CN101264933A - Deep purification method for removing micro-tungsten from high-concentration molybdenate solution - Google Patents
Deep purification method for removing micro-tungsten from high-concentration molybdenate solution Download PDFInfo
- Publication number
- CN101264933A CN101264933A CNA2008100310515A CN200810031051A CN101264933A CN 101264933 A CN101264933 A CN 101264933A CN A2008100310515 A CNA2008100310515 A CN A2008100310515A CN 200810031051 A CN200810031051 A CN 200810031051A CN 101264933 A CN101264933 A CN 101264933A
- Authority
- CN
- China
- Prior art keywords
- tungsten
- solution
- concentration
- molybdenate
- resin
- 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
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
A method for completely cleaning high concentration molybdate solution by removing trace tungsten comprises the steps of pre-adjusting pH value of molybdate solution containing trace tungsten, allowing tungstate ions to completely polymerize to form polytungstate ions, and performing selective adsorption of tungsten with adsorption bed filled with macroporous weak base anion exchange resin, so as to completely remove tungsten from molybdate solution.
Description
Technical field
The present invention relates to a kind of from molybdate solution the degree of depth separate the ion exchange process of low levels tungsten.
Background technology
The processing characteristics of molybdenum goods and electricity, change, physicals are limited by impurity component content in the metal molybdenum to a great extent, and the influence of elemental tungsten is particularly outstanding.In order to obtain to have the molybdenum goods of excellent properties, must prepare high-purity molybdenum intermediate compound, as ammonium paramolybdate, ammonium tetramolybdate or ammonium dimolybdate.In the detrimental impurity element, the most difficult deep purifying surely belongs to normal and the symbiotic elemental tungsten of molybdenum.Because of tungsten and molybdenum are similar element, physico-chemical property is extremely close, and in weak acidic medium, can generate the heteropolyacid radical ion each other, therefore, separates micro-tungsten and have suitable difficulty from the magnanimity molybdenum.
At present, the comparatively deep method of research of separating micro-tungsten from molybdate solution is a hydrous metal oxides absorption tungsten, existing industrial application, but fail to put it over because of the deficiency of method self, therefore domestic most molybdate manufacturer does not have the technology of micro-tungsten deep purifying.Research separates micro-tungsten from the magnanimity molybdenum excellent technology is the task of top priority.
Summary of the invention
Purpose of the present invention aims to provide removes micro-tungsten a kind of the separation from the magnanimity molybdenum, and effective, and technology is simple, and is reliable and stable, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution that can not pollute
The objective of the invention is to realize by following manner:
Method of the present invention is: (1) pre-treatment: molybdate solution is added mineral acid, adjust pH value of solution value to 7.0～8.5, and deposited 5-12 hour; (2) will be through pretreated molybdate solution at the uniform velocity by the adsorption bed of anionite-exchange resin be housed, remove tungsten adsorption process duration of contact in the molybdate solution between 30～120min, continuously feeding is to WO
3Leakage is the absorption terminal point.
Molybdenum content range in the molybdate solution is 50～250g/l, and the mass ratio of tungstic oxide and molybdenum is 5 * 10
-4～2 * 10
-2
The preferred macroporous type weak base anion-exchange resin of described anionite-exchange resin is Cl when resin uses
-Type.
Negative tungsten resin is resolved with basic solution, and the sodium salt system is resolved with 1～2mol/lNaOH solution, and the ammonium salt system is resolved with the ammoniacal liquor of 5～6mol/l.
Resin after the parsing, the HCl solution regeneration with 4～6%, and water washing is used for next round absorption to fluid pH=3～5.
Its specific implementation process of technology of the present invention is:
1, the pre-treatment of solution: molybdate solution slowly adds mineral acid under agitation condition, adjust pH value of solution value to 7.0～8.5, make wolframate radical be condensed into isopoly-acid root heavy ion, and molybdenum is still existed with the unit molecule form, general sodium molybdate solution can be used hydrochloric acid, ammonium molybdate solution can be used nitric acid, and the molybdate solution that the pH value is adjusted to the right place was deposited 5-12 hour or heated a little to shorten the shelf-time.
