CN108034842A - Ion type rareearth ore is without the environmentally protective production practice of ammoniumization - Google Patents

Ion type rareearth ore is without the environmentally protective production practice of ammoniumization Download PDF

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Publication number
CN108034842A
CN108034842A CN201711272172.4A CN201711272172A CN108034842A CN 108034842 A CN108034842 A CN 108034842A CN 201711272172 A CN201711272172 A CN 201711272172A CN 108034842 A CN108034842 A CN 108034842A
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ore
ammoniumization
ammonium
environmentally protective
ion type
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CN201711272172.4A
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Inventor
王炯辉
黄冬梅
陈道贵
赵彬
张成学
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Five Mineral Exploration And Development Co Ltd
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Five Mineral Exploration And Development Co Ltd
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Priority to CN201711272172.4A priority Critical patent/CN108034842A/en
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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
    • C22B3/04Extraction of metal compounds from ores or concentrates by wet processes by leaching
    • 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
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/44Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
    • 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
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/44Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
    • C22B3/46Treatment or purification of solutions, e.g. obtained by leaching by chemical processes by substitution, e.g. by cementation
    • 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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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (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)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

It is as follows without the environmentally protective production practice of ammoniumization, step the invention discloses ion type rareearth ore:The certain density no ammonium leaching ore deposit agent of liquid injection hole injection laid out of stope, occurs ion-exchange reactions with rare-earth mineral, obtains the mother liquor of enrichment rare-earth cation;Mother liquor seepage flow, converge in the liquid collecting engineering such as the natural water proof bottom plate of ore bed or artificial liquid collecting tunnel collocation liquid collecting deflector hole;Hydrometallurgy workshop is transported to by main transport pipeline again, using no ammonium medicament impurity-removing precipitating, obtains rare earth carbonate, supernatant is recycled back to liquid pool, and return to stope after overregulating pH value, addition medicament soaks ore deposit agent as new without ammonium.The advantage of the invention is that:Whole process is realized without ammonium, friendly to soil, water body environment;Produce waste water circulation comprehensive to utilize, without the outer row of useless evil;Rare earth ion leaching rate, liquid collecting rate and rate of deposition are high, improve resource and pick up comprehensive recovery.

