CN85101874A - P507 extration resin chromatography is separated and extraction HIGH PURITY THULIUM OXIDE and lutecium oxide - Google Patents
P507 extration resin chromatography is separated and extraction HIGH PURITY THULIUM OXIDE and lutecium oxide Download PDFInfo
- Publication number
- CN85101874A CN85101874A CN 85101874 CN85101874A CN85101874A CN 85101874 A CN85101874 A CN 85101874A CN 85101874 CN85101874 CN 85101874 CN 85101874 A CN85101874 A CN 85101874A CN 85101874 A CN85101874 A CN 85101874A
- Authority
- CN
- China
- Prior art keywords
- oxide
- purity
- high purity
- post
- lutecium
- 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.)
- Withdrawn
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Catalysts (AREA)
Abstract
The invention belongs to the chromatographic separation of element.Can be used for industrial-scale production HIGH PURITY THULIUM OXIDE and lutecium oxide, more with short production cycle than ion exchange method, the purity height, present method is a stationary phase with the P507 extration resin, with hydrochloric acid is moving phase, chromatography separation and Extraction HIGH PURITY THULIUM OXIDE and lutecium oxide from rareearth enriching material fast and efficiently on the post, Tm
2O
3Purity>99.995%, yield 90~98%, Lu
2O
3Purity 99.99%, yield 75~85%.
Description
The invention belongs to the chromatographic separation rare earth element, from the enriched substance of thulium and lutetium, extract the novel method of HIGH PURITY THULIUM OXIDE and lutecium oxide.
Solvent extraction and ion exchange method are mainly adopted in the separation of plant-scale rare earth element, and the former selectivity is good, latter's separation efficiency height.And the extraction high-purity rare-earth then biases toward the ion exchange method ion exchange method because the formation and the dissociation reaction speed of complex compound are slow, causes separation cycle long.
The present inventor as far back as 1975 at first with P
507(abbreviation of the own ester of 2-ethylhexyl phosphonic acid single 2-ethyl) is used for extraction-chromatography rare-earth separating (Peng Chunlin, Ji Yongyi, Lu Anqiu etc.; Analytical chemistry 8(4) 318(1980); Peng Chunlin, Cui Yongde, Song Qingxiu analytical chemistry 11(7) 489(1983), it merges the high efficiency of solvent-extracted highly selective and ion-exchange chromatography, 15 rare earth elements have been separated quantitatively, in rare earth analysis, obtained using widely, showed favorable industrial application prospect.
In recent years, the domestic P that occurred
507Extration resin, it is with P
507Extraction agent is aggregated in vinylbenzene, and a kind of novel extraction resin on the skeleton of divinylbenzene is to be the improvement of carrier to silica gel, still is mainly used in rare earth analysis and separates.
The objective of the invention is to adopt P
507The extration resin chromatography, from rareearth enriching material efficiently, separation and Extraction high purity rare earth oxides apace.
P set forth in the present invention
507The technology of extration resin chromatography separation and Extraction HIGH PURITY THULIUM OXIDE and lutecium oxide is: with-50~200 purpose P
507Extration resin (0.55 gram P
507/ gram resin) be the ratio of the post footpath of stationary phase chromatographic column and height between 1/15 to 1/40, be moving phase with 0.7~4N hydrochloric acid, be raw material with 70~90% grade person's rareearth enriching materials, the mode (flow velocity 0.2~1ml/cm of employing gradient elution
2Divide) chromatography rare-earth separating on the post, and Er, Tm appear successively, Yb, Lu(are positive sequence), the fraction collection effluent liquid, with oxalate precipitation, and calcination becomes oxide compound after the enrichment.