2, anionite-exchange resin after the pre-treatment, changes into Cl routinely
-Type, transformation process should carry out in exchange column.The resin that is used to exchange except that tungsten is the macroporous type weak base anion-exchange resin, washes with water to fluid pH3～5 stand-by with the resin of 4-6%HCl after transition.
3, absorption removes tungsten: through the good molybdate solution of pre-treatment, at the uniform velocity pass through to load Cl with certain flow velocity
-The exchange bed of type macroporous weakly basic anion exchange resin, (Q is L/min) by the resin volume (V that exchanges cot loading for the absorption flow velocity
R, L) and absorption duration of contact (T, min) determine i.e. Q=V
R/ T removes tungsten adsorption process scope duration of contact between 30～120min from the molybdate solution of the low tungsten of high molybdenum, continuously feeding is to WO
3Leakage is the absorption terminal point, and liquid leaks to wear to press to purify and requires and decide for purify removing the tungsten qualifying liquid after the friendship of collection, looks the concentration and the scavenging solution WO of tungsten in the feed liquid
3/ Mo (mass ratio) controls requirement, and each exchanging operation can be handled the feed liquid of 10～30 times of resin bed volumes.
4, the desorb of tungsten (molybdenum): very easily from loaded resin, tungsten is resolved fully with basic solution, the sodium salt system is resolved agent with 1～2mol/lNaOH solution, the ammonium salt system is resolved with the ammoniacal liquor of 5～6mol/l, and the molybdenum that is adsorbed with tungsten loses (recyclable).For dropping into below 4% of total molybdenum amount
Resin regeneration; Resin after the parsing is washed with water to fluid pH=3～5 subsequently and is used for next round absorption with the HCl solution regeneration of the 4-6% of about 3 times of resin volumes.
It is ion exchange process that the present invention studies successful technology.In the tungstenic molybdate solution, impurity tungsten and magnanimity molybdenum generate the minute differences of isopoly-acid salt condition and select suitable ion exchange resin, and the tungsten preferentially adsorbed has obtained the effect of degree of depth separating tungsten.Tungstenic reaches 1% molybdate solution of the mass ratio of molybdenum (tungsten with) is after the degree of depth is separated, and tungsten is many ammonium molybdates of making of technology routinely, and W content can be reduced to below 0.02%.
The present invention is by means of making the tungsten polymerization generate the isopoly-acid radical ion under weak base and neutral medium condition, and molybdenum still exists with single molybdenum acid ion form basically, select suitable anionite-exchange resin, the many tungstate ions of energy preferentially adsorbed reach the isolating purpose of molybdenum tungsten under the situation that a large amount of molybdenums exist.This technology is suitable for separating tungsten from ammonium molybdate that contains a small amount of tungsten or sodium molybdate solution, and the molybdenum content range in the solution is 50～250g/l, and the mass ratio of tungstic oxide and molybdenum is 5 * 10
-4～2 * 10
-2,
The advantage of this technology is:
1, technology is simple, need not special reagent, reduced investment.
2, compare with inorganic adsorbent absorption tungsten, this technology is not introduced the chemical reagent that contains harmful impurity element, can not cause the pollution to the molybdenum the finished product because of the adding that removes the tungsten operation.
3, the convenient use, the different many ammonium molybdates manufacturer of raw material different process all is easy to use, and inserts before many ammonium molybdates of precipitated crystal operation and removes the tungsten exchanging operation just, and former technology can not done any change.
4, effective, reliable and stable except that tungsten, reach 1% ammonium molybdate solution as handling tungsten and molybdenum mass ratio, the tungsten ratio of an exchange process scavenging solution can be reduced to below 0.04%, and co-adsorption molybdenum amount belongs to recyclable loss below 4%.
Embodiment
Be described further from molybdate solution, purifying the exchange process that removes tungsten below in conjunction with embodiment.