Description

Ion type rareearth ore is without the environmentally protective production practice of ammoniumization
Technical field
The present invention relates to the environmentally protective production technique field of ion type rareearth ore, more particularly to ion type rareearth ore is without ammonium Production technique.
Background technology
Weathering crust ion adsorption type re is the distinctive rare earth mineral found in Jiangxi in 1969, and rare earth element is in mainly Hydration or hydroxyl hydrated cation preservation leach precipitation in weathering crust clay mineral, by cation exchange and obtain rare earth element Product.
The production of Rare-earth Mine experienced multiple great change from mining type to coprecipitation mode is leached.The warp from mining Pond leaching-dump leaching-in_situ leaching has been gone through, indoor salt bucket leaching-field ammonium sulfate pond leaching-field sulphur is experienced from Leaching way Sour ammonium in_situ leaching, the oxalic acid secondary precipitation+extraction method of dividision into groups-oxalate precipitation method-carbon ammonium precipitation method is experienced from coprecipitation mode. Carbon ammonium precipitation technology studied maturation for 1985 by University Of Nanchang, its precipitated products can be directly entered follow-up rare earth without calcination Separation, and can be returned after the supernatant acidifying after precipitating and make leachate, reduce discharge of wastewater and pollution, but its technical requirements Harshness, is unfavorable for improving production efficiency, the growth to benefit has restriction.
The production of existing Rare-earth Mine is mainly ammonium sulfate leaching ore deposit+carbon ammonium precipitation, most of using in_situ leaching Mode.This mode of production reduces production cost, reduces the stripping of earth's surface and the stacking of waste residue, reduces water quality dirt Dye, preferably protects surface vegetation and ecological environment, but solve the problems, such as without basic:
1. the technical problem of most critical
Used leaching ore deposit agent, impurity-removing precipitating agent contain ammonium ion, are entered with leaching ore deposit agent in massif, if phase Pass technology and engineering are unqualified, then there is a possibility that soaking ore deposit agent leaks into underground water, so as to cause soil and surrounding body Middle ammonia nitrogen, sulfate etc. are exceeded, cause environmental pollution.
Meanwhile in_situ leaching production process injects a large amount of leaching ore deposit agent into massif, massif is chronically at immersion or even is satisfied And state, soil physicochemical characteristic is changed, the excavation of the engineering such as earth's surface and ground lower groove, tunnel, destroys and stablize originally in addition With the stress of primary rock system of balance, the geological disasters such as landslide, surface subsidence are caused to occur.
2. peripheral issue
Original leaching ore deposit agent, the effect unobvious of impurity-removing precipitating agent, rare earth leaching rate is relatively low, and impurity-removing precipitating rate is relatively low, dilute The soil resource rate of recovery is low, so as to cause rare earth loss and the wasting of resources.
The content of the invention
The present invention is intended to provide it is dirty to solve soil, water body environment without the environmentally protective production practice of ammoniumization for ion type rareearth ore Dye is serious;The problem of leaching ore deposit, removal of impurities, deposition efficiency are low, and rare earth resources comprehensive recovery is low.
Ion type rareearth ore comprises the following steps without the environmentally protective production practice of ammoniumization:
(1) liquid injection hole is laid in the stope chosen, utilizes the natural water proof bottom plate of ore bed or the artificial liquid collecting lane of arrangement Road, and liquid collecting deflector hole i.e. water drilling of arranging in pairs or groups carries out liquid collecting;
(2) injected from liquid injection hole and soak ore deposit agent without ammonium;
(3) ion-exchange reactions occurs with rare-earth mineral without ammonium leaching ore deposit agent, obtains the mother liquor of enrichment rare earth, seepage flow, convergence To the natural water proof bottom plate of ore bed or artificial liquid collecting tunnel, into mother liquor collecting pit;
(4) mother liquor obtains rare earth by conveyance conduit to hydrometallurgy workshop successively by removal of impurities, precipitation and the processing of press filtration link Carbonate products;
(5) supernatant filtered out i.e. waste water is recycled to liquid pool, and by adjusting pH value, addition medicament is prepared into new no ammonium Soak ore deposit agent;
(6) freshly prepd no ammonium leaching ore deposit agent is passed through into pipeline to the new stope for meeting step (1).
Further, the no ammonium leaching ore deposit agent includes a kind of in Adlerika, liquor ferri trichloridi, aluminum trichloride solution It is or two or more.
Further, the mass fraction of the Adlerika is 2%-5%.
Further, the mass fraction of the liquor ferri trichloridi is 0.2%-1%.
Further, the mass fraction of the aluminum trichloride solution is 0.5%-1%.
Further, it is sodium hydroxide, sodium carbonate or sodium acid carbonate without ammonium medicament i.e. cleaner to be used in dedoping step In one kind.
Further, cleaned using sodium hydroxide, pH is adjusted to 5.3.
Further, cleaned using sodium carbonate, pH is adjusted to 5.3 ± 0.1.
Further, cleaned using sodium acid carbonate, pH is adjusted to 5.3 ± 0.1.
