulate flow rate control at 0.4mL/min, weathered superficial leaching rare-earth ore is carried out to post to be soaked, obtaining rare earth leaching mother liquor employing EDTA volumetric determination content of rare earth is the REO1.108mmol/250g rare-earth mineral, after removal of impurities with the ammonium bicarbonate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, rare earth yield is 93.4%, and purity is 92.1%.
Embodiment 4
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, the Tripotassium Citrate (K that the preparation mass percent is 1.0%
3c
6h
5o
7h
2o) solution is for soaking the ore deposit agent, ratio in solid-to-liquid ratio 1:2, regulate flow rate control at 0.4mL/min, weathered superficial leaching rare-earth ore is carried out to post to be soaked, obtaining rare earth leaching mother liquor employing EDTA volumetric determination content of rare earth is the REO1.110mmol/250g rare-earth mineral, after removal of impurities with the ammonium bicarbonate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, rare earth yield is 93.6%, and purity is 92.7%.
Embodiment 5
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, the following Citrate trianion that mixes of preparation soaks ore deposit agent (mass percent): 0.5% Trisodium Citrate, 0.5% Tripotassium Citrate, 0.5% magnesium citrate, all the other are water, adding the salt acid for adjusting pH is 7.3, ratio in solid-to-liquid ratio 1:2, regulate flow rate control at 0.4mL/min, weathered superficial leaching rare-earth ore is carried out to post to be soaked, obtaining rare earth leaching mother liquor employing EDTA volumetric determination content of rare earth is the REO1.111mmol/250g rare-earth mineral, after removal of impurities with the oxalate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, rare earth yield is 94.2%, and purity is 92.2%.
Embodiment 6
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, in the ratio of solid-to-liquid ratio 1:2, use respectively 1% ammonium sulfate and 1.28% ammonium citrate ((NH
4)
3c
6h
5o
7) solution is for soaking the ore deposit agent, consistent (the 0.151mol/L NH of ammonium ion content in two kinds of ammonium salts that this time use
4 +), weathered superficial leaching rare-earth ore is carried out to post and soaks, obtain rare earth leaching mother liquor and adopt EDTA volumetric determination content of rare earth, after removal of impurities with the oxalate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, ammonium sulfate leach liquor Rare-Earth Content is the REO0.9646mmol/250g rare-earth mineral, and rare earth yield is 81.3%, and purity is 92.3%; And ammonium citrate leach liquor Rare-Earth Content is the REO1.127mmol/250g rare-earth mineral, rare earth yield is 95.0%, and purity is 92.2%.
Embodiment 7
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, use respectively 2% Trisodium Citrate (Na in the ratio of solid-to-liquid ratio 1:2
3c
6h
5o
72H
2o) and 1.192% sodium chloride solution for soaking the ore deposit agent, the consistent (0.204mol/LNa of sodium ions content in two kinds of ammonium salts that this time use
+), weathered superficial leaching rare-earth ore is carried out to post and soaks, obtain rare earth leaching mother liquor and adopt EDTA volumetric determination content of rare earth, after removal of impurities with the oxalate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, Leaching of sodium chloride liquid Rare-Earth Content is the 0.3319mmol/250g rare-earth mineral, and rare earth yield is 28.1%, and purity is 92.6%; And ammonium citrate leach liquor Rare-Earth Content is the 1.126mmol/250g rare-earth mineral, rare earth yield is 94.9%, and purity is 92.3%.
Embodiment 8
Take the weathered superficial leaching rare-earth ore 250.0g of oven dry, in the ratio of solid-to-liquid ratio 1:2, use respectively 1.5% sal epsom and 1.88% magnesium citrate solution (Mg
2(C
6h
5o
7)
3) for soaking the ore deposit agent, two kinds that this time use are soaked consistent (the 0.125mol/L Mg of magnesium ion content in the agent of ore deposit
2+), weathered superficial leaching rare-earth ore is carried out to post and soaks, obtain rare earth leaching mother liquor and adopt EDTA volumetric determination content of rare earth, after removal of impurities with the oxalate precipitation method enrichment, calcination under 900 ℃ of conditions after filtration washing.