Embodiment 1
Raw material is that molybdenum glance calcining ammonia leaching solution is through (NH
4)
2Ammonium molybdate solution behind the S purification and impurity removal behind concentrated nitric acid adjustment pH to 8.0, contains molybdenum 121.73g/l in the solution, tungstic oxide 1.379g/l, polymeric adsorbent are macroporous weakly basic anion exchange resin (numbering S
18), adsorbing on the post, exchange column Φ 20 * 250mm by liquid after the friendship after 8 times of resin bed volume feed liquids, contains molybdenum 121.73g/l 80 minutes duration of contact, tungstic oxide 0.101g/l, this moment, the clearance of tungstic oxide was 92.5%.
Embodiment 2
Stock liquid is with embodiment 1, and pH=7.5 contains molybdenum 120.71g/l in the liquid before handing over, and tungstic oxide 1.371g/l, polymeric adsorbent are macroporous weakly basic anion exchange resin (numbering 8
63), adsorb exchange column Φ 20 * 250mm on the post, 60 minutes duration of contact, preceding ten times of resin bed volume flow fluid tungstic oxide mean concnss are 0.054g/l, and the clearance of tungstic oxide can reach 96%, by the ammonium molybdate crystallization that this mixed solution acid settles out, W content is 0.0156%.
Embodiment 3
Ammonium molybdate crystal with ammonia solvent after, adjust pH value of solution value to 7.2, ammonium molybdate solution (molybdenum 120.7g/l, tungstic oxide 0.174g/l,) adsorb except that tungsten, adsorption column and resin are with embodiment 2, and be 40 minutes the duration of contact of absorption, preceding 21 times of resin bed volume flow fluid tungstic oxide mean concnss are 0.016g/l, and the tungstic oxide clearance is 90.8%.
Claims (6)
1, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution is characterized in that, (1) pre-treatment: molybdate solution is added mineral acid, adjust pH value of solution value to 7.0～8.5, and deposited 5-12 hour; (2) will be through pretreated molybdate solution at the uniform velocity by the adsorption bed of anionite-exchange resin be housed, remove tungsten adsorption process duration of contact in the molybdate solution between 30～120min, continuously feeding is to WO
3Leakage is the absorption terminal point.
2, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution according to claim 1,, it is characterized in that the molybdenum content range in the molybdate solution is 50～250g/l, the mass ratio of tungstic oxide and molybdenum is 5 * 10
-4～2 * 10
-2
3, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution according to claim 1,, it is characterized in that molybdate solution comprises ammonium molybdate solution and sodium molybdate solution.
4, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution according to claim 1,, it is characterized in that described anionite-exchange resin is the macroporous type weak base anion-exchange resin, when using, resin is Cl
-Type.
5, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution according to claim 1,, it is characterized in that negative tungsten resin is resolved with basic solution, the sodium salt system is resolved with 1～2mol/lNaOH solution, and the ammonium salt system is resolved with the ammoniacal liquor of 5～6mol/l.
6, a kind of method that deep purifying is removed micro-tungsten from high-concentration molybdenate solution according to claim 5,, it is characterized in that, the resin after the parsing, the HCl solution regeneration with 4～6%, and water washing is used for next round absorption to fluid pH=3～5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100310515A CN101264933B (en) | 2008-04-11 | 2008-04-11 | Deep purification method for removing micro-tungsten from high-concentration molybdenate solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100310515A CN101264933B (en) | 2008-04-11 | 2008-04-11 | Deep purification method for removing micro-tungsten from high-concentration molybdenate solution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101264933A true CN101264933A (en) | 2008-09-17 |
| CN101264933B CN101264933B (en) | 2011-03-23 |
Family
ID=39987658
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008100310515A Expired - Fee Related CN101264933B (en) | 2008-04-11 | 2008-04-11 | Deep purification method for removing micro-tungsten from high-concentration molybdenate solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101264933B (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102162030A (en) * | 2011-03-25 | 2011-08-24 | 中南大学 | Ion-exchange separation method for tungsten and molybdenum in tungstate and molybdate mixed solution |
| CN102329962A (en) * | 2011-10-17 | 2012-01-25 | 中南大学 | Method for deeply separating tungsten and molybdenum from high-tungsten and high-molybdenum mixed solution |
| CN102676810A (en) * | 2012-05-22 | 2012-09-19 | 中南大学 | Method for separating and recycling vanadium and chromium from vanadate-chromate-containing solution |
| CN103906709A (en) * | 2011-08-26 | 2014-07-02 | 环保金属有限公司 | Method for recovering technical-grade molybdenum from diluted acid leacing solutions (PLS) that have a high arsenic concentration and originate from metallurgical waste |
| CN107419099A (en) * | 2016-05-24 | 2017-12-01 | 北京清树科技发展有限公司 | A kind of separation and the method for tungsten and molybdenum in recovery tungstates and molybdic acid salt mixture |
| CN108642309A (en) * | 2018-06-07 | 2018-10-12 | 江西理工大学 | A kind of technique that ion-exchange removes molybdenum from tungstate solution |
| CN110724838A (en) * | 2019-09-30 | 2020-01-24 | 浙江特力再生资源有限公司 | Method for separating tungsten and molybdenum from waste catalyst containing tungsten and molybdenum |
| CN111634946A (en) * | 2020-05-26 | 2020-09-08 | 金堆城钼业股份有限公司 | Method for removing trace tungsten in molybdate |
| CN111659535A (en) * | 2020-05-26 | 2020-09-15 | 金堆城钼业股份有限公司 | Molybdenum-tungsten separation method |
| CN114275816A (en) * | 2021-12-15 | 2022-04-05 | 成都虹波钼业有限责任公司 | Molybdic acid and production process thereof |
-
2008
- 2008-04-11 CN CN2008100310515A patent/CN101264933B/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102162030A (en) * | 2011-03-25 | 2011-08-24 | 中南大学 | Ion-exchange separation method for tungsten and molybdenum in tungstate and molybdate mixed solution |
| CN103906709A (en) * | 2011-08-26 | 2014-07-02 | 环保金属有限公司 | Method for recovering technical-grade molybdenum from diluted acid leacing solutions (PLS) that have a high arsenic concentration and originate from metallurgical waste |
| CN103906709B (en) * | 2011-08-26 | 2015-11-25 | 环保金属有限公司 | The method of technical grade molybdenum is reclaimed from the rare acid dip solution of the metallurgical slag containing High Concentration of Arsenic (PLS) |
| CN102329962A (en) * | 2011-10-17 | 2012-01-25 | 中南大学 | Method for deeply separating tungsten and molybdenum from high-tungsten and high-molybdenum mixed solution |
| CN102329962B (en) * | 2011-10-17 | 2014-04-09 | 中南大学 | Method for deeply separating tungsten and molybdenum from high-tungsten and high-molybdenum mixed solution |
| CN102676810A (en) * | 2012-05-22 | 2012-09-19 | 中南大学 | Method for separating and recycling vanadium and chromium from vanadate-chromate-containing solution |
| CN102676810B (en) * | 2012-05-22 | 2013-08-21 | 中南大学 | Method for separating and recycling vanadium and chromium from vanadate-chromate-containing solution |
| CN107419099B (en) * | 2016-05-24 | 2018-08-14 | 北京清树科技发展有限公司 | A method of separation and tungsten and molybdenum in recycling tungstates and molybdic acid salt mixture |
| CN107419099A (en) * | 2016-05-24 | 2017-12-01 | 北京清树科技发展有限公司 | A kind of separation and the method for tungsten and molybdenum in recovery tungstates and molybdic acid salt mixture |
| CN108642309A (en) * | 2018-06-07 | 2018-10-12 | 江西理工大学 | A kind of technique that ion-exchange removes molybdenum from tungstate solution |
| CN110724838A (en) * | 2019-09-30 | 2020-01-24 | 浙江特力再生资源有限公司 | Method for separating tungsten and molybdenum from waste catalyst containing tungsten and molybdenum |
| CN111634946A (en) * | 2020-05-26 | 2020-09-08 | 金堆城钼业股份有限公司 | Method for removing trace tungsten in molybdate |
| CN111659535A (en) * | 2020-05-26 | 2020-09-15 | 金堆城钼业股份有限公司 | Molybdenum-tungsten separation method |
| CN111659535B (en) * | 2020-05-26 | 2022-10-11 | 金堆城钼业股份有限公司 | Molybdenum-tungsten separation method |
| CN111634946B (en) * | 2020-05-26 | 2022-11-18 | 金堆城钼业股份有限公司 | Method for removing trace tungsten in molybdate |
| CN114275816A (en) * | 2021-12-15 | 2022-04-05 | 成都虹波钼业有限责任公司 | Molybdic acid and production process thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101264933B (en) | 2011-03-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101264933B (en) | Deep purification method for removing micro-tungsten from high-concentration molybdenate solution | |
| AU724141B2 (en) | Apparatus and method for ammonia removal from waste streams | |
| CN107486130B (en) | Preparation method of prussian blue compound deammoniation material and application of prussian blue compound deammoniation material in sewage deammoniation | |
| CN101215636B (en) | Stone coal sodication roasting and vanadium-extracting method | |
| Liang et al. | Preparation of mixed rare earths modified chitosan for fluoride adsorption | |
| CN105384195B (en) | Method for recovering rhenium from molybdenum smelting waste acid | |
| CN107265548B (en) | Method for deeply adsorbing and removing phosphorus by using hydrated iron oxide loaded attapulgite | |
| CN109182791B (en) | Method for removing aluminum from rare earth feed liquid by organic acid complexation-solid phase adsorption | |
| CN101234827A (en) | Method for treating chromium-containing wastewater containing high-concentration sodium sulfate and recovering resources | |
| CN101113062A (en) | Vanadium-containing sewage treatment method | |
| CN111422942A (en) | Method for synchronously reducing and adsorbing hexavalent chromium in water by using ethylenediamine-based resin | |
| CN105817210A (en) | Method for preparing alkalescent ion exchange fibers | |
| WO2023087727A1 (en) | Method for vanadium extraction and precipitation by using vanadium-containing carbonated leach liquor and recycling of residual liquid | |
| CN101607769A (en) | A kind of treatment process of nitrogen-containing wastewater | |
| CN110724838A (en) | Method for separating tungsten and molybdenum from waste catalyst containing tungsten and molybdenum | |
| CN104628087A (en) | Method for treating vanadium-chromium wastewater by using ion-exchange fibers | |
| CN102329962B (en) | Method for deeply separating tungsten and molybdenum from high-tungsten and high-molybdenum mixed solution | |
| CN107012331B (en) | Vanadium and the method for preparing vanadic anhydride are recycled from the dead catalyst of vanadium containing molybdenum | |
| CN101781035B (en) | Method for recovering terramycin from terramycin production wastewater. | |
| CN106178591B (en) | A method of purification organic amine | |
| CN104628032B (en) | Method for preparing high-purity ammonium metavanadate from spent catalyst | |
| CN103387506A (en) | Method for producing EDTA ferric sodium salt by recovering Fe<II>EDTA wet-process complexed denitrated waste-liquid | |
| CN1923345A (en) | Process for removal of sulfate ions from organic amine absorbent | |
| CN101016171A (en) | Preparation process for high-purity alpha-Fe2O3 by ferrous sulfate-ammonium carbonate method | |
| CN107486131B (en) | Preparation method of zinc ferricyanide sodium deamination material and application of zinc ferricyanide sodium deamination material in sewage deamination |
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 | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20080917 Assignee: Jiangsu Star Limited company of tungsten and molybdenum Assignor: Central South University Contract record no.: 2018320000175 Denomination of invention: Deep purification method for removing micro-tungsten from high-concentration molybdenate solution Granted publication date: 20110323 License type: Common License Record date: 20180929 |
|
| EE01 | Entry into force of recordation of patent licensing contract | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110323 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |