JPS5939719A - Manufacture of high purity lithium carbonate - Google Patents

Manufacture of high purity lithium carbonate

Info

Publication number
JPS5939719A
JPS5939719A JP14766882A JP14766882A JPS5939719A JP S5939719 A JPS5939719 A JP S5939719A JP 14766882 A JP14766882 A JP 14766882A JP 14766882 A JP14766882 A JP 14766882A JP S5939719 A JPS5939719 A JP S5939719A
Authority
JP
Japan
Prior art keywords
lithium
high purity
lithium carbonate
perchlorate
lithium perchlorate
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.)
Pending
Application number
JP14766882A
Other languages
Japanese (ja)
Inventor
Teruhiko Naito
内藤 輝彦
Yuji Kando
観堂 雄二
Toshiyasu Ikeda
池田 稔保
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.)
KANTO KOATSU KAGAKU KK
Original Assignee
KANTO KOATSU KAGAKU KK
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 KANTO KOATSU KAGAKU KK filed Critical KANTO KOATSU KAGAKU KK
Priority to JP14766882A priority Critical patent/JPS5939719A/en
Publication of JPS5939719A publication Critical patent/JPS5939719A/en
Pending legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To obtain simply and efficiently high purity lithium carbonate suitable for use as a material for the optical industry by converting a crude lithium compound into lithium perchlorate, recrystallizing the lithium perchlorate, and reacting it with carbon dioxide in the presence of ammonia. CONSTITUTION:A crude lithium compound such as industrial lithium carbonate, industrial lithium hydroxide or industrial lithium oxide is dissolved in an aqueous soln. of perchloric acid. The resulting soln. is concentrated or merely cooled to crystallize and separate lithium perchlorate. The lithium perchlorate is recrystallized using water or an org. solvent such as ethyl ether to obtain high purity lithium perchlorate. The high purity lithium perchlorate is dissolved in pure water, the resulting soln. is made basic by adding ammonia, and carbon dioxide is blown into the basic soln. and reacted to precipitate high purity lithium carbonate. The high purity lithium carbonate is taken out by filtration.

Description

【発明の詳細な説明】 本発明は粗製リチウム化合物よシ高純度の炭酸リチウム
を製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing high purity lithium carbonate from a crude lithium compound.

高純度の炭酸リチウムは近年電子工業材料、光工業材料
としての需要が増大している。これらの材料に使用され
る炭酸リチウムは極めて純度の高いものが要求され、従
来の再結晶あるいは再沈澱法などによる高純度の炭酸リ
チウムの製造法は、極めて手数がかかるだけでなく歩留
りも悪いので、精製にはかなりの経費が必要であった。
Demand for high-purity lithium carbonate as a material for electronic and optical industries has increased in recent years. The lithium carbonate used in these materials requires extremely high purity, and conventional methods of producing high-purity lithium carbonate, such as recrystallization or reprecipitation, are not only extremely time-consuming but also have low yields. , Refining required considerable expense.

本発明は粗製リチウム化合物中に含まれる不純物を簡単
かつ効率よく除去し、高純度の炭酸リチウムを製造する
方法を提供するもので、粗製リチウム化合物を過塩素酸
水溶液に溶解し、この溶液を濃縮冷却または単に冷却し
て過塩素酸す1クムの結晶を晶出させて単離した後、水
およびまたは有機溶剤を用いて再結晶させ、次いでこの
結晶を声媒の中でアンモニア性塩基性下で、二酸化炭素
と反応させることから成る。
The present invention provides a method for easily and efficiently removing impurities contained in a crude lithium compound and producing high-purity lithium carbonate. Crystals of 1 cum perchlorate are crystallized and isolated by cooling or simply cooling, then recrystallized using water and/or organic solvents, and the crystals are then crystallized in a vocal medium under ammoniacal base. It consists of reacting with carbon dioxide.

本発明の製造法は過塩素酸リチウムの特異の性質を利用
し、リチウムの精製を過塩素酸リチウムの段階で行うこ
とを特徴とし、十分精製したyFIIi塩素酸リチウム
を用いて常法によりアンモニア塩基性の下で、二酸化炭
素と反応させて高純度の炭酸リチウムを得るものである
The production method of the present invention is characterized by utilizing the unique properties of lithium perchlorate and purifying lithium at the stage of lithium perchlorate. Highly purified lithium carbonate is obtained by reacting with carbon dioxide under the same conditions.

