CN1093517C - Lithium salt extraction process from carbonate type bittern - Google Patents

Lithium salt extraction process from carbonate type bittern Download PDF

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Publication number
CN1093517C
CN1093517C CN99105828A CN99105828A CN1093517C CN 1093517 C CN1093517 C CN 1093517C CN 99105828 A CN99105828 A CN 99105828A CN 99105828 A CN99105828 A CN 99105828A CN 1093517 C CN1093517 C CN 1093517C
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lithium
salt
bittern
carbonate type
water
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CN1270927A (en
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郑绵平
郭珍旭
张永生
杨卉芃
卜令忠
李琦
邓月金
赵元艺
张克仁
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R&D CENTER FOR SALINE LAKE AND EPITHERMAL DEPOSIT CAGS
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R&D CENTER FOR SALINE LAKE AND EPITHERMAL DEPOSIT CAGS
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    • 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
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    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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    • Y02P20/133Renewable energy sources, e.g. sunlight

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Abstract

The present invention provides a method for extracting lithium salts from carbonate type brine, which takes high-lithium and low-sulfate radical brine in a plateau cold-stage lithium salt lake as raw materials; after mixed Li2CO3 salts of which the concentration is 5% are obtained by a salt field technology, lithium concentrates of which the concentration is 68% and the recovery rate is 76% can be separated out by a secondary scrubbing flow by water. CO2 is introduced to convert the Li2CO3 in solution into LiHCO3, and then the solution is heated to enable the Li2CO3 to be precipitated to obtain lithium carbonate products; the byproducts such as boron, potassium, etc. can be recovered. The whole technological flow is simple and advanced and has easy operation; solar energy and cold resources are fully utilized, the consumed energy is little, the consumed materials are few, and the environment can not be polluted, the economic benefit is high.