Further, the precipitating reagent used in precipitation process is sodium acid carbonate, and pH is adjusted to 5.3 ± 0.1.
The advantage of the invention is that:
1st, without ammonium, it is pollution-free, comprehensive recovery is high the characteristics of, meet environmentally protective requirement.The leaching ore deposit agent institute of use Originally it is the essential element in ore body and soil containing pantogen, whole technique does not bring massif into from outside pollution sources;Utilize Production waste water and rare earth waste regeneration leaching ore deposit agent, which reach, to be recycled, and is avoided and is arranged outside leaching ore deposit agent, while reduces rare earth resources It is lost in, improves resource comprehensive utilization rate;The big advantage of the process makes full use iron, aluminium environmental carrying capacity, avoids ammonia and nitrogen pollution, symbol Country is closed without ammonium, free of contamination environmentally protective policy requirements;
2nd, it is good to soak ore deposit agent Adlerika permeance property, can preferably arrange in pairs or groups with the rock ore deposit characteristic of ion type rareearth;
3rd, it is best to soak ore deposit agent liquor ferri trichloridi effect, liquor ferri trichloridi infiltration is strong, and early, not trailing occurs in peak, dilute Soil can be with Rapid Leaching, and leaching efficiency is high, and leaching ore deposit effect is used in combination than single significant effect with Adlerika, can be low Concentration, which leaches, to be used, and impurity leaching is low.
Brief description of the drawings
Fig. 1 is the stope structure schematic diagram using the natural water proof bottom plate of ore bed;
Fig. 2 is the stope structure schematic diagram using artificial liquid collecting tunnel and liquid collecting deflector hole;
Fig. 3 is the structure schematic top plan view in artificial liquid collecting tunnel.
Embodiment
Below in conjunction with the embodiment in the present invention, the technical solution in the present invention is clearly and completely described.It is aobvious So, described is only part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, Those of ordinary skill in the art's all other embodiments obtained on the premise of creative work is not made, belong to this Invent the scope of protection.
Using the leaching ore deposit agent of each embodiment, cleaner, precipitating reagent in Tables 1 and 2, carried out respectively by following processing step Soak ore deposit:
(1) liquid injection hole is laid by certain net degree in the stope chosen, using the natural water proof bottom plate of ore bed or by one Determining deviation arranges artificial liquid collecting tunnel, and the liquid collecting deflector hole for certain specification of arranging in pairs or groups i.e. water drilling carries out liquid collecting;
(2) injected from liquid injection hole and soak ore deposit agent without ammonium;
(3) as shown in Figure 1, being the stope using the natural water proof bottom plate of ore bed in Fig. 1, liquid injection hole 5, note are laid in stope Fluid apertures 5 passes through topsoil 1, extends to completely decomposed layer 2, and no ammonium leaching ore deposit agent flows into completely decomposed layer 2, half weathered layer from liquid injection hole 5 3, ion-exchange reactions occurs with rare-earth mineral, obtains the mother liquor of enrichment rare-earth cation, mother liquor is in dead weight and fluid injection pressure (dynamic) The power effect natural water proof bottom plate 4 of lower edge ore bed converges, into mother liquor collecting pit;
Alternatively,
As shown in Fig. 2, be to apply artificial liquid collecting tunnel in Fig. 2, and the stope of the liquid collecting deflector hole for certain specification of arranging in pairs or groups, note Fluid apertures 24 extends to completely decomposed layer 22 through topsoil 21, be located in artificial liquid collecting tunnel 25 ore bed original phreatic line 26 it On, liquid collecting deflector hole is equipped between liquid injection hole 24 and manually liquid collecting tunnel 25, no ammonium leaching ore deposit agent flows into full blast from liquid injection hole 24 Change 22 rare-earth mineral of layer and ion-exchange reactions occurs, obtain the mother liquor of enrichment rare-earth cation, mother liquor is in dead weight and fluid injection pressure The lower seepage flow of (dynamic) power effect, converge to artificial liquid collecting tunnel, into mother liquor collecting pit 7.
(4) mother liquor is successively handled by conveyance conduit to hydrometallurgy workshop by the removal of impurities of no ammonium medicament, precipitation and press filtration link, Obtain rare earth carbonate product;
(5) supernatant filtered out i.e. waste water is recycled to liquid pool, and by adjusting pH value, addition medicament is prepared into new leaching ore deposit Agent;
(6) freshly prepd no ammonium leaching ore deposit agent is passed through into pipeline to the new stope for meeting step (1).
Leaching ore deposit effect also together embodies in table.
Table 1:
Table 2
Note:The concentration that ore deposit agent is soaked in Tables 1 and 2 refers to mass fraction, precipitant concentration be solute and weight of solvent part it Than.
Above content is that a further detailed description of the present invention in conjunction with specific preferred embodiments, it is impossible to is assert The specific implementation of the present invention is confined to these explanations.For general technical staff of the technical field of the invention, On the premise of not departing from present inventive concept, some simple deduction or replace can also be made, should all be considered as belonging to the present invention's Protection domain.

