CN1108700A - Preparation method of crystal form rare earth carbonate - Google Patents
Preparation method of crystal form rare earth carbonate Download PDFInfo
- Publication number
- CN1108700A CN1108700A CN94110881A CN94110881A CN1108700A CN 1108700 A CN1108700 A CN 1108700A CN 94110881 A CN94110881 A CN 94110881A CN 94110881 A CN94110881 A CN 94110881A CN 1108700 A CN1108700 A CN 1108700A
- Authority
- CN
- China
- Prior art keywords
- rare earth
- crystal
- carbonated rare
- preparation
- additive
- 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.)
- Granted
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 belongs to a new process method in the field of rare earth extraction. It is characterized by that in the course of ore-leaching of ionic rare earth ore an additive is added, and the obtained leached mother liquor directly uses ammonium hydrogen carbonate as precipitant to prepare and extract crystal form rare earth carbonate. The invention can greatly reduce the production cost and overcome the problems of large volume, difficult filtration and purification before precipitation of the conventional rare earth carbonate. The product purity REO is more than 94 percent, and Al2O3Less than 0.3 percent, and the cost of the medicament is reduced by more than 60 percent compared with the cost of the oxalic acid process.
Description
The preparation method of crystal carbonated rare earth
What produce from ion type rareearth ore that crystal carbonated rare earth relates to is a kind of new processing method that rare earth extracts the field.
Ammonium sulfate maceration-oxalic acid precipitation-calcination explained hereafter rare earth oxide is adopted in the ion type rareearth mine usually.Make precipitation agent because oxalic acid costs an arm and a leg with oxalic acid, production cost is higher.Therefore people wish to obtain a kind of cheap, surrogate that market is easy to get, it is generally acknowledged that it is promising that bicarbonate of ammonia is used for the ion type rareearth ore precipitating rare earth as precipitation agent.But the sedimentary carbonated rare earth of ordinary method is amorphous flocks, and is bulky, and the dehydration difficulty contains assorted height, difficult quality guarantee, and before precipitation, need purification to remove aluminium, often reach 10%(in the loss of clean-up stage rare earth and see Chinese patent 86100671A).
Purpose of the present invention be exactly utilize bicarbonate of ammonia do precipitation agent from ion type rareearth, produce long-pending not quite, easily filter and precipitate before the crystal carbonated rare earth that need not purify.
Technical scheme of the present invention and preparation process are:
1) when the ammoniumsulphate soln maceration, add a kind of additive, aluminium is not leached, or the very fast hydrolysis again of aluminium of having been come out by leaching and being stored in the leached mud.This class additive can be the organic buffer agent, as acetate, urotropine etc.; Also can be inorganic salt, as molysite, ammonium salt, calcium salt or magnesium salts.The adding of this additive is leached rare earth does not have influence.Its process is: additive is sneaked in the ore of pond, or be dissolved in the soaking solution, the additive add-on is as the criterion with effluent liquid PH=5.0~6.0.
2) above-mentioned technology gained leach liquor is directly prepared crystal carbonated rare earth with bicarbonate of ammonia as precipitation agent.This process is divided into two steps, and promptly the preparation of crystal seed and crystalline duplicate.
Step 1: crystal seed preparation is under 10~50 ℃ temperature, with the REO in bicarbonate of ammonia (solid or solution) and the feed liquid by weight NH
4HCO
3The mixed of/REO=2~5:1, and control precipitated liquid PH stirred 0.5~60 minute between 6.5~8.5, treat mixing after room temperature leave standstill, ageing a couple of days, the crystal carbonated rare earth grows up to;
Step 2: crystal duplicate be crystal carbonated rare earth that step 1 is obtained as crystal seed, duplicate the carbonated rare earth crystal.It is identical that copy condition and method and crystal seed prepare, but at bicarbonate of ammonia and rare earth feed liquid blended simultaneously, need to add part and make crystal seed by the crystal of step 1 preparation.Crystal seed add-on (in REO) should be more than 1/4 of feed liquid rare earth.Digestion time 4~16 hours.This crystal that duplicates can be used as crystal seed and continues cycles prepare carbonated rare earth crystal.
Embodiment
The present invention carries out the technical scale experiment in certain rare-earth mineral, its main technical details and index such as following table:
Use this invented technology, reach 91% to the total recovery of carbonated rare earth, improve 5% than oxalic acid technology, reagent cost can reduce by 8000 yuan than oxalic acid technology rare earth oxide per ton.And, can calcination change into rare earth oxide and be directly used in the smelting separation because the solubility in acid of carbonated rare earth is good.