Measure by analysis, sal epsom leach liquor Rare-Earth Content is that 0.7393mmol/250g rare-earth mineral rare earth yield is 62.3%, and purity is 92.0%; And ammonium citrate leach liquor Rare-Earth Content is 1.112mmol/250g rare-earth mineral rare earth yield, be 93.7%, purity is 92.1%.
The result of example 6,7,8 can find out, when soaking ore deposit agent cation concn one regularly, the rare earth leaching yield that Citrate trianion soaks the ore deposit agent is higher, because citrate has promoted to soak with the mating reaction of rare earth ion the carrying out that react in ore deposit, has improved rare earth yield.
Claims (10)
- One kind for weathered superficial leaching rare-earth ore soak the ore deposit agent solution, it is characterized in that activeconstituents is Citrate trianion.
- As claimed in claim 1 for weathered superficial leaching rare-earth ore soak the ore deposit agent solution, it is characterized in that described Citrate trianion be ammonium citrate, Trisodium Citrate, Tripotassium Citrate and magnesium citrate any one or mix arbitrarily.
- As claimed in claim 1 for weathered superficial leaching rare-earth ore soak the ore deposit agent solution, it is characterized in that described Citrate trianion active component content is 0.5-2.0wt%.
- As claimed in claim 1 for weathered superficial leaching rare-earth ore soak the ore deposit agent solution, it is characterized in that the described ore deposit agent solution pH value of soaking between 3.0-8.0.
- 5. the method for an Extraction of rare earth from weathered superficial leaching rare-earth ore, comprise and use Citrate trianion to obtain rare earth leaching mother liquor as soaking ore deposit agent activeconstituents, and removal of impurities, add precipitation agent to obtain rareearth enriching material.
- 6. the method for Extraction of rare earth from weathered superficial leaching rare-earth ore as claimed in claim 5, it is characterized in that described Citrate trianion be ammonium citrate, Trisodium Citrate, Tripotassium Citrate and magnesium citrate any one or mix arbitrarily.
- 7. the method for Extraction of rare earth from weathered superficial leaching rare-earth ore as claimed in claim 5, is characterized in that described Citrate trianion active component content is 0.5-2wt%.
- 8. the method for Extraction of rare earth from weathered superficial leaching rare-earth ore as claimed in claim 5, characterized by further comprising and regulate the pH value to 3.0-8.0 to soaking the ore deposit agent solution.
- 9. the method for Extraction of rare earth from weathered superficial leaching rare-earth ore as claimed in claim 5, adopt hydrochloric acid while it is characterized in that regulating the pH value.
- 10. the method for Extraction of rare earth from weathered superficial leaching rare-earth ore as claimed in claim 5, is characterized in that described precipitation agent is oxalic acid or bicarbonate of ammonia.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310481335.5A CN103484668A (en) | 2013-10-15 | 2013-10-15 | Weathering crust illuviation-type rare-earth ore leaching agent and method for extracting rare earths by using same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310481335.5A CN103484668A (en) | 2013-10-15 | 2013-10-15 | Weathering crust illuviation-type rare-earth ore leaching agent and method for extracting rare earths by using same |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103484668A true CN103484668A (en) | 2014-01-01 |
Family
ID=49825257
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310481335.5A Pending CN103484668A (en) | 2013-10-15 | 2013-10-15 | Weathering crust illuviation-type rare-earth ore leaching agent and method for extracting rare earths by using same |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103484668A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103924105A (en) * | 2014-03-17 | 2014-07-16 | 赵书生 | Novel method for leaching rare earth |