Claims (10)

1. ion type rareearth ore is without the environmentally protective production practice of ammoniumization, it is characterised in that comprises the following steps:
(1) liquid injection hole is laid in the stope chosen, using the natural water proof bottom plate of ore bed or the artificial liquid collecting tunnel of arrangement, and Liquid collecting deflector hole, that is, water drilling of arranging in pairs or groups carries out liquid collecting;
(2) injected from liquid injection hole and soak ore deposit agent without ammonium;
(3) ion-exchange reactions occurs with rare-earth mineral without ammonium leaching ore deposit agent, obtains the mother liquor of enrichment rare earth, seepage flow, converge to ore deposit The natural water proof bottom plate of layer or artificial liquid collecting tunnel, into mother liquor collecting pit;
(4) mother liquor is successively handled by conveyance conduit to hydrometallurgy workshop by the removal of impurities of no ammonium medicament, precipitation and press filtration link, is obtained Rare earth carbonate product;
(5) supernatant filtered out i.e. waste water is cycled back to liquid pool, and new no ammonium leaching is prepared into by adjusting pH value, adding medicament Ore deposit agent;
(6) freshly prepd no ammonium leaching ore deposit agent is passed through into pipeline to the new stope for meeting step (1).
2. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 1, it is characterised in that the no ammonium Soaking ore deposit agent includes one or more in Adlerika, liquor ferri trichloridi, aluminum trichloride solution.
3. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 2, it is characterised in that the sulfuric acid The mass fraction of magnesium solution is 2%-5%.
4. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 2, it is characterised in that the trichlorine The mass fraction for changing ferrous solution is 0.2%-1%.
5. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 2, it is characterised in that the trichlorine The mass fraction for changing aluminum solutions is 0.5%-1%.
6. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 1, it is characterised in that dedoping step It is middle that use is one kind in sodium hydroxide, sodium carbonate or sodium acid carbonate without ammonium medicament i.e. cleaner.
7. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 6, it is characterised in that using hydrogen-oxygen Change sodium removal of impurities, pH is adjusted to 5.3.
8. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 6, it is characterised in that using carbonic acid Sodium cleans, and pH is adjusted to 5.3 ± 0.1.
9. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 6, it is characterised in that using carbonic acid Hydrogen sodium cleans, and pH is adjusted to 5.3 ± 0.1.
10. ion type rareearth ore is without the environmentally protective production practice of ammoniumization according to claim 1, it is characterised in that precipitated The precipitating reagent used in journey is sodium acid carbonate, and pH is adjusted to 5.3 ± 0.1.
CN201711272172.4A 2017-12-06 2017-12-06 Ion type rareearth ore is without the environmentally protective production practice of ammoniumization Pending CN108034842A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108486373A (en) * 2018-07-01 2018-09-04 广西那神晞途环保科技有限公司 ionic mineral precipitation agent and preparation method thereof
CN109402417A (en) * 2018-12-21 2019-03-01 中国科学院广州地球化学研究所 The method for the exploitation Rare Earth Mine that is powered
CN111944996A (en) * 2020-07-10 2020-11-17 五矿(北京)稀土研究院有限公司 In-situ ore leaching method for reducing seepage through air seal
CN112410554A (en) * 2020-11-02 2021-02-26 江西理工大学 Environment-friendly extraction method of ionic rare earth ore calcium salt
CN114892030A (en) * 2022-05-11 2022-08-12 中国地质科学院矿产综合利用研究所 In-situ ore leaching structure and method based on ionic rare earth slope reinforcement