本発明で使用する粗製リチウム化合物としては例えば炭
酸リチクム、水酸化リチウム3、塩化リチウムなどの工
業用リチウム化合物であるが、一般には工業用炭酸リチ
ウムが用いられる。
The crude lithium compound used in the present invention includes, for example, industrial lithium compounds such as lithium carbonate, lithium 3 hydroxide, and lithium chloride, but industrial lithium carbonate is generally used.

工業用炭酸リチウムを用いた場合の高純度炭酸リチウム
の製造法について説明すると、市販の工業用炭酸リチウ
ムは通常炭酸リチウムとして99−以上を含有するが、
不純物として微量のカリウム、ナトリウム、マグネシウ
ム、鉄、カルシウムなどの塩類も含まれている。この粗
製炭酸リチウムから高純度の炭酸リチウムを得るには、
まず仁れを例えば1喚用の601%の過塩素酸に溶解さ
せて過塩素酸リチウムにする。過塩素酸リチウムの水に
対する溶解度は大きくもなく、また小さくも欺く中程度
であるので再結晶、精製の目的には好/ 都合であり、一般の過塩素酸塩類はアルカリ土金属塩類
をけじめとして水に対する溶解度が大きいので極めて好
都合に精製することができる。過塩素酸リチウムを含有
する水溶液を冷却または濃縮冷却すると過塩素酸リチウ
ムは三水塩の形で比較的大きな取扱い容易な結晶として
析出する。これtF別し、水洗、脱水すればかなり純度
の高い過塩素酸リチウムが得られる。ζうして得られた
過塩素酸リチウムを純水を用いて再結晶を繰返して行な
えば、更に純度の高い過塩素酸リチウムの三水塩が得ら
れる。また過塩素酸リチウムは他の過塩素酸金属塩と異
なり、有機溶剤、特にエーテルに対する溶解度が特異的
に大きいので、精製された三水塩を例えばエチルエーテ
ルに加えれば、過塩素酸リチウムはエーテル層に移り、
他の不純物を水層に残し分離精製することができる。
To explain the method for producing high-purity lithium carbonate using industrial lithium carbonate, commercially available industrial lithium carbonate usually contains 99 or more as lithium carbonate,
It also contains trace amounts of salts such as potassium, sodium, magnesium, iron, and calcium as impurities. To obtain high purity lithium carbonate from this crude lithium carbonate,
First, the kernels are dissolved in, for example, 601% perchloric acid to make lithium perchlorate. The solubility of lithium perchlorate in water is neither large nor deceptively small, so it is favorable/convenient for the purpose of recrystallization and purification, and general perchlorates are superior to alkaline earth metal salts. Due to its high solubility in water, it can be purified very conveniently. When an aqueous solution containing lithium perchlorate is cooled or concentrated and cooled, lithium perchlorate precipitates in the form of trihydrate as relatively large crystals that are easy to handle. If this is separated by tF, washed with water, and dehydrated, lithium perchlorate of considerably high purity can be obtained. ζ If the thus obtained lithium perchlorate is repeatedly recrystallized using pure water, a trihydrate of lithium perchlorate with even higher purity can be obtained. Also, unlike other metal perchlorates, lithium perchlorate has a uniquely high solubility in organic solvents, especially ether, so if purified trihydrate is added to ethyl ether, for example, lithium perchlorate will dissolve into ether. Moving on to the layers,
Other impurities can be left in the aqueous layer for separation and purification.

これよシ高純度炭酸リチウムを得るには、かくして精製
された過塩素酸リチウムを純水に溶解し、アンモニアを
加えて塩基性とし、二酸化炭素を吹き込んで炭酸リチウ
ムを沈澱させる。この際加温すると沈澱の生成を容易に
することができる。使昂スるアンモ=1および二酸化炭
素はできるだけグ 高純度のものが必要であり、アンモニアはガス状のもの
を用いるのが好ま1−<、二酸化炭素もガス状のものが
望ましい。得られた結晶は水洗、脱水、乾燥して高純度
炭酸リチウムとする。
In order to obtain highly purified lithium carbonate, the thus purified lithium perchlorate is dissolved in pure water, ammonia is added to make it basic, and carbon dioxide is blown in to precipitate lithium carbonate. At this time, heating can facilitate the formation of a precipitate. The ammonia and carbon dioxide to be used need to be as highly purified as possible; ammonia is preferably gaseous, and carbon dioxide is also preferably gaseous. The obtained crystals are washed with water, dehydrated, and dried to obtain high purity lithium carbonate.

次に本発明を実施例によシ説明するが、その主旨はこれ
らの例にのみ限定されるものではない。
Next, the present invention will be explained with reference to examples, but the gist thereof is not limited only to these examples.

