[go: up one dir, main page]

CN106186006A - A kind of purifying lithium chloride method - Google Patents

A kind of purifying lithium chloride method Download PDF

Info

Publication number
CN106186006A
CN106186006A CN201610597647.6A CN201610597647A CN106186006A CN 106186006 A CN106186006 A CN 106186006A CN 201610597647 A CN201610597647 A CN 201610597647A CN 106186006 A CN106186006 A CN 106186006A
Authority
CN
China
Prior art keywords
lithium chloride
water
mother solution
purifying
wet product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201610597647.6A
Other languages
Chinese (zh)
Other versions
CN106186006B (en
Inventor
包志泉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Hong Hao Science And Technology Ltd
Original Assignee
Zhejiang Hong Hao Science And Technology Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhejiang Hong Hao Science And Technology Ltd filed Critical Zhejiang Hong Hao Science And Technology Ltd
Priority to CN201610597647.6A priority Critical patent/CN106186006B/en
Publication of CN106186006A publication Critical patent/CN106186006A/en
Application granted granted Critical
Publication of CN106186006B publication Critical patent/CN106186006B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D15/00Lithium compounds
    • C01D15/04Halides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/80Compositional purity
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/80Compositional purity
    • C01P2006/82Compositional purity water content

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The invention discloses a kind of purifying lithium chloride method, comprise the following steps: a) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, after heated and stirred, carry out solid-liquid separation operation, obtain lithium chloride wet product A, collect the mother solution of isolated simultaneously;B) crystallization: mother solution is poured in evaporative crystallization still, circulation and evacuation in opening, the most slowly heat up, steamed by the water in mother solution, cool down afterwards, obtain magma;C) dry: magma is carried out solid-liquid separation operation, obtains lithium chloride wet product B, be dried after the lithium chloride wet product obtained is mixed, pack after being dried in two steps.Present invention process is simple, without any medicament, does not produce product and pollutes, and purifying lithium chloride technology yield is high, and energy consumption is low.

Description

A kind of purifying lithium chloride method
Technical field
The present invention relates to lithium compound purification technique field, especially relate to a kind of purifying lithium chloride method.
Background technology
Highly purified lithium metal and lithium compound (purity is not less than 99.9%) have been widely used in various field, as Lithium battery, containing lithium constructional alloy, nuclear energy high-tech, the aluminum lithium constructional alloy etc. of application in Aeronautics and Astronautics;The most nearest tens Year, along with developing rapidly of lithium ion battery industry, the demand of high-purity lithium compound is significantly increased;Highly purified lithium metal and It is that raw material prepares that lithium compound is presently mainly with highly purified lithium chloride (purity is not less than 99.9%);Therefore, height is obtained The lithium chloride of purity is it is critical that a ring.Existing lithium compound uses in environment, to impurity natrium ion in lithium compound Existence require harsher, general requirement≤15ppm, so in some sense, remove impurity natrium ion, become this One of key of control of product quality, and the biggest to the elimination difficulty of impurity natrium ion.
At present, purifying lithium chloride method having carried out substantial amounts of work, the method for purification of conventional chemical chemical industry, as coprecipitated The processes such as shallow lake, fractional crystallization, solvent extraction, ion exchange, the purification to lithium chloride, or not reaching the degree of depth removes impurity Sodium ion, though or technically feasible, but cost is high.Such as Chinese periodical " rare metal ", vol23.No2.P95~99, public affairs Open the document of entitled " from the flow process research of Saturated with Magnesium chloride bittern extraction lithium ", wherein with Qinghai Salt Lake Bittern resource, first After in salt, sodium, potassium, boron are separated into corresponding product, remaining mother solution contains magnesium, lithium valuable constituent, uses containing lithium aqueous solution ground Organic solvent extractionprocess, to separate the impurity such as substantial amounts of magnesium and the sodium of residual, potassium, boron, ferrum in solution;Result shows, this technique Can only obtain qualified industrial chlorinations lithium product, purity does not reaches pure lithium chloride standard, only with regard to impurity natrium content >=1700ppm.
Summary of the invention
For solving the problems referred to above, the invention provides one and have lithium chloride yield height, purity is more than 99.9%, impurity natrium The effective Radix Raphani of ion remaval, purifying lithium chloride method.
For achieving the above object, the technical solution used in the present invention is as follows:
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water Being 1.5~2.0:1.0, heating keeps the temperature at 25~35 DEG C, after stirring 2~3 hours, carries out solid-liquid separation operation, obtains Lithium chloride wet product A, collects the mother solution of isolated simultaneously;
B) crystallization: the mother solution collected in step a is poured in evaporative crystallization still, circulation and evacuation in opening, the most slowly rise Temperature, steams the water in mother solution, stops distillation when 50 that the moisture steamed is mother solution volume~80% and stops evacuation, and It is cooled to less than 20 DEG C, after keeping 2~3 hours, obtains magma;
C) dry: magma step b obtained carries out solid-liquid separation operation, obtains lithium chloride wet product B, by lithium chloride wet product B and It is dried after the lithium chloride wet product A mixing prepared by step a, packs after being dried.
Step a is selected water dissolution lithium chloride crude product, it is preferred to use purified water or deionized water dissolve, and so may be used To reduce the pollution of foreign ion, it is ensured that in purification process, the content of sodium ion reaches minimum;At a temperature of this and under amount of water, chlorine Change lithium solution the most saturated, and sodium ion (existing as sodium chloride in crude product) unsaturation far away, then in crude product lithium chloride Sodium chloride can be dissolved completely in water, and lithium chloride solution has reached supersaturation simultaneously, so substantial amounts of lithium chloride is the most molten Solving, can be obtained by centrifuge dehydration, yield improves, and decreases the energy consumption of evaporation water required behind.
Step b first carries out the water of continuous print evaporative crystallization, i.e. evaporation section, separates out partial oxidation crystalline lithium, due to water It is not vaporized completely, so the sodium ion of trace will not be precipitated, simultaneously in order to make lithium chloride as much as possible separate out, needs Transpiring moistures the most in the case of not separating out ensureing sodium chloride;Next decrease temperature crystalline is started, along with at temperature Fall, lithium chloride crystal can constantly separate out, but owing to the sodium ion of trace exists as sodium chloride, its dissolubility is with temperature Degree impact is less, so sodium chloride crystal separates out hardly.
As preferably, the solid-liquid separation operation in step a and step c is precipitate and separate, centrifugation or filters separation Operation.
As preferably, the solid-liquid separation operation in step a and step c operates for centrifugation.
Although precipitate and separate and filtration separate the effect that also can play solid-liquid separation, but due to precipitate and separate and filtration point In wet product lithium chloride after both PROCESS FOR TREATMENT, water content is higher, can increase the operating pressure of follow-up baking operation, and from The heart separates moisture content less in the wet product lithium chloride obtained, it is possible to reduce the pressure of baking operation.
As preferably, after lithium chloride crude product and water add dissolution kettle in step a, account for the 75~85% of dissolution kettle volume.
As preferably, in step b, after mother solution pours evaporative crystallization still into, in first opening, circulate evacuation again.
As preferably, in step b, aqueous cooling solution is used to cool down.
As preferably, in step b, using chilled brine to cool down, chilled brine concentration is 15~25wt%, freezing salt Temperature≤-10 DEG C of water.
As preferably, in step c, the solution obtained after collecting solid-liquid separation, and upper once purify time add as raw material Enter.
The solution that in step c, magma obtains after solid-liquid separation is also dissolved with the lithium chloride of certain content, receives for improving Rate, using this part solution upper once purify time as raw material add, reduce waste, improve yield.
As preferably, in step c, lithium chloride wet product is dried, moisture≤0.1wt% contained therein.
Therefore, the method have the advantages that
(1) present invention process is simple, without any medicament, does not produce product and pollutes;
(2) the purifying lithium chloride technology yield in the present invention is high, and energy consumption is low.
Detailed description of the invention
Below in conjunction with detailed description of the invention, technical scheme is further described.
Embodiment 1
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water After adding dissolution kettle for 1.5:1.0, lithium chloride crude product and water, accounting for the 75% of dissolution kettle volume, heating keeps the temperature at 25 DEG C, After stirring 2 hours, carry out solid-liquid separation operation, obtain lithium chloride wet product A, collect the mother solution of isolated simultaneously;