When adopting present method separation and Extraction thulium and lutetium, the separation factor β of adjacent rare earth
Tm Er=3.14, β
Yb Tm=2.94, β
Lu Yb=1.76, rare earth loaded heavy increase, separation factor descends, and adopts technology of the present invention, advances post with the rareearth enriching material of 70~90% grades, can once obtain purity 〉=99.995%Tm
2O
3, yield 90~98% also can obtain purity and be 99.99% Lu
2O
3, yield 75~85%.The elution acidity of present method is lower, and lower more than 1~3 times than HDEHP and HEH φ P, separation cycle is short, the top condition of using φ 50mm post was respectively 18~23 hours thulium and lutetium, faster more than 20 times than ion exchange method, using the inventive method has tangible economic benefit, every processing 1Kg80%Tm
2O
3Enriched substance can obtain 750 the gram about purity>99.995%Tm
2O
3, amount to 1300 yuan of Renminbi, 176 yuan of Renminbi are amounted in chemical reagent consumption.Every processing 1Kg80%Lu
2O
3Enriched substance can obtain 640 gram left and right sides purity and be 99.99% Lu
2O
3, amount to 1920 yuan of Renminbi, 244 yuan of Renminbi are amounted in chemical reagent consumption.
The preparation of example 1. high-purity thuliums
Use φ 50mm chromatographic column, post height/1500mm, there is the glass sand filter disc post lower end, and post has constant temperature circulation sleeve pipe outward, and the control column temperature is 50 ℃, takes by weighing 750 gram-50+200 order P
507Extration resin, after the dilute hydrochloric acid immersion with 2 times of volumes, the slurry method is adorned post, takes by weighing 3~10% magnetic rare earth oxide (2%Er of chromatographic column total amount
2O
3, 80%Tm
2O
317%Yb
2O
3, 1%Lu
2O
3) with behind 1: 1 dissolving with hydrochloric acid, steam near and do, add the water dissolution of 10 times of amounts, advance post, control flow velocity 1~4 ml/min, again with 0.7~1.5N hydrochloric acid wash-out Ev, 1.5~2.6N hydrochloric acid wash-out Tm and Yb, 2.6~4N salt pickling acid Yb and Lu, the elution of ladder acidity, substep is collected, and uses inductance coupling plasma emissioning spectral analysis, Ho in the working sample
2O
3, Y
2O
3, Er
2O
3, Yb
2O
3, Lu
2O
3Content, main body solution becomes oxide compound through the oxalate precipitation calcination.Products obtained therefrom Tm
2O
3Purity 〉=99.995%, yield 90~98%, obtaining purity simultaneously is 98~99.95%Er
2O
3, Yb
2O
3, Lu
2O
3Yield>90%.
The preparation of example 2. high-purity lutetiums
Use φ 50mm chromatographic column, the high 1500mm of post, there is the glass sand filter disc post lower end, and post has constant temperature circulation sleeve pipe outward, and controlled temperature is 50 ℃, takes by weighing 1Kg-50+200 order P
507Extration resin, after soaking with the dilute hydrochloric acid of 2 times of volumes, slurry method dress post takes by weighing 3~10% rare earth oxide (20%Yb of chromatographic column total amount
2O
3, 80%Lu
2O
3) with behind 1: 1 dissolving with hydrochloric acid, steam near and do, the water dissolution that adds 10 times of amounts, advance post, control flow velocity 1~4 ml/min is earlier with 1.0~2.6N hydrochloric acid wash-out Yb, continue with 2.6~4.0N hydrochloric acid wash-out Lu, the elution of ladder acidity, fraction collection is with Ho in the inductance coupling plasma emissioning spectral analysis working sample
2O
3, Y
2O
3, Er
2O
3, Tm
2O
3, Yb
2O
3And Lu
2O
3Content, main body solution becomes oxide compound through the oxalate precipitation calcination, products obtained therefrom Lu
2O
3Purity be 99.99% yield 75~85%, still can obtain purity>99.95%Yb
2O
3, yield 80%.
Claims (3)
1, the method for a kind of separation and Extraction HIGH PURITY THULIUM OXIDE and lutecium oxide, it is characterised in that: at 50 ℃, with-50+200 order P
507Extration resin is a stationary phase, is moving phase with 0.7~4.0N hydrochloric acid, with the enriched substance raw material of thulium and lutetium, and in the mode of ladder acidity elution, chromatographic separation on the post.
2, as the described chromatography separating method of claim 1., its feature also is the ratio of the post footpath of chromatographic column and height between 1: 15 to 1: 40, and the useful load of rare earth is between 3% to 10%.
3, as the described chromatography separating method of claim 1., its feature is that also the speed of moving phase is at 0.2~1.0ml/cm
2Divide
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN85101874A CN85101874B (en) | 1985-04-01 | 1985-04-01 | Chromatographic separation and extraction method of high-purity thulium oxide and lutetium oxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN85101874A CN85101874B (en) | 1985-04-01 | 1985-04-01 | Chromatographic separation and extraction method of high-purity thulium oxide and lutetium oxide |
Publications (2)
Publication Number | Publication Date |
---|---|
CN85101874A true CN85101874A (en) | 1986-07-30 |
CN85101874B CN85101874B (en) | 1988-08-17 |
Family
ID=4792112
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN85101874A Expired CN85101874B (en) | 1985-04-01 | 1985-04-01 | Chromatographic separation and extraction method of high-purity thulium oxide and lutetium oxide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN85101874B (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1101476C (en) * | 1998-01-13 | 2003-02-12 | 北京大学 | Process for producing high-purity lutetium oxide by extracting separation method |
CN103050165A (en) * | 2012-12-27 | 2013-04-17 | 中国原子能科学研究院 | 79Se, 93Zr, 107Pd joint extraction device |
CN104593595A (en) * | 2015-01-26 | 2015-05-06 | 江西理工大学 | Method for separating rare earth elements |
CN104593591A (en) * | 2015-01-26 | 2015-05-06 | 江西理工大学 | Method for separating rare earth elements |
CN104593594A (en) * | 2015-01-26 | 2015-05-06 | 江西理工大学 | Method for enriching rare earth from rare earth leaching mother liquor |
CN104611560A (en) * | 2015-01-26 | 2015-05-13 | 江西理工大学 | Method for enriching rare earth from rare-earth leaching mother liquor |
CN104726710A (en) * | 2015-01-26 | 2015-06-24 | 江西理工大学 | Method for separating rare earth element |
CN106629809A (en) * | 2016-12-20 | 2017-05-10 | 攀枝花市精研科技有限公司 | Method for purifying coarse scandium oxide |
CN113337739A (en) * | 2021-06-03 | 2021-09-03 | 赣州有色冶金研究所有限公司 | Desorption method of rare earth loaded resin and recovery method of rare earth |
CN115198120A (en) * | 2022-07-20 | 2022-10-18 | 中国核动力研究设计院 | A slave bag 176 Yb 3+ Recovering and enriching the eluate 176 Yb 2 O 3 Method (2) |
CN115216652A (en) * | 2021-04-20 | 2022-10-21 | 赣江中药创新中心 | Method for separating and purifying lutetium from ytterbium-lutetium mixture |
CN115637341A (en) * | 2022-11-03 | 2023-01-24 | 湖南稀土金属材料研究院有限责任公司 | Ytterbium oxide purification method |
-
1985
- 1985-04-01 CN CN85101874A patent/CN85101874B/en not_active Expired
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1101476C (en) * | 1998-01-13 | 2003-02-12 | 北京大学 | Process for producing high-purity lutetium oxide by extracting separation method |
CN103050165A (en) * | 2012-12-27 | 2013-04-17 | 中国原子能科学研究院 | 79Se, 93Zr, 107Pd joint extraction device |
CN104726710B (en) * | 2015-01-26 | 2017-07-18 | 江西理工大学 | A kind of method of separation of rare earth elements |
CN104593594B (en) * | 2015-01-26 | 2017-11-03 | 江西理工大学 | The method of rare earth is enriched with a kind of leaching mother liquor from rare earth |
CN104593594A (en) * | 2015-01-26 | 2015-05-06 | 江西理工大学 | Method for enriching rare earth from rare earth leaching mother liquor |
CN104611560A (en) * | 2015-01-26 | 2015-05-13 | 江西理工大学 | Method for enriching rare earth from rare-earth leaching mother liquor |
CN104726710A (en) * | 2015-01-26 | 2015-06-24 | 江西理工大学 | Method for separating rare earth element |
CN104593595B (en) * | 2015-01-26 | 2017-11-03 | 江西理工大学 | A kind of method of separation of rare earth elements |
CN104593595A (en) * | 2015-01-26 | 2015-05-06 | 江西理工大学 | Method for separating rare earth elements |
CN104593591A (en) * | 2015-01-26 | 2015-05-06 | 江西理工大学 | Method for separating rare earth elements |
CN106629809A (en) * | 2016-12-20 | 2017-05-10 | 攀枝花市精研科技有限公司 | Method for purifying coarse scandium oxide |