なお実施例中、部は重量部を表わす。In the examples, parts represent parts by weight.

実施例1 工業用炭酸リチウム75部を水650部の中に入れて攪
拌し、これに60%工業用過塩素酸320部を徐々に加
えた。加え終り九ら約15分間そのtま攪拌した後、濾
過した。F液を約4になるまで濃縮し放冷すると過塩素
酸リチウムの三水塩が析出した。これを濾過して水洗し
、遠心分離器で脱水すると220部の過塩素酸リチウム
の三水塩が得られ、収率は6B、8%であった。この結
晶を再び150部の純水に入れ攪拌溶解した後、濃縮、
冷却し更に高純度の過塩素酸リチウムを得た。
Example 1 75 parts of industrial lithium carbonate were stirred in 650 parts of water, and 320 parts of 60% industrial perchloric acid was gradually added thereto. After the addition was complete, the mixture was stirred for about 15 minutes and then filtered. When the F solution was concentrated to a concentration of about 4 and allowed to cool, trihydrate of lithium perchlorate was precipitated. This was filtered, washed with water, and dehydrated using a centrifuge to obtain 220 parts of lithium perchlorate trihydrate, with a yield of 6B and 8%. The crystals were again put into 150 parts of pure water, stirred and dissolved, and then concentrated.
After cooling, highly purified lithium perchlorate was obtained.

実施例2 工業用炭酸リチウム75部を水650部の中に入れて攪
拌し、これに70%工業用過塩素酸265で濃縮し放冷
すると過塩素酸リチウム三水塩の結晶が析出した。これ
を濾過し、遠心分離器で脱水すると250部の過塩素酸
リチウム三水塩が得られ。
Example 2 75 parts of industrial lithium carbonate were stirred in 650 parts of water, concentrated with 70% industrial perchloric acid 265, and allowed to cool to precipitate crystals of lithium perchlorate trihydrate. This was filtered and dehydrated using a centrifuge to obtain 250 parts of lithium perchlorate trihydrate.

収率は7a1チであった。The yield was 7a1.

これに10部の純水と300部のエチルエーテルを加え
、よく振盪してから静置した後、エーテル部を分離し、
減圧でエーテルを除去した。減圧し九デシケータ−の中
で乾燥すると過塩素酸リチウム145部が得られた。こ
れを更に純水150部の中に投じ、再結晶し高純度の過
塩素酸リチウム三水塩を得た。
Add 10 parts of pure water and 300 parts of ethyl ether to this, shake well and leave to stand, then separate the ether part,
Ether was removed under reduced pressure. After drying in a vacuum desiccator, 145 parts of lithium perchlorate was obtained. This was further poured into 150 parts of pure water and recrystallized to obtain highly pure lithium perchlorate trihydrate.

実施例3 実施例1および2の方法で得られた十分に精製された過
塩素酸リチウム三水塩160部を純水160部と共に容
器に入れ攪拌して溶解し、アンモニアガスを吹込み1次
に二酸化炭素ガスを吹込みながら反応させると炭酸リチ
ウムが沈澱した。計算量のアンモニアガスおよび二酸化
炭素ガスを吹込んだ後、加熱し80Cで一時間更にアン
モニアガスおよび二酸化炭素ガスを吹込んで反応を続け
た。反応液を冷却後、炭酸リチウムを分離し、水洗、乾
燥して高純度炭酸リチウムを得た。収量は65部、収率
は88%であった。
Example 3 160 parts of sufficiently purified lithium perchlorate trihydrate obtained by the method of Examples 1 and 2 was put into a container with 160 parts of pure water, stirred and dissolved, and ammonia gas was blown into the primary solution. When reacting while blowing carbon dioxide gas into the solution, lithium carbonate precipitated. After blowing in calculated amounts of ammonia gas and carbon dioxide gas, the reaction was continued by heating and blowing in ammonia gas and carbon dioxide gas for one hour at 80C. After cooling the reaction solution, lithium carbonate was separated, washed with water, and dried to obtain high purity lithium carbonate. The yield was 65 parts, or 88%.

含有される不純物の量は次表のごとくであった。The amount of impurities contained was as shown in the following table.

なお表中の数値は騨、NDは検出せずの意味を表わす。In addition, the numerical values in the table represent the value of 0, and ND represents not detected.

また高純度炭酸リチウム(1)および(2)は、それぞ
れ実施例1の方法および実施例2の方法で得られた過塩
素酸リチウムを用いて製造したものである。
Further, high purity lithium carbonate (1) and (2) were produced using lithium perchlorate obtained by the method of Example 1 and the method of Example 2, respectively.