B) crystallization: pour in evaporative crystallization still by the mother solution collected in step a, circulates evacuation again in first opening, the most slowly Heat up, the water in mother solution is steamed, stop distillation when 50% that the moisture steamed is mother solution volume and stop evacuation, and adopting Carry out being cooled to 20 DEG C with aqueous cooling solution, after keeping 2 hours, obtain magma;
C) dry: magma step b obtained carries out solid-liquid separation operation, obtains lithium chloride wet product B, by lithium chloride wet product B and Being dried after the lithium chloride wet product A mixing prepared by step a, lithium chloride wet product is dried, and moisture need contained therein≤ 0.1wt%, then packs;After solid-liquid separation, collect the solution obtained after solid-liquid separation, and upper once purify time conduct Raw material adds.
Embodiment 2
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water After adding dissolution kettle for 1.7:1.0, lithium chloride crude product and water, accounting for the 80% of dissolution kettle volume, heating keeps the temperature at 30 DEG C, After stirring 2.5 hours, carry out solid-liquid separation operation, obtain lithium chloride wet product A, collect the mother solution of isolated simultaneously;
B) crystallization: pour in evaporative crystallization still by the mother solution collected in step a, circulates evacuation again in first opening, the most slowly Heat up, the water in mother solution is steamed, stop distillation when 65% that the moisture steamed is mother solution volume and stop evacuation, and adopting Carry out being cooled to 15 DEG C with aqueous cooling solution, after keeping 2.5 hours, obtain magma;
C) dry: magma step b obtained carries out solid-liquid separation operation, obtains lithium chloride wet product B, by lithium chloride wet product B and Being dried after the lithium chloride wet product A mixing prepared by step a, lithium chloride wet product is dried, and moisture need contained therein≤ 0.1wt%, then packs;After solid-liquid separation, collect the solution obtained after solid-liquid separation, and upper once purify time conduct Raw material adds.
Embodiment 3
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water After adding dissolution kettle for 2.0:1.0, lithium chloride crude product and water, accounting for the 85% of dissolution kettle volume, heating keeps the temperature at 35 DEG C, After stirring 3 hours, carry out solid-liquid separation operation, obtain lithium chloride wet product A, collect the mother solution of isolated simultaneously;
B) crystallization: pour in evaporative crystallization still by the mother solution collected in step a, circulates evacuation again in first opening, the most slowly Heat up, the water in mother solution is steamed, stop distillation when 80% that the moisture steamed is mother solution volume and stop evacuation, and adopting Carry out being cooled to 10 DEG C with aqueous cooling solution, after keeping 3 hours, obtain magma;
C) dry: magma step b obtained carries out solid-liquid separation operation, obtains lithium chloride wet product B, by lithium chloride wet product B and Being dried after the lithium chloride wet product A mixing prepared by step a, lithium chloride wet product is dried, and moisture need contained therein≤ 0.1wt%, then packs;After solid-liquid separation, collect the solution obtained after solid-liquid separation, and upper once purify time conduct Raw material adds.
Embodiment 4
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water After adding dissolution kettle for 1.5:1.0, lithium chloride crude product and water, accounting for the 75% of dissolution kettle volume, heating keeps the temperature at 25 DEG C, After stirring 2 hours, carry out precipitate and separate operation, obtain lithium chloride wet product A, collect the mother solution of isolated simultaneously;
B) crystallization: pour in evaporative crystallization still by the mother solution collected in step a, circulates evacuation again in first opening, the most slowly Heat up, the water in mother solution is steamed, stop distillation when 50% that the moisture steamed is mother solution volume and stop evacuation, and adopting Carry out being cooled to 20 DEG C with chilled brine, after keeping 2 hours, obtain magma;Wherein, chilled brine concentration is 15wt%, freezing salt The temperature of water is-10 DEG C;
C) dry: magma step b obtained carries out precipitate and separate operation, obtains lithium chloride wet product B, by lithium chloride wet product B and Being dried after the lithium chloride wet product A mixing prepared by step a, lithium chloride wet product is dried, and moisture need contained therein≤ 0.1wt%, then packs;After precipitate and separate operation, collect the solution that obtains after separating, and upper once purify time conduct Raw material adds.
Embodiment 5
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water After adding dissolution kettle for 1.7:1.0, lithium chloride crude product and water, accounting for the 80% of dissolution kettle volume, heating keeps the temperature at 30 DEG C, After stirring 2.5 hours, it is centrifuged lock out operation, obtains lithium chloride wet product A, collect the mother solution of isolated simultaneously;
B) crystallization: pour in evaporative crystallization still by the mother solution collected in step a, circulates evacuation again in first opening, the most slowly Heat up, the water in mother solution is steamed, stop distillation when 65% that the moisture steamed is mother solution volume and stop evacuation, and adopting Carry out being cooled to 15 DEG C with chilled brine, after keeping 2.5 hours, obtain magma;Wherein, chilled brine concentration is 20wt%, freezing The temperature of saline is-12 DEG C;
C) dry: magma step b obtained is centrifuged lock out operation operation, obtains lithium chloride wet product B, by lithium chloride wet product B and lithium chloride wet product A prepared by step a are dried after mixing, and lithium chloride wet product is dried, and moisture need contained therein≤ 0.1wt%, then packs;After centrifugation operation, collect the solution that obtains after separating, and upper once purify time conduct Raw material adds.
Embodiment 6
A kind of purifying lithium chloride method, comprises the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water After adding dissolution kettle for 2.0:1.0, lithium chloride crude product and water, accounting for the 85% of dissolution kettle volume, heating keeps the temperature at 35 DEG C, After stirring 3 hours, carry out filtering lock out operation, obtain lithium chloride wet product A, collect the mother solution of isolated simultaneously;
B) crystallization: pour in evaporative crystallization still by the mother solution collected in step a, circulates evacuation again in first opening, the most slowly Heat up, the water in mother solution is steamed, stop distillation when 80% that the moisture steamed is mother solution volume and stop evacuation, and adopting Carry out being cooled to 10 DEG C with chilled brine, after keeping 3 hours, obtain magma;Wherein, chilled brine concentration is 25wt%, freezing salt The temperature of water is-15 DEG C;
C) dry: magma step b obtained carries out filtering lock out operation, obtains lithium chloride wet product B, by lithium chloride wet product B and Being dried after the lithium chloride wet product A mixing prepared by step a, lithium chloride wet product is dried, and moisture need contained therein≤ 0.1wt%, then packs;Filter after lock out operation, collect the solution obtained after separating, and upper once purify time conduct Raw material adds.
The technical grade lithium chloride that purity is 97wt% of the raw material lithium chloride crude product employed in above-described embodiment, is passing through Above-mentioned steps purifies the purity of afterchlorinate lithium and is both greater than 99.9wt%, and sodium ions content is all not more than 15ppm, even purity and is more than 99.95wt%, sodium ions content is less than 10ppm.

Claims (9)

1. a purifying lithium chloride method, it is characterised in that comprise the following steps:
A) dissolve: in dissolution kettle, add lithium chloride crude product, and inject a certain amount of water, make the mass ratio of lithium chloride crude product and water Being 1.5~2.0:1.0, heating keeps the temperature at 25~35 DEG C, after stirring 2~3 hours, carries out solid-liquid separation operation, obtains Lithium chloride wet product A, collects the mother solution of isolated simultaneously;
B) crystallization: the mother solution collected in step a is poured in evaporative crystallization still, circulation and evacuation in opening, the most slowly rise Temperature, steams the water in mother solution, stops distillation when 50 that the moisture steamed is mother solution volume~80% and stops evacuation, and It is cooled to less than 20 DEG C, after keeping 2~3 hours, obtains magma;
C) dry: magma step b obtained carries out solid-liquid separation operation, obtains lithium chloride wet product B, by lithium chloride wet product B and It is dried after the lithium chloride wet product A mixing prepared by step a, packs after being dried.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: consolidating in described step a and step c Liquid lock out operation is precipitate and separate, centrifugation or filters lock out operation.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: consolidating in described step a and step c Liquid lock out operation is centrifugation operation.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: lithium chloride crude product in described step a After adding dissolution kettle with water, account for the 75~85% of dissolution kettle volume.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: in described step b, mother solution pours steaming into After sending out crystallization kettle, in first opening, circulate evacuation again.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: in described step b, use cooling water Solution cools down.
7. according to a kind of purifying lithium chloride method described in claim 1 or 6, it is characterised in that: in described step b, use cold Freezing saline to cool down, chilled brine concentration is 15~25wt%, temperature≤-10 DEG C of chilled brine.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: in described step c, collect solid-liquid and divide The solution obtained after from, and upper once purify time as raw material add.
A kind of purifying lithium chloride method the most according to claim 1, it is characterised in that: in described step c, lithium chloride wet product After drying, moisture≤0.1wt% contained therein.
CN201610597647.6A 2016-07-27 2016-07-27 A kind of purifying lithium chloride method Active CN106186006B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610597647.6A CN106186006B (en) 2016-07-27 2016-07-27 A kind of purifying lithium chloride method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610597647.6A CN106186006B (en) 2016-07-27 2016-07-27 A kind of purifying lithium chloride method

Publications (2)

Publication Number Publication Date
CN106186006A true CN106186006A (en) 2016-12-07
CN106186006B CN106186006B (en) 2017-08-25

Family

ID=57495381

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610597647.6A Active CN106186006B (en) 2016-07-27 2016-07-27 A kind of purifying lithium chloride method

Country Status (1)

Country Link
CN (1) CN106186006B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109662991A (en) * 2019-02-20 2019-04-23 郑州大学第附属医院 A kind of drug and preparation method of the treatment diabetic nephropathy based on lithium chloride

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4274834A (en) * 1979-04-11 1981-06-23 Foote Mineral Company Process for purification of lithium chloride
US4588565A (en) * 1984-08-01 1986-05-13 The United States Of America As Represented By The Secretary Of The Interior Separation of lithium chloride from impurities
CN1063663A (en) * 1992-03-05 1992-08-19 化学工业部化工矿山设计研究院 New method for preparing potassium chloride from chloride type potassium-containing brine
US6063345A (en) * 1996-11-04 2000-05-16 Metallgesellschaft Aktiengesellschaft Method of separating NaCl from a LiCl solution
CN1559902A (en) * 2004-02-26 2005-01-05 东北大学 A purification method for removing impurity sodium in lithium chloride
CN1978321A (en) * 2005-11-29 2007-06-13 高崧耀 Process for producing high-purity potassium chloride
JP2011031232A (en) * 2009-08-04 2011-02-17 Kee:Kk Method of manufacturing lithium hydroxide
CN102167369A (en) * 2010-12-06 2011-08-31 兰州大学 Method for reducing content of NaCl in LiCl
RU2012105842A (en) * 2012-02-17 2013-08-27 Закрытое акционерное общество (ЗАО) "Экостра-Наутех" METHOD FOR PRODUCING LITHIUM CONCENTRATE AND LITHIUM COMPOUNDS WITH ITS USE FROM LITHIUM-BEARING NATURAL BRINS
US20140227154A1 (en) * 2009-04-24 2014-08-14 Simbol Inc. Preparation of Lithium Carbonate From Lithium Chloride Containing Brines
CN205170407U (en) * 2015-07-21 2016-04-20 湖北瑞邦石化装备科技有限公司 Purification anhydrous lithium chloride's composite set among mixtures of follow sodium chloride and lithium chloride

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4274834A (en) * 1979-04-11 1981-06-23 Foote Mineral Company Process for purification of lithium chloride
US4588565A (en) * 1984-08-01 1986-05-13 The United States Of America As Represented By The Secretary Of The Interior Separation of lithium chloride from impurities
CN1063663A (en) * 1992-03-05 1992-08-19 化学工业部化工矿山设计研究院 New method for preparing potassium chloride from chloride type potassium-containing brine
US6063345A (en) * 1996-11-04 2000-05-16 Metallgesellschaft Aktiengesellschaft Method of separating NaCl from a LiCl solution
CN1559902A (en) * 2004-02-26 2005-01-05 东北大学 A purification method for removing impurity sodium in lithium chloride
CN1978321A (en) * 2005-11-29 2007-06-13 高崧耀 Process for producing high-purity potassium chloride
US20140227154A1 (en) * 2009-04-24 2014-08-14 Simbol Inc. Preparation of Lithium Carbonate From Lithium Chloride Containing Brines
JP2011031232A (en) * 2009-08-04 2011-02-17 Kee:Kk Method of manufacturing lithium hydroxide
CN102167369A (en) * 2010-12-06 2011-08-31 兰州大学 Method for reducing content of NaCl in LiCl
RU2012105842A (en) * 2012-02-17 2013-08-27 Закрытое акционерное общество (ЗАО) "Экостра-Наутех" METHOD FOR PRODUCING LITHIUM CONCENTRATE AND LITHIUM COMPOUNDS WITH ITS USE FROM LITHIUM-BEARING NATURAL BRINS
CN205170407U (en) * 2015-07-21 2016-04-20 湖北瑞邦石化装备科技有限公司 Purification anhydrous lithium chloride's composite set among mixtures of follow sodium chloride and lithium chloride

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
孙建之等: "氯化锂的应用与生产方法研究进展", 《海湖盐与化工》 *
白仟等: "钾盐开采—加工技术及其对产业发展的影响", 《资源与产业》 *
金哲男等: "乙醇萃取法制备低Na ,K高纯氯化锂", 《东北大学学报( 自然科学版)》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109662991A (en) * 2019-02-20 2019-04-23 郑州大学第附属医院 A kind of drug and preparation method of the treatment diabetic nephropathy based on lithium chloride

Also Published As

Publication number Publication date
CN106186006B (en) 2017-08-25

Similar Documents

Publication Publication Date Title
KR102251421B1 (en) Recovery of lithium from low content extracted tail water and recycling method of extracted tail water
CN105271347B (en) Method for preparing high-purity barium salt by using witherite-barytocalcite industrial waste residues
CN112158858A (en) Method for preparing ammonium bifluoride by using BOE waste liquid
WO2022122028A1 (en) Method and device for back-extraction purification of crude product obtained by sublimation of maltol or ethyl maltol
CN108910949A (en) The preparation method of high-purity potassium floutaramite
CN112047362A (en) Multistage purification equipment and process for high-salt-content wastewater
CN115818671A (en) Method for crystallizing and purifying sodium carbonate of incineration product
CN106186006A (en) A kind of purifying lithium chloride method
CN107459472B (en) Method for refining dimethyl sulfoxide solvent in carbon fiber precursor production process
Wei et al. Centrifugation forced ice-concentrate separation to enhance suspension freezing desalination performance
Sun et al. Manufacture of sodium-free lithium chloride from salt lake brine
CN107963669B (en) A kind of calcium removal methods of technical grade sulfuric acid manganese
CN106278823A (en) A kind of preparation method of natural Broneolum Syntheticum
CN102826959B (en) Method for extracting erythritol from erythritol mother liquor
CN102633293B (en) Method for refining multistage circulation evaporation-free copper sulfate
CN1951817A (en) Method for separating magnesium and enriching lithium from brine of saline lake using high temperature evaporation and crystallization method
CN111020632B (en) Method for recovering electrolytic fluorine waste electrolyte
CN109292798B (en) Process for producing anhydrous lithium chloride by crystallization method
CN113511662A (en) Purification method of waste salt containing sodium sulfate
CN109574047B (en) Method for recovering high-purity efavirenz and lithium chloride from medical lithium-containing waste liquid
CN103788112A (en) Method for preparing biotin by debenzylating benzyl biotin
CN118221140A (en) Method for extracting lithium carbonate from lithium-containing solution
CN109796371A (en) A kind of crystallization and purification technique of Bravo
CN116623009A (en) Method for comprehensively recovering lithium, rubidium and cesium from lithium ore leaching solution
CN104605307B (en) A kind of preparation method of ecosystem edible salt

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CB03 Change of inventor or designer information

Inventor after: Weng Min

Inventor after: Bao Zhiquan

Inventor before: Bao Zhiquan

CB03 Change of inventor or designer information
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A purification method of lithium chloride

Effective date of registration: 20221024

Granted publication date: 20170825

Pledgee: Zhejiang Suichang Rural Commercial Bank Co.,Ltd.

Pledgor: ZHEJIANG HONGHAO TECHNOLOGY CO.,LTD.

Registration number: Y2022330002781

PE01 Entry into force of the registration of the contract for pledge of patent right