Description

Lithium salt extraction process from carbonate type bittern
The present invention relates to a kind of extracting method of lithium salts, particularly from the carbonate type salt lake brine, extract the method for Quilonum Retard.
Because the electrochemical activity of lithium is strong, is again light metal, thereby has purposes widely.The demand of lithium is constantly increasing, particularly as the compound Quilonum Retard of lithium.
In world's lithium total resources, bittern lithium ore deposit accounts for 75%, and hard rock lithium ore deposit accounts for 25%, and China bittern lithium ore deposit accounts for 72%, and hard rock lithium ore deposit accounts for 28%.Before the sixties, lithium resource is mainly from hard rock lithium ore.The salt lake carry the lithium cost than the low 1-1.5 of hard rock doubly more than, this forces the industrial development of Chinese lithium must pay attention to putting forward from salt lake brine the method for lithium.It is the best outlet of developing china lithium industry.
Because it is different with the economic technology condition to contain lithium salts lake water chemical type, so the operational path that adopts also has nothing in common with each other.At present in the method for from bittern, carrying lithium, organic ion (TBP, be tributyl phosphate etc.) exchange resin method, inorganic ion exchanger method, aluminate method, hydrogenchloride saltout method and the precipitator method (being phosphate process) and carbon method etc. are arranged.Chinese patent application numbers 941116387 discloses a kind of method of extracting lithium salts from bittern, this method is, with high-carbon hydrochlorate type bittern behind the Exposure to Sunlight pre-concentration, logical carbonic acid gas carries out carbonization, make yellow soda ash change into the sodium bicarbonate precipitation, filter then, behind the further enrichment method lithium of Exposure to Sunlight, add yellow soda ash again, be settled out Quilonum Retard.Its shortcoming is: 1. need to consume a large amount of mineral fuel, get CO in the limestone with burning 2, Quilonum Retard per ton need consume coal more than 6 tons; 2. its bittern lithium salts rate of recovery lower (about 35%) can not sufficiently and reasonably be utilized local resources; 3. this method is not considered comprehensive utilization.
The object of the present invention is to provide a kind ofly have inconvenient traffic on the plateau, high and cold anoxic and lack area such as fossil energy, utilize natural condition (sun power and cold resource), the power consumption feed consumption is few, and technological operation is simple and easy, the lithium method of carrying from carbonate type bittern of pollution-free and high benefit.
Technical solution of the present invention is:
1. utilize plateau cold conditions of living in to impel Na 2SO 410H 2The a large amount of sedimentary resources characteristics of O extract the low sulfate radical bittern of high lithium and make raw material from the salt lake;
2. adopting multistage freezing Exposure to Sunlight on-swimmer's pool-control pond-crystallizing pond-mother liquor pond (Fig. 1).Make halite, saltcake separate (evaporation precipitation) in a large number in the shallow pond of Exposure to Sunlight, make lithium in bittern, reach pre-concentration, focus on the control pond then, with the lithium content 1500-2800mg/l of bittern and temperature more than 5 ℃, control is fallen halogen to crystallizing pond, make enrichment higher-grade in the crystallizing pond, high lithium mixed salt that thickness is big, it contains Li 2CO 3Grade is more than 5%;
3. use on the spot mud and make salt pan substrate and mud and halite blending and constitute " salt cement concrete ", construct salt pan key facility-water proof earth dyke;
4. adopt clear water to clean the mixed salt novel process, with mixed salt (raw ore)<10 millimeter (Li 2CO 35% ±) use scrub water I-first road classification-scouring II-second road scouring-classification-dehydration-lithium concentrate, tail washings reclaims.This method can will contain Li 2CO 35% mixed salt (raw ore) sub-elects through secondary scouring flow process and contains Li 2CO 3Reach or greater than 68%, the Quilonum Retard concentrate (Fig. 2) of the rate of recovery 76%;
5. the impurity at concentrate comprises water-soluble and solubility in citric acid or sour insoluble characteristics, takes water logging to remove water-soluble salt, then with CO 2Leach Li 2CO 3Carbon soak method, the latter uses LiHCO 3Solubleness is than Li 2CO 3High 3--4 characteristic (Fig. 3) doubly, with concentrate add water-soak except that water-soluble salt class (halite, sylvite and borax etc. are reclaimed in evaporation)-wash thick Li 2CO 3, after it is dissolved in water, in solution, feed CO 2, make the Li in the solution 2CO 3Be converted into LiHCO 3, increase lithium content in the solution:
Solution is heated to 50-150 ℃ then, makes Li 2CO 3A large amount of precipitations, CO 2From solution, overflow (recycling use), obtain finished product Li 2CO 3Product.
This cover is put forward the lithium method and is had and suit measures to local conditions, and obtains to contain Li 2CO 3Reach 99% high grade Li 2CO 3Product, and can comprehensively reclaim salt byproducts such as boron potassium.
Advantage of the present invention is:
At carbonate type lithium salts lake characteristic and plateau Yanhu District nature and economic technology characteristics, suit measures to local conditions, maximize favourable factors and minimize unfavourable ones, by the optimization method of design studies and examination, for finding an economical and effective novel process method in the abundant lithium salts lake of exploitation under high conditions.
1. use novel salt field process, can make full use of the advantage of the climate resources (sun power and cold resource) of nature, make and be easy to dispersive Li in the bittern 2CO 3A large amount of concentrate precipitation and extract, and reduce cost to greatest extent and reduce the consumption of mineral fuel.
2. utilization scouring method is from mixed salt (raw ore) sorting Li 2CO 3Concentrate is the sorting agent with the most cheap Freshwater resources, replaces flotation agent such as coco amine, obtains at the scene to contain higher-grade (more than 68%) Li 2CO 3Concentrate not only reduces the sorting cost significantly, has avoided little poisonous substance matter contaminate environment, and reduces long-distance useless transportation in a large number.
3. comprise water-soluble and solubility in citric acid or sour insoluble characteristics at selecting the concentrate impurities, take carbon to soak the method novel process.
This cover is put forward the lithium method and is had to suit measures to local conditions to obtain and contain Li 2CO 3Reach 99% high grade Li 2CO 3Product, and have the practicality and the advance of salts such as comprehensive recovery boron potassium.
4. make " salt cement concrete " with local mud and construct water proof materials such as water proof earth dyke substituted type plastic film, can save a large amount of expenses of building the big area salt pan.
Description of drawings
Fig. 1. be salt pan of the present invention sinker flow sheet
Fig. 2. be the present invention's scouring-grading technology schema
Fig. 3. for carbon of the present invention soaks method purification schemes figure
The rich caesium bromine of the rich potassium boron of the high lithium mixed salt of 1-1 halite sodium chloride crystal section .1-2 halite crystallized region .2. crystallized region .3. mixed salt crystallized region .4. potassium boron mother liquor among Fig. 1
Implementation result: at carbonate type lithium salts lake, as novel type lithium salts lake, Zha Buye lake, Tibet, according to technical scheme of the present invention, the implementation result of obtaining sees Table 1.
Table 1 implementation result table
The name of an article Contain Li 2CO 3(%) Quantity (kg) Rate of recovery % Remarks
Mixed salt 4.5-5.2 65000 70 Pilot scale
Concentrate 65-70 2100 76 Pilot scale
Product 98-99 100 96 Finish lab scale, just set about pilot scale

Claims (3)