CN106629809B (en) * | 2016-12-20 | 2022-09-16 | 攀枝花市精研科技有限公司 | Method for purifying coarse scandium oxide |
CN115216652A (en) * | 2021-04-20 | 2022-10-21 | 赣江中药创新中心 | Method for separating and purifying lutetium from ytterbium-lutetium mixture |
CN113337739A (en) * | 2021-06-03 | 2021-09-03 | 赣州有色冶金研究所有限公司 | Desorption method of rare earth loaded resin and recovery method of rare earth |
CN115198120A (en) * | 2022-07-20 | 2022-10-18 | 中国核动力研究设计院 | A slave bag 176 Yb 3+ Recovering and enriching the eluate 176 Yb 2 O 3 Method (2) |
CN115198120B (en) * | 2022-07-20 | 2023-09-26 | 中国核动力研究设计院 | From containing 176 Yb 3+ Recovery and enrichment in leacheate 176 Yb 2 O 3 Is a method of (2) |
CN115637341A (en) * | 2022-11-03 | 2023-01-24 | 湖南稀土金属材料研究院有限责任公司 | Ytterbium oxide purification method |
CN115637341B (en) * | 2022-11-03 | 2024-03-12 | 湖南稀土金属材料研究院有限责任公司 | Ytterbium oxide purification method |
Also Published As
Publication number | Publication date |
---|---|
CN85101874B (en) | 1988-08-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104498739B (en) | A kind of rare-earth mineral decomposes the separation and recovery method of uranium, thorium, rare earth in recrement | |
CN102899485B (en) | Resin in pulp process is from containing the method extracting scandium scandium material | |
AU2013351773B2 (en) | Monazite ballast separation and recovery method | |
CN104831073B (en) | A kind of technique reclaiming platinum, palladium, rhodium from spent auto-catalysts | |
CN85101874A (en) | P507 extration resin chromatography is separated and extraction HIGH PURITY THULIUM OXIDE and lutecium oxide | |
CN114107668B (en) | Method for mechanically activating, reinforcing and leaching rare earth in waste polishing solution | |
WO1997003743A1 (en) | Zirconium and hafnium separation in sulfate solutions using continuous ion exchange chromatography | |
CN106745171A (en) | A kind of method for extraction and purification of dysprosia | |
CN102925681B (en) | Method for separating valuable components of monazite slags | |
CN106834687A (en) | A kind of method for extraction and purification of lanthana | |
CN106756015A (en) | A kind of method for extraction and purification of ytterbium oxide | |
CN102127127A (en) | Kanamycin extracting process | |
CN110423902A (en) | A kind of preparation method and system of high-purity carbonated rare earth | |
JPS5845341A (en) | Separation of rare earth metal | |
CN87101822A (en) | Medium-gadolinium and rich-europium ion type rare-earth mineral rare earth complete-separation process | |
CN106756019A (en) | A kind of method for extraction and purification of gadolinium oxide | |
CN106636686B (en) | Hydrochloric acid method produces synthetic rutile and leaches the method for extracting scandium in mother liquor | |
CN116065021A (en) | Ion exchange separation and purification method of single rare earth element samarium | |
CN85101611A (en) | P507 extration resin chromatography is separated and is extracted high-purity Holmium trioxide and dysprosium oxide | |
CN106834685A (en) | A kind of method for extraction and purification of luteium oxide | |
Gongyi et al. | Application of extraction chromatography to the preparation of high-purity scandium oxide | |
CN1061246A (en) | The method of extracting and separating zirconium from Scium trioxide | |
CN113151676A (en) | Retrieve device of tombarthite in follow tombarthite waste material | |
US3482932A (en) | Process for separating yttrium from the lanthanide elements | |
CN106756021A (en) | A kind of method for extraction and purification of samarium oxide |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
SE01 | Entry into force of request for substantive examination | ||
C06 | Publication | ||
PB01 | Publication | ||
C13 | Decision | ||
GR02 | Examined patent application | ||
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 |