Claims (1)

【特許請求の範囲】[Claims] を晶出させて単離した後、水およびまたは有機溶剤を用
いて再結晶させ、次いでこの結晶を溶媒の中でアンモニ
ア性塩基性下で、二酸化炭素と反応させることを特徴と
する高純度炭酸リチウムの製造法。
High purity carbonic acid characterized by crystallizing and isolating it, recrystallizing it using water and/or an organic solvent, and then reacting the crystals with carbon dioxide in a solvent under ammoniacal basicity. Lithium production method.
JP14766882A 1982-08-27 1982-08-27 Manufacture of high purity lithium carbonate Pending JPS5939719A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14766882A JPS5939719A (en) 1982-08-27 1982-08-27 Manufacture of high purity lithium carbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14766882A JPS5939719A (en) 1982-08-27 1982-08-27 Manufacture of high purity lithium carbonate

Publications (1)

Publication Number Publication Date
JPS5939719A true JPS5939719A (en) 1984-03-05

Family

ID=15435565

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14766882A Pending JPS5939719A (en) 1982-08-27 1982-08-27 Manufacture of high purity lithium carbonate

Country Status (1)

Country Link
JP (1) JPS5939719A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62252315A (en) * 1986-04-23 1987-11-04 Nippon Chem Ind Co Ltd:The High-purity lithium carbonate and production thereof
WO1993012034A1 (en) * 1991-12-12 1993-06-24 Olin Corporation Process for producing lithium perchlorate
KR100725589B1 (en) 2006-04-19 2007-06-08 한밭대학교 산학협력단 Preparation of lithium hydroxide monohydrate from spent lithium carbonate
JP2008261339A (en) * 1996-06-18 2008-10-30 3M Co Installation mat and contamination inhibition device
CN102139861A (en) * 2011-05-10 2011-08-03 湖北百杰瑞新材料有限公司 Method for producing anhydrous lithium perchlorate
JP2012116681A (en) * 2010-11-30 2012-06-21 Nittetsu Mining Co Ltd Method for producing lithium carbonate
KR101179505B1 (en) 2010-12-14 2012-09-07 서강대학교산학협력단 Preparation of Lithium Hydroxide Monohydrate from Lithium Carbonate
US8394333B2 (en) 2008-12-10 2013-03-12 Nichias Corporation Holding material for catalytic converter, method for producing the same, and catalytic converter
JP2013193940A (en) * 2012-03-22 2013-09-30 Nittetsu Mining Co Ltd Method of producing lithium carbonate
CN103449481A (en) * 2012-05-29 2013-12-18 日铁矿业株式会社 Preparation method of lithium carbonate

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62252315A (en) * 1986-04-23 1987-11-04 Nippon Chem Ind Co Ltd:The High-purity lithium carbonate and production thereof
JPH0449489B2 (en) * 1986-04-23 1992-08-11 Nippon Chemical Ind
WO1993012034A1 (en) * 1991-12-12 1993-06-24 Olin Corporation Process for producing lithium perchlorate
JP2008261339A (en) * 1996-06-18 2008-10-30 3M Co Installation mat and contamination inhibition device
KR100725589B1 (en) 2006-04-19 2007-06-08 한밭대학교 산학협력단 Preparation of lithium hydroxide monohydrate from spent lithium carbonate
US8394333B2 (en) 2008-12-10 2013-03-12 Nichias Corporation Holding material for catalytic converter, method for producing the same, and catalytic converter
JP2012116681A (en) * 2010-11-30 2012-06-21 Nittetsu Mining Co Ltd Method for producing lithium carbonate
US8920763B2 (en) 2010-11-30 2014-12-30 Nittetsu Mining Co., Ltd. Method for producing lithium carbonate
KR101179505B1 (en) 2010-12-14 2012-09-07 서강대학교산학협력단 Preparation of Lithium Hydroxide Monohydrate from Lithium Carbonate
CN102139861A (en) * 2011-05-10 2011-08-03 湖北百杰瑞新材料有限公司 Method for producing anhydrous lithium perchlorate
JP2013193940A (en) * 2012-03-22 2013-09-30 Nittetsu Mining Co Ltd Method of producing lithium carbonate
US9255011B2 (en) 2012-03-22 2016-02-09 Nittetsu Mining Co., Ltd. Method for producing lithium carbonate
CN103449481A (en) * 2012-05-29 2013-12-18 日铁矿业株式会社 Preparation method of lithium carbonate
CN103449481B (en) * 2012-05-29 2016-08-24 日铁矿业株式会社 The method preparing lithium carbonate

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