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CN103436720A (en) * 2013-09-18 2013-12-11 许瑞高 Process for leaching rare earth from ion-adsorption type rare earth ore without using ammonium salt
CN104152693A (en) * 2014-07-16 2014-11-19 江西理工大学 Method for precipitating rare earth from ionic rare earth ore magnesium sulfate leaching solution
CN104611547A (en) * 2015-03-09 2015-05-13 龙南县锦易矿业有限公司 Ore leaching process for south rare earth ore
CN105506314A (en) * 2015-12-18 2016-04-20 中铝广西有色崇左稀土开发有限公司 Method for recycling rare-earth rich liquor from volcanic rock ionic type rare earth ores
CN105907959A (en) * 2016-05-16 2016-08-31 龙南县锦易矿业有限公司 Ammonia-free mining method for rare earth ore in south China
CN106367622A (en) * 2016-09-13 2017-02-01 南昌大学 High-efficient and green ion-absorbed-type rear earth extraction method by adopting aluminum sulfate as leaching agent
CN106636683A (en) * 2016-10-14 2017-05-10 赣州弘茂稀土工程有限公司 Rare earth in-situ leaching and enriching process for ionic rare earth ore
CN107217139A (en) * 2017-05-31 2017-09-29 赣州稀土开采技术服务有限公司 Southern ion type rareearth ore is without ammonia production practice

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103266224A (en) * 2013-05-27 2013-08-28 江西理工大学 Ion-adsorption-type rare earth extracting method
CN103436720A (en) * 2013-09-18 2013-12-11 许瑞高 Process for leaching rare earth from ion-adsorption type rare earth ore without using ammonium salt
CN104152693A (en) * 2014-07-16 2014-11-19 江西理工大学 Method for precipitating rare earth from ionic rare earth ore magnesium sulfate leaching solution
CN104611547A (en) * 2015-03-09 2015-05-13 龙南县锦易矿业有限公司 Ore leaching process for south rare earth ore
CN105506314A (en) * 2015-12-18 2016-04-20 中铝广西有色崇左稀土开发有限公司 Method for recycling rare-earth rich liquor from volcanic rock ionic type rare earth ores
CN105907959A (en) * 2016-05-16 2016-08-31 龙南县锦易矿业有限公司 Ammonia-free mining method for rare earth ore in south China
CN106367622A (en) * 2016-09-13 2017-02-01 南昌大学 High-efficient and green ion-absorbed-type rear earth extraction method by adopting aluminum sulfate as leaching agent
CN106636683A (en) * 2016-10-14 2017-05-10 赣州弘茂稀土工程有限公司 Rare earth in-situ leaching and enriching process for ionic rare earth ore
CN107217139A (en) * 2017-05-31 2017-09-29 赣州稀土开采技术服务有限公司 Southern ion type rareearth ore is without ammonia production practice

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108486373A (en) * 2018-07-01 2018-09-04 广西那神晞途环保科技有限公司 ionic mineral precipitation agent and preparation method thereof
CN109402417A (en) * 2018-12-21 2019-03-01 中国科学院广州地球化学研究所 The method for the exploitation Rare Earth Mine that is powered
CN111944996A (en) * 2020-07-10 2020-11-17 五矿(北京)稀土研究院有限公司 In-situ ore leaching method for reducing seepage through air seal
CN112410554A (en) * 2020-11-02 2021-02-26 江西理工大学 Environment-friendly extraction method of ionic rare earth ore calcium salt
CN114892030A (en) * 2022-05-11 2022-08-12 中国地质科学院矿产综合利用研究所 In-situ ore leaching structure and method based on ionic rare earth slope reinforcement
CN114892030B (en) * 2022-05-11 2023-10-17 中国地质科学院矿产综合利用研究所 In-situ mineral leaching structure and method based on ionic rare earth slope reinforcement

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