CN106435225A - Method of dissolving basic zinc carbonate from solid mixture of samaric carbonate and basic zinc carbonate - Google Patents

Method of dissolving basic zinc carbonate from solid mixture of samaric carbonate and basic zinc carbonate Download PDF

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Publication number
CN106435225A
CN106435225A CN201610233792.6A CN201610233792A CN106435225A CN 106435225 A CN106435225 A CN 106435225A CN 201610233792 A CN201610233792 A CN 201610233792A CN 106435225 A CN106435225 A CN 106435225A
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CN
China
Prior art keywords
carbonate
basic zinc
zinc carbonate
solid mixture
samaric
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Pending
Application number
CN201610233792.6A
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Chinese (zh)
Inventor
郝先库
张瑞祥
马显东
赵永志
刘海旺
王士智
刘莎莎
斯琴毕力格
许宗泽
贾红梅
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JINGRUI NEW MATERIAL CO Ltd BAOTOU
Baotou Rare Earth Research Institute
Santoku Corp
Original Assignee
JINGRUI NEW MATERIAL CO Ltd BAOTOU
Baotou Rare Earth Research Institute
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Application filed by JINGRUI NEW MATERIAL CO Ltd BAOTOU, Baotou Rare Earth Research Institute filed Critical JINGRUI NEW MATERIAL CO Ltd BAOTOU
Priority to CN201610233792.6A priority Critical patent/CN106435225A/en
Publication of CN106435225A publication Critical patent/CN106435225A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B59/00Obtaining rare earth metals
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to a method of dissolving basic zinc carbonate from a solid mixture of samaric carbonate and basic zinc carbonate and belongs to the field of rare earth hydrometallurgy. The method comprises the following steps of: adding a samarium-europium separating rare earth saponification residual liquid containing NH4Cl and a solid mixture of samaric carbonate and basic zinc carbonate into a reaction tank; then adding a solid NH4Cl; adjusting the pH value of the solution to 7 with ammonia water; performing a reaction at a certain time at a reaction temperature of 60 DEG C, wherein the basic zinc carbonate is dissolved into the solution from the solid mixture while samaric carbonate is insoluble; and performing filtration, washing and firing to obtain a samarium oxide product, the ZnO content of which is 0.005%. The method can lower the production cost and simplify the production step, so that industrialization is conveniently realized.

Description

The method dissolving basic zinc carbonate from samaric carbonate and basic zinc carbonate solid mixture
Technical field
The present invention relates to a kind of method dissolving basic zinc carbonate from samaric carbonate and basic zinc carbonate solid mixture, belong to In field of rare earth hydrometallurgy.
Background technology
Current enterprise uses Eu in zinc powder reduction europium-enriched solution3+Prepare europium oxide technique, in europium-enriched solution, add zinc powder By Eu3+It is reduced into Eu2+, and zinc powder is changed into Zn2+Enter in earth solution, containing Zn2+Earth solution as reduction extraction Feed liquid, at reduction extraction segregation section Zn2+As easy extraction component with Sm3+、Gd3+Return after back extraction Deng trivalent rare earth ions To samarium europium segregation section, Zn2+With Sm3+Flow out from samarium europium segregation section raffinate together, with ammonium hydrogen carbonate as the precipitating reagent of samarium, obtain To samaric carbonate precipitation, in order to control the content of impure zinc in samaric carbonate precipitation, industrialized production may often be such that samarium incomplete Precipitation, in mother liquor of precipitation of ammonium, reserved concentration is the Sm of 0.01-0.02 mol/L3+, after centrifugal solid-liquid separates, filtrate is contained Sm3+And Zn2+Again with ammonium hydrogen carbonate by Sm3+Precipitation is complete, the mixture being precipitated as samaric carbonate and basic zinc carbonate obtaining, In order to reclaim samarium in mixture, use hydrochloric acid to dissolve the mixture of samaric carbonate and basic zinc carbonate, then use N235Or P507Extraction Separate, obtain without Zn2+SmCl3Solution, this technological operation operation is loaded down with trivial details, relatively costly.
Content of the invention
Present invention aim at providing a kind of side dissolving basic zinc carbonate from samaric carbonate and basic zinc carbonate solid mixture Method, the method is by basic zinc carbonate dissolution from samaric carbonate and basic zinc carbonate solid mixture, prepares ZnO content and is less than The Sm of 0.005%2O3Product.
Technical solution:
The present invention adds in retort and contains NH4More than the samarium europium rare-earth separating saponification of Cl, liquid, samaric carbonate and basic zinc carbonate consolidates Body mixture, NH in liquid more than rare-earth sodium saponification4Cl concentration is 2.24 mol/L, and more than rare-earth sodium saponification, liquid and solid mixture weight ratio are 10:1, in solid mixture, samaric carbonate and basic zinc carbonate percentage by weight are 90-50%:10-50%, after stirring, adds Solid NH4Cl, liquid and NH more than rare-earth sodium saponification4Cl weight ratio is 10:0.41-0.94, NH4After Cl dissolves, with ammoniacal liquor by solution ph Being formulated to 7, when reaction temperature 60 DEG C, in 4 hours reaction time, basic zinc carbonate is dissolved into solution from solid mixture, carbon Acid samarium does not dissolves, and through filtration, washing, calcination, obtains the samarium oxide product less than 0.005% for the ZnO content.
Invention effect
The present invention adds NH4Cl and with ammoniacal liquor allotment solution ph be key problem in technology;If the NH adding4Cl measures deficiency, only Part basic zinc carbonate is dissolved into solution from solid mixture, the NH of addition4Cl amount too much, can improve basic zinc carbonate Solubility, but basic zinc carbonate can not be completely dissolved, also can increase production cost;If allocating solution ph without ammoniacal liquor, only Small part basic zinc carbonate is had to be dissolved into solution from solid mixture, too high by ammoniacal liquor allotment solution ph, can not be by admittedly In body mixture, basic zinc carbonate is dissolved in solution;So control NH4Cl addition and with ammoniacal liquor allocate solution ph size, Can be dissolved out basic zinc carbonate from solid mixture, samaric carbonate does not dissolves, it is simple to realize industrialization.
Detailed description of the invention
Embodiment 1
3000 L are added to contain NH in retort4Cl concentration be 2.24 mol/L samarium europium rare-earth separating saponification more than liquid, add 300 Kg contains 90% samaric carbonate and 10% basic zinc carbonate solid mixture, after stirring, adds 123 kg solid NH4Cl, NH4Cl is molten Xie Hou, adds ammoniacal liquor allotment solution ph to be 7, and when reaction temperature 60 DEG C, in 4 hours reaction time, basic zinc carbonate is from solid Mixture is dissolved in solution, and samaric carbonate does not dissolves, and through filtration, washing, calcination, obtains the samarium oxide that ZnO content is 0.002% Product.
Embodiment 2
3000 L are added to contain NH in retort4Cl concentration be 2.24 mol/L samarium europium rare-earth separating saponification more than liquid, add 300 Kg contains 70% samaric carbonate and 30% basic zinc carbonate solid mixture, after stirring, adds 203 kg solid NH4Cl, NH4Cl is molten Xie Hou, adds ammoniacal liquor allotment solution ph to be 7, and when reaction temperature 60 DEG C, in 4 hours reaction time, basic zinc carbonate is from solid Mixture is dissolved in solution, and samaric carbonate does not dissolves, and through filtration, washing, calcination, obtains the samarium oxide that ZnO content is 0.003% Product.
Embodiment 3
3000 L are added to contain NH in retort4Cl concentration be 2.24 mol/L samarium europium rare-earth separating saponification more than liquid, add 300 Kg contains 50% samaric carbonate and 50% basic zinc carbonate solid mixture, after stirring, adds 282 kg solid NH4Cl, NH4Cl is molten Xie Hou, adds ammoniacal liquor allotment solution ph to be 7, and when reaction temperature 60 DEG C, in 4 hours reaction time, basic zinc carbonate is from solid Mixture is dissolved in solution, and samaric carbonate does not dissolves, and through filtration, washing, calcination, obtains the samarium oxide that ZnO content is 0.0035% Product.

Claims (1)

1. the method dissolving basic zinc carbonate from samaric carbonate and basic zinc carbonate solid mixture, it is characterised in that in reaction Tank adds and contains NH4The solid mixture of liquid, samaric carbonate and basic zinc carbonate, rare-earth sodium saponification more than the samarium europium rare-earth separating saponification of Cl NH in remaining liquid4Cl concentration is 2.24 mol/L, and more than rare-earth sodium saponification, liquid and solid mixture weight ratio are 10:1, in solid mixture Samaric carbonate and basic zinc carbonate percentage by weight are 90-50%:10-50%, after stirring, adds solid NH4Cl, rare-earth sodium saponification Remaining liquid and NH4Cl weight ratio is 10:0.41-0.94, NH4After Cl dissolves, with ammoniacal liquor, solution ph is formulated to 7, in reaction temperature When 60 DEG C, in 4 hours reaction time, basic zinc carbonate is dissolved into solution from solid mixture, and samaric carbonate does not dissolves, through filtering, Washing, calcination, obtain the samarium oxide product less than 0.005% for the ZnO content.
CN201610233792.6A 2016-04-15 2016-04-15 Method of dissolving basic zinc carbonate from solid mixture of samaric carbonate and basic zinc carbonate Pending CN106435225A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610233792.6A CN106435225A (en) 2016-04-15 2016-04-15 Method of dissolving basic zinc carbonate from solid mixture of samaric carbonate and basic zinc carbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610233792.6A CN106435225A (en) 2016-04-15 2016-04-15 Method of dissolving basic zinc carbonate from solid mixture of samaric carbonate and basic zinc carbonate

Publications (1)

Publication Number Publication Date
CN106435225A true CN106435225A (en) 2017-02-22

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014051718A (en) * 2012-09-10 2014-03-20 Hitachi Metals Ltd Rare earth separation method and rare earth separation unit
CN103924080A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Method for increasing samarium and zinc extraction separation factor in ammonium chloride system by increasing phase ratio
CN103924075A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Application of hydrochloric acid solution with NH4Cl as washing liquid for extraction separation of samarium and zinc
CN103924078A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Method for improving extraction separation factor for samarium and zinc by adding ammonium chloride into feed liquid
CN103924077A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Application of SmCl3 solution with NH4Cl as washing liquid for extraction separation of Sm3+ and Zn2+
CN103922383A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Extraction separation method for rare earth and zinc in reverse extraction raffinate obtained in reduction extraction separation of europium

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014051718A (en) * 2012-09-10 2014-03-20 Hitachi Metals Ltd Rare earth separation method and rare earth separation unit
CN103924080A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Method for increasing samarium and zinc extraction separation factor in ammonium chloride system by increasing phase ratio
CN103924075A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Application of hydrochloric acid solution with NH4Cl as washing liquid for extraction separation of samarium and zinc
CN103924078A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Method for improving extraction separation factor for samarium and zinc by adding ammonium chloride into feed liquid
CN103924077A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Application of SmCl3 solution with NH4Cl as washing liquid for extraction separation of Sm3+ and Zn2+
CN103922383A (en) * 2014-03-18 2014-07-16 包头稀土研究院 Extraction separation method for rare earth and zinc in reverse extraction raffinate obtained in reduction extraction separation of europium

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Effective date of abandoning: 20181019