Claims (3)
1, by the method for producing crystal carbonated rare earth in the ion type rareearth ore, it is characterized in that: add a kind of additive when the ammoniumsulphate soln maceration, the mother liquor that is drawn directly duplicates with crystal seed and the crystalline thereof that ammonium hydrogencarbonate is produced crystal carbonated rare earth as precipitation agent.
2, according to the preparation method of the described crystal carbonated rare earth of claim 1; It is characterized in that: ammoniumsulphate soln soak that additive can be organic salt in the ore deposit, as acetate, urotropine, also can be inorganic salt, as molysite, ammonium salt, calcium salt or magnesium salts, the consumption of additive is as the criterion with effluent liquid PH=5.0~6.0;
3, according to the preparation method of the described crystal carbonated rare earth of claim 1, it is characterized in that: directly prepare crystal carbonated rare earth as precipitation agent and divide the preparation of crystal seed and crystalline to duplicate two steps, that is: with ammonium hydrogencarbonate
Under 10~50 ℃ temperature, by weight the mixed of 2~5:1, the pH value of control precipitated liquid is 6.5~8.5, stirs 0.5~60 minute with the REO in bicarbonate of ammonia and the feed liquid, and even room temperature afterwards to be mixed leaves standstill, ageing a couple of days grows up to the carbonated rare earth crystal;
The crystal that said process makes is made crystal seed, join and treat in the sedimentary leaching mother liquor, prepare the crystal carbonated rare earth crystal with the condition identical with aforesaid method, the crystal that ageing was duplicated after 4~16 hours can continue circulation combinations type carbonated rare earth as crystal seed again, and the add-on of each crystal seed only accounts for when time more than 1/4 of feed liquid rare earth.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN94110881A CN1042146C (en) | 1994-03-18 | 1994-03-18 | Preparation method of crystal form rare earth carbonate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN94110881A CN1042146C (en) | 1994-03-18 | 1994-03-18 | Preparation method of crystal form rare earth carbonate |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1108700A true CN1108700A (en) | 1995-09-20 |
CN1042146C CN1042146C (en) | 1999-02-17 |
Family
ID=5034798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN94110881A Expired - Fee Related CN1042146C (en) | 1994-03-18 | 1994-03-18 | Preparation method of crystal form rare earth carbonate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1042146C (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100457928C (en) * | 2007-03-22 | 2009-02-04 | 广东富远稀土新材料股份有限公司 | Carbonate deposition method of crystal type heavy rare earth |
CN102583493A (en) * | 2012-02-20 | 2012-07-18 | 甘肃稀土新材料股份有限公司 | Method for preparing large-particle Ce rich rare earth oxide |
CN103224248A (en) * | 2013-04-03 | 2013-07-31 | 南昌大学 | Method of preparing rare earth carbonate and recycling materials thereof |
CN103276440A (en) * | 2013-06-15 | 2013-09-04 | 清远市嘉禾稀有金属有限公司 | Processing method for rare earth carbonate with low chlorine ions |
CN103526014A (en) * | 2013-10-25 | 2014-01-22 | 武汉工程大学 | Method for leaching weathering crust eluvial type rare earth ore with aluminum inhibition |
CN107043122A (en) * | 2017-05-18 | 2017-08-15 | 赣州晨光稀土新材料股份有限公司 | A kind of continuous method for producing rare earth compound precipitation |
CN107188215A (en) * | 2017-05-24 | 2017-09-22 | 中国北方稀土(集团)高科技股份有限公司 | The method that reaction end is automatically adjusted in carbonated rare earth continuous precipitation production process |
CN115232992A (en) * | 2022-07-27 | 2022-10-25 | 中南民族大学 | Method for extracting rare earth from weathering crust leaching type rare earth ore by virtue of impurity suppression in stages |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1008082B (en) * | 1986-01-25 | 1990-05-23 | 江西大学 | Precipitating rare-earth by using ammonium bicarbonate |
CN1094380A (en) * | 1993-04-30 | 1994-11-02 | 甘肃稀土公司 | The method for preparing carbonated rare earth |
-
1994
- 1994-03-18 CN CN94110881A patent/CN1042146C/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100457928C (en) * | 2007-03-22 | 2009-02-04 | 广东富远稀土新材料股份有限公司 | Carbonate deposition method of crystal type heavy rare earth |
