CN102031369B - Method for extracting uranium by using ion exchange fixed tower under alternate Ph condition - Google Patents
Method for extracting uranium by using ion exchange fixed tower under alternate Ph condition Download PDFInfo
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- CN102031369B CN102031369B CN2010105689506A CN201010568950A CN102031369B CN 102031369 B CN102031369 B CN 102031369B CN 2010105689506 A CN2010105689506 A CN 2010105689506A CN 201010568950 A CN201010568950 A CN 201010568950A CN 102031369 B CN102031369 B CN 102031369B
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- uranium
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- resin
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- 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
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Abstract
Description
Claims (5)
- One kind under the solution acid alkalinity alternation condition ion-exchange fixed tower put forward the uranium method, comprising: poor resin absorption uranium step and carry a uranium resin Elution of Uranium step is characterized in that:Described poor resin absorption uranium step adopts the ion-exchange fixed tower to reclaim uranium from acid leaching solution, feeding manner is lower feed liquor, poor during at 0~20mg/L when effluent liquid uranium concentration and stoste uranium concentration, with solution emptying in the ion-exchange fixed tower, poor resin absorption uranium step finishes;Carrying uranium resin Elution of Uranium step comprises again successively:Drip washing neutralization stage: use to contain CO 3 2-The spent acid in the uranium resin is carried in neutralization with the eluent of sodium hydroxide, and feeding manner is lower feed liquor; In described drip washing neutralization stage, when the pH of effluent liquid value was in 2.5~8.0, the drip washing neutralization stage finished to enter the drip washing qualifying liquid stage;The drip washing qualifying liquid stage: feeding manner is upper feed liquor; Employing contains CO 3 2-Eluent or a barren solution of last tower make eluent and carry out drip washing to carrying a uranium resin;The one poor stage of drip washing: feeding manner is upper feed liquor, and effluent liquid is a barren solution; Employing contains CO 3 2-Eluent or two barren solutions of last tower make eluent and carry out drip washing to carrying a uranium resin;The two poor stages of drip washing: feeding manner is upper feed liquor, and effluent liquid is two barren solutions; Employing contains CO 3 2-Eluent carry out drip washing to carrying a uranium resin.
- According to claim 1 a kind of under the solution acid alkalinity alternation condition ion-exchange fixed tower put forward the uranium method, it is characterized in that: described poor resin absorption uranium step adopts the mode of a plurality of ion-exchange fixed tower series connection to carry out.
- According to claim 1 a kind of under the solution acid alkalinity alternation condition ion-exchange fixed tower put forward the uranium method, it is characterized in that: in the described two poor stages of drip washing, when drip washing effluent liquid uranium concentration during less than 0.2g/L, drip washing finishes, the solution in the emptying ion-exchange fixed tower.
- According to claim 1 a kind of under the solution acid alkalinity alternation condition ion-exchange fixed tower put forward the uranium method, it is characterized in that: in the described drip washing qualifying liquid stage, when the uranium concentration of effluent liquid was reduced to 1~10g/L, the described drip washing qualifying liquid stage finished, and enters the one poor stage of drip washing.
- According to claim 1 a kind of under the solution acid alkalinity alternation condition ion-exchange fixed tower put forward the uranium method, it is characterized in that: in the described one poor stage of drip washing, when the uranium concentration of effluent liquid was reduced to 0.5~1g/L, the described one poor stage of drip washing finished, and enters the two poor stages of drip washing.
Priority Applications (1)
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CN2010105689506A CN102031369B (en) | 2010-12-01 | 2010-12-01 | Method for extracting uranium by using ion exchange fixed tower under alternate Ph condition |
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CN2010105689506A CN102031369B (en) | 2010-12-01 | 2010-12-01 | Method for extracting uranium by using ion exchange fixed tower under alternate Ph condition |
Publications (2)
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CN102031369A CN102031369A (en) | 2011-04-27 |
CN102031369B true CN102031369B (en) | 2013-03-20 |
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CN2010105689506A Expired - Fee Related CN102031369B (en) | 2010-12-01 | 2010-12-01 | Method for extracting uranium by using ion exchange fixed tower under alternate Ph condition |
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Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103204601B (en) * | 2013-04-23 | 2014-05-07 | 清华大学 | Wastewater treatment method |
CN111020190B (en) * | 2019-12-10 | 2021-10-22 | 核工业北京化工冶金研究院 | Process linking method for extracting uranium by two-step ion exchange method |
CN112680606B (en) * | 2020-12-16 | 2022-10-21 | 核工业北京化工冶金研究院 | Ion exchange method for gas generation in uranium extraction process |
CN114192195A (en) * | 2021-12-09 | 2022-03-18 | 中核内蒙古矿业有限公司 | Elution device for uranium extraction by ion exchange method and elution method of ion exchange resin |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101619401A (en) * | 2009-07-17 | 2010-01-06 | 云南佰盾环保新技术咨询有限公司 | Method for recycling uranium from uranium extraction tailings |
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2010
- 2010-12-01 CN CN2010105689506A patent/CN102031369B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101619401A (en) * | 2009-07-17 | 2010-01-06 | 云南佰盾环保新技术咨询有限公司 | Method for recycling uranium from uranium extraction tailings |
Non-Patent Citations (1)
Title |
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周根茂等.铀水冶离子交换塔中树脂床层状态的研究.《铀矿冶》.2006,第25卷(第3期),133-136. * |
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CN102031369A (en) | 2011-04-27 |
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C14 | Grant of patent or utility model | ||
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CB03 | Change of inventor or designer information |
Inventor after: Li Weicai Inventor after: Zhou Genmao Inventor after: Niu Yuqing Inventor after: Liu Chao Inventor after: Deng Shunqin Inventor before: Li Weicai Inventor before: Zhou Genmao Inventor before: Liu Chao Inventor before: Deng Shunqin |
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CB03 | Change of inventor or designer information | ||
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Free format text: CORRECT: INVENTOR; FROM: LI WEICAI ZHOU GENMAO LIU CHAO DENG SHUNQIN TO: LI WEICAI ZHOU GENMAO NIU YUQING LIU CHAO DENG SHUNQIN |
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130320 Termination date: 20141201 |
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