1. from carbonate type bittern, extract the method for Quilonum Retard, it is characterized in that:
(1). utilize salt lake, plateau cold conditions of living in to impel Na 2SO 410H 2O precipitates in a large number, extracts the low sulfate radical bittern of high lithium and makes raw material;
(2). raw brine is sent into multistage freezing Exposure to Sunlight on-swimmer's pool earlier, freezing Exposure to Sunlight, after enter the control pond, controlled temperature more than 5 ℃, the lithium content of bittern is at 1500-2800mg/l, sends into the crystallizing pond crystallization again, can obtain Li 2CO 3Content is at the high lithium mixed salt more than 5%;
(3). high lithium mixed salt through the clear water secondary clean, classification, dewater afterwards lithium concentrate;
(4). remove water soluble salt in the lithium concentrate with water logging, halite, sylvite and borax are reclaimed in evaporation, wash thick Li 2CO 3, be dissolved in water again, in solution, feed CO 2, make Li 2CO 3Become LiHCO 3,, make LiHCO by thermolysis 3Become Li 2CO 3
2. the method for extracting Quilonum Retard from carbonate type bittern according to claim 1 is characterized in that, uses the mud on the spot of fusion halite to construct salt pan water proof earth dyke.
3. the method for extracting Quilonum Retard from carbonate type bittern according to claim 1 is characterized in that described heat decomposition temperature is at 50-150 ℃.
CN99105828A 1999-04-20 1999-04-20 Lithium salt extraction process from carbonate type bittern Expired - Lifetime CN1093517C (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109824067A (en) * 2018-12-22 2019-05-31 魏万仁 Natural evaporation crystallization analysis lithium, joint heating crystallization analysis lithium+dissolution wash lithium and extract lithium concentrate

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100343399C (en) * 2002-12-27 2007-10-17 中国科学院青海盐湖研究所 Process for extracting lithium from salt lake brine by manganese dioxide
CN100478278C (en) * 2007-01-10 2009-04-15 青海省地质调查院 Preparation method of lithium carbonate by using brine of oil field
CN102320809A (en) * 2011-08-03 2012-01-18 山发寿 Preparation and application of rock salt concrete
CN102491378B (en) * 2011-10-14 2013-02-20 陈兆华 Producing method for preparing lithium carbonate by taking carbonate type brine and sulphate type brine as raw material and by repeatedly mixing brine
CN102502720B (en) * 2011-10-27 2013-08-21 白银扎布耶锂业有限公司 Process for producing battery-grade lithium carbonate through processing carbonate type lithium concentrate by deep carbonation method
CN102910652A (en) * 2012-10-18 2013-02-06 中国科学院青海盐湖研究所 Clean production process of plateau sulfate type boron-lithium salt lake brine
CN103318928B (en) * 2013-06-20 2014-12-03 西藏金浩投资有限公司 Method and system for rapid extraction of lithium carbonate from salt lake water
CN103934112B (en) * 2014-04-04 2016-08-31 湖南有色金属研究院 A kind of beneficiation method of lithium Ore
CN105883862B (en) * 2016-04-07 2018-02-16 中国科学院青海盐湖研究所 The method that lithium carbonate is prepared from the carbonate type bittern of plateau
CN107337217B (en) * 2016-04-28 2020-03-06 中国地质科学院盐湖与热水资源研究发展中心 System and method for concentrating and separating light salt lake brine
CN109179455B (en) * 2018-09-29 2021-02-09 吉林大学 Method for enriching lithium salt and simultaneously extracting potassium salt from carbonate type salt lake brine
CN111439761A (en) * 2020-02-19 2020-07-24 江西赣锋锂业股份有限公司 Method for preparing high-purity lithium carbonate through continuous carbonization and decomposition
CN115418498B (en) * 2022-08-23 2023-12-12 广东邦普循环科技有限公司 Treatment method of carbonate lithium clay

Citations (2)

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Publication number Priority date Publication date Assignee Title
CN1069958A (en) * 1992-06-20 1993-03-17 轻工业部制盐工业科学研究所 A kind of material that can be used for salt pan (pond)
CN1106358A (en) * 1994-02-04 1995-08-09 地质矿产部西藏自治区中心实验室 Method for extracting lithium salt from brine

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1069958A (en) * 1992-06-20 1993-03-17 轻工业部制盐工业科学研究所 A kind of material that can be used for salt pan (pond)
CN1106358A (en) * 1994-02-04 1995-08-09 地质矿产部西藏自治区中心实验室 Method for extracting lithium salt from brine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109824067A (en) * 2018-12-22 2019-05-31 魏万仁 Natural evaporation crystallization analysis lithium, joint heating crystallization analysis lithium+dissolution wash lithium and extract lithium concentrate

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