CN104459083A (en) * | 2014-11-28 | 2015-03-25 | 武汉工程大学 | Mineral prospecting method for middle and heavy rare earth enrichment area of weathered crust elution-deposited rare earth ore |
CN104498738A (en) * | 2014-11-28 | 2015-04-08 | 武汉工程大学 | Method for leaching rare earth from weathering crust leaching type rare-earth ore heap |
CN104611547A (en) * | 2015-03-09 | 2015-05-13 | 龙南县锦易矿业有限公司 | Ore leaching process for south rare earth ore |
CN105331835A (en) * | 2015-10-11 | 2016-02-17 | 江西理工大学 | Auxiliary leaching agent applied to ion-absorbed rare earth ore leaching process and ore leaching method of auxiliary leaching agent |
CN105695741A (en) * | 2016-02-29 | 2016-06-22 | 中铝广西有色崇左稀土开发有限公司 | Ionic type rare earth mother solution treatment process |
CN108998663A (en) * | 2018-09-30 | 2018-12-14 | 许瑞高 | It is a kind of to leach ion adsorption type re technique with aluminum aluminum sulfate work leaching mine agent |
CN113025817A (en) * | 2021-03-09 | 2021-06-25 | 中南大学 | Method for extracting weathering crust elution-deposited rare earth ore |
CN113046554A (en) * | 2021-03-09 | 2021-06-29 | 中南大学 | Method for leaching weathering crust elution-deposited rare earth ore by using metabolite of microorganism |
CN113151697A (en) * | 2021-03-09 | 2021-07-23 | 中南大学 | Method for leaching weathering crust leaching type rare earth ore |
CN115181866A (en) * | 2022-07-25 | 2022-10-14 | 中南大学 | Combined leaching agent and application thereof in anode leaching |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101182597A (en) * | 2007-12-13 | 2008-05-21 | 东北大学 | Method of acidic extractant complexing extraction separation rare-earth element |
US20090272230A1 (en) * | 2008-05-02 | 2009-11-05 | Arafura Resources Limited | Recovery of Rare Earth Elements |
CN102747222A (en) * | 2012-07-20 | 2012-10-24 | 武汉工程大学 | Composite ammonium salt leaching agent for preventing landslide in in-situ leaching of ion absorpt deposit |
WO2012174454A1 (en) * | 2011-06-17 | 2012-12-20 | Vierheilig Albert A | Methods of recovering rare earth elements |
-
2013
- 2013-10-15 CN CN201310481335.5A patent/CN103484668A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101182597A (en) * | 2007-12-13 | 2008-05-21 | 东北大学 | Method of acidic extractant complexing extraction separation rare-earth element |
US20090272230A1 (en) * | 2008-05-02 | 2009-11-05 | Arafura Resources Limited | Recovery of Rare Earth Elements |
WO2012174454A1 (en) * | 2011-06-17 | 2012-12-20 | Vierheilig Albert A | Methods of recovering rare earth elements |
CN102747222A (en) * | 2012-07-20 | 2012-10-24 | 武汉工程大学 | Composite ammonium salt leaching agent for preventing landslide in in-situ leaching of ion absorpt deposit |
Non-Patent Citations (3)
Title |
---|
姚慧琴等: "用复合浸出剂浸取风化壳淋积型稀土矿中的稀土研究", 《江西科学》, vol. 23, no. 6, 31 December 2005 (2005-12-31) * |
尹敬群等: "从风化壳淋积型稀土矿浸取液提取稀土技术与发展", 《江西科学》, vol. 30, no. 5, 31 October 2012 (2012-10-31) * |
张臻悦等: "复合铵盐浸出风化壳淋积型稀土矿的研究", 《有色金属(冶炼部分)》, no. 4, 30 April 2013 (2013-04-30) * |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103924105A (en) * | 2014-03-17 | 2014-07-16 | 赵书生 | Novel method for leaching rare earth |
CN104459083A (en) * | 2014-11-28 | 2015-03-25 | 武汉工程大学 | Mineral prospecting method for middle and heavy rare earth enrichment area of weathered crust elution-deposited rare earth ore |
CN104498738A (en) * | 2014-11-28 | 2015-04-08 | 武汉工程大学 | Method for leaching rare earth from weathering crust leaching type rare-earth ore heap |
CN104459083B (en) * | 2014-11-28 | 2016-04-13 | 武汉工程大学 | The methods of prospecting for ore deposits of heavy rare earth enrichment region in a kind of weathered superficial leaching rare-earth ore |
CN104611547A (en) * | 2015-03-09 | 2015-05-13 | 龙南县锦易矿业有限公司 | Ore leaching process for south rare earth ore |
CN105331835B (en) * | 2015-10-11 | 2017-07-28 | 江西理工大学 | A kind of leaching agent and its leaching ore deposit method that ore deposit process is soaked applied to ion type rareearth ore |
CN105331835A (en) * | 2015-10-11 | 2016-02-17 | 江西理工大学 | Auxiliary leaching agent applied to ion-absorbed rare earth ore leaching process and ore leaching method of auxiliary leaching agent |
CN105695741A (en) * | 2016-02-29 | 2016-06-22 | 中铝广西有色崇左稀土开发有限公司 | Ionic type rare earth mother solution treatment process |
CN108998663A (en) * | 2018-09-30 | 2018-12-14 | 许瑞高 | It is a kind of to leach ion adsorption type re technique with aluminum aluminum sulfate work leaching mine agent |
CN113025817A (en) * | 2021-03-09 | 2021-06-25 | 中南大学 | Method for extracting weathering crust elution-deposited rare earth ore |
CN113046554A (en) * | 2021-03-09 | 2021-06-29 | 中南大学 | Method for leaching weathering crust elution-deposited rare earth ore by using metabolite of microorganism |
CN113151697A (en) * | 2021-03-09 | 2021-07-23 | 中南大学 | Method for leaching weathering crust leaching type rare earth ore |
CN113025817B (en) * | 2021-03-09 | 2021-12-31 | 中南大学 | Method for extracting weathering crust elution-deposited rare earth ore |
CN113046554B (en) * | 2021-03-09 | 2022-03-11 | 中南大学 | Method for leaching weathering crust elution-deposited rare earth ore by using metabolite of microorganism |
CN115181866A (en) * | 2022-07-25 | 2022-10-14 | 中南大学 | Combined leaching agent and application thereof in anode leaching |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103484668A (en) | Weathering crust illuviation-type rare-earth ore leaching agent and method for extracting rare earths by using same | |
CN102220488B (en) | Method for separating rare earth from phosphate ore | |
CN103266224B (en) | A kind of ion adsorption type re extracting method | |
CN106367622B (en) | It is a kind of using aluminum sulfate as the ion adsorption type re efficient green extracting method of leaching agent | |
CN102876890A (en) | Method for recovering uranium from beryllium uranium ore with wet process | |
CN102732731B (en) | Method for extracting valuable metals and refining zinc sulphate monohydrate from zinc-containing waste material | |
CN111926180A (en) | Method for extracting ion adsorption type rare earth | |
CN103789552B (en) | Method for recovering rhenium from high-temperature alloy pickle liquor | |
CN103436720A (en) | Process for leaching rare earth from ion-adsorption type rare earth ore without using ammonium salt | |
CN103320628A (en) | Method for reducing acid consumption by concentrated acid aging method in process of leaching vanadium from navajoite | |
CN103436715B (en) | Method of extracting vanadium from stone coal | |
CN104018012A (en) | Method of extracting gallium from aluminum chloride solution | |
CN101260467A (en) | Method for purifying and enriching low-concentration vanadium-containing water solution | |
CN105200233A (en) | Method for recovering manganese and magnesium from manganese electrolysis anode liquid | |
CN104962739A (en) | Quick impurity removing method for rare earth leach liquor of weathering crust elution-deposited rare earth ores | |
CN103643256A (en) | Deep purification method for manganese sulfate solution in manganese metal production | |
CN110372038A (en) | A kind of method of raw material containing manganese preparation LITHIUM BATTERY manganese sulfate and its LITHIUM BATTERY manganese sulfate of preparation | |
CN104073634A (en) | Method for removing iron of nickel ore leaching liquid or electrolytic anode liquid | |
CN109022835A (en) | The method without rare earth in ammonium rare earth mother solution is recycled in precisely removal of impurities fractional precipitation | |
CN101289703A (en) | Process for extracting vanadium form oxygen tension pickle liquor of high ferro vanadium-containing stone coal | |
CN105731513B (en) | The method for producing rare earth oxide containing rare earth phosphate rock with regeneration phosphoric acid leaching | |
CN105161746A (en) | Method for preparing vanadium battery electrolyte from acid vanadium-enriched liquid | |
CN102925681A (en) | Method for separating valuable components of monazite slags | |
CN103243226A (en) | Method for preparing rare earth concentrate from low-grade light rare earth tailings | |
CN100392122C (en) | Method for extracting gold (I) from enriched alkaline cyanide gold immersing liquid |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140101 |