CN102583493A (en) * | 2012-02-20 | 2012-07-18 | 甘肃稀土新材料股份有限公司 | Method for preparing large-particle Ce rich rare earth oxide |
CN103224248A (en) * | 2013-04-03 | 2013-07-31 | 南昌大学 | Method of preparing rare earth carbonate and recycling materials thereof |
CN103224248B (en) * | 2013-04-03 | 2015-07-01 | 南昌大学 | Method of preparing rare earth carbonate and recycling materials thereof |
CN103276440A (en) * | 2013-06-15 | 2013-09-04 | 清远市嘉禾稀有金属有限公司 | Processing method for rare earth carbonate with low chlorine ions |
CN103276440B (en) * | 2013-06-15 | 2015-09-02 | 清远市嘉禾稀有金属有限公司 | A kind of low chlorine root rare earth carbonate working method |
CN103526014A (en) * | 2013-10-25 | 2014-01-22 | 武汉工程大学 | Method for leaching weathering crust eluvial type rare earth ore with aluminum inhibition |
CN107043122A (en) * | 2017-05-18 | 2017-08-15 | 赣州晨光稀土新材料股份有限公司 | A kind of continuous method for producing rare earth compound precipitation |
CN107188215A (en) * | 2017-05-24 | 2017-09-22 | 中国北方稀土(集团)高科技股份有限公司 | The method that reaction end is automatically adjusted in carbonated rare earth continuous precipitation production process |
CN115232992A (en) * | 2022-07-27 | 2022-10-25 | 中南民族大学 | Method for extracting rare earth from weathering crust leaching type rare earth ore by virtue of impurity suppression in stages |
CN115232992B (en) * | 2022-07-27 | 2023-07-18 | 中南民族大学 | Method for leaching rare earth in weathered crust leaching type rare earth ore by segmentation and impurity suppression |
Also Published As
Publication number | Publication date |
---|---|
CN1042146C (en) | 1999-02-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108642310B (en) | Method for removing aluminum from rare earth feed liquid by complexing precipitation | |
CN107190140B (en) | A method of recovering rare earth and aluminium from ion adsorption type rare earth ore | |
CN101597688A (en) | From phosphogypsum, reclaim a kind of method of rare earth | |
CN108342597B (en) | Method for decomposing scheelite by using hydrochloric acid with mother liquor circulation | |
CN104928475A (en) | Recycling method of rare earth-containing aluminum silicon waste material | |
US20200140974A1 (en) | Method of removing iron ions from a solution containing neodymium, praseodymium, dysprosium and iron | |
CN1042146C (en) | Preparation method of crystal form rare earth carbonate | |
CN104073634A (en) | Method for removing iron of nickel ore leaching liquid or electrolytic anode liquid | |
CN111634952A (en) | Method for preparing iron oxide red by using ferrous sulfate as byproduct of titanium dioxide, product and application | |
CN102912129A (en) | Method for recycling tungsten in liquids after tungsten smelting exchanges | |
CN114538486A (en) | Magnesium recovery method and system based on chlor-alkali salt mud | |
CN108977675B (en) | Method for preparing low-sulfur-content rare earth oxide by reverse feeding precipitation-staged roasting | |
CN108428893B (en) | Preparation method of brine lithium carbonate | |
CN113355538A (en) | Terbium oxide extraction process for treating ion ore by combining hydrochloric acid and organic extractant | |
RU2456358C1 (en) | Method of processing of phospho-gypsum | |
RU2674527C1 (en) | Method for extracting rare earth metals from productive solutions in sulfuric acid leaching of uranium ores | |
CN113249598B (en) | Method for complexing, separating and removing aluminum from rare earth feed liquid | |
CN1110328A (en) | Ionic type leaching impurity-removing precipitating process of rare-earth ore | |
CN114737069A (en) | Method for removing aluminum from ionic rare earth mine leachate | |
CN110615453B (en) | Method for directly preparing battery-grade lithium carbonate | |
CN115679131B (en) | Method for recovering rare earth from rare earth bioleaching solution through solution structure transformation | |
CN1120589A (en) | Carbonate method for conversion of sulfuric double salt of rareearth and separating cerium | |
CN1475443A (en) | Method of producing neutral high quality anhydrous sodium sulfate using natucal salt lake sodium sulfate decahydrate | |
CN115595458B (en) | Method for recovering rare earth from bioleaching solution through configuration conversion and self-precipitation of rare earth complex | |
CN110983054A (en) | Method for separating and recovering cobalt and nickel from manganese sulfate solution |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |