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 PDFInfo
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- 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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- carbonate
- basic zinc
- zinc carbonate
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B59/00—Obtaining rare earth metals
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
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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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- Life Sciences & Earth Sciences (AREA)
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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
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.
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Citations (6)
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 |
-
2016
- 2016-04-15 CN CN201610233792.6A patent/CN106435225A/en active Pending
Patent Citations (6)
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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