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JPH0617207B2 - Method for producing high-purity metal fluoride - Google Patents
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JPH0617207B2 - Method for producing high-purity metal fluoride - Google Patents

Method for producing high-purity metal fluoride

Info

Publication number
JPH0617207B2
JPH0617207B2 JP27523389A JP27523389A JPH0617207B2 JP H0617207 B2 JPH0617207 B2 JP H0617207B2 JP 27523389 A JP27523389 A JP 27523389A JP 27523389 A JP27523389 A JP 27523389A JP H0617207 B2 JPH0617207 B2 JP H0617207B2
Authority
JP
Japan
Prior art keywords
fluoride
metal
metal fluoride
purity
oxygen
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.)
Expired - Lifetime
Application number
JP27523389A
Other languages
Japanese (ja)
Other versions
JPH03137003A (en
Inventor
博美 川本
夏哉 西村
晃 坂上
能徳 久保田
康 喜田
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.)
Central Glass Co Ltd
Original Assignee
Central Glass Co 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 Central Glass Co Ltd filed Critical Central Glass Co Ltd
Priority to JP27523389A priority Critical patent/JPH0617207B2/en
Publication of JPH03137003A publication Critical patent/JPH03137003A/en
Publication of JPH0617207B2 publication Critical patent/JPH0617207B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Inorganic Compounds Of Heavy Metals (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、フッ化物光ファイバー等の原料として有用な
高純度金属フッ化物の製造方法に関し、特に遷移金属不
純物、酸素および炭素の極めて少ない金属フッ化物の製
造方法に関するものである。
Description: TECHNICAL FIELD The present invention relates to a method for producing a high-purity metal fluoride useful as a raw material for a fluoride optical fiber, and more particularly to a metal fluoride containing extremely few transition metal impurities, oxygen and carbon. The present invention relates to a method for producing a compound.

[従来技術] フッ化物光ファイバーの超低損失化を阻害する要因とし
て、光ファイバー中に混入している鉄、銅、ニッケル、
コバルト等の遷移金属および酸素が挙げられる。従来よ
り遷移金属不純物の少ない金属フッ化物を得るためには
一般的には溶媒抽出法やイオン交換法により精製ののち
フッ素化しているものであるが、酸素含有量を少なくす
るために金属フッ化物の脱水、焼成を窒素やアルゴン等
の不活性ガス雰囲気中、フッ化水素ガスを導入しておこ
なっているものである。これらの金属フッ化物は原料由
来あるいは精製過程において試薬、溶媒、イオン交換樹
脂等に起因する有機物が混入するが、このような不活性
雰囲気では炭素の脱離が十分に起こらず、焼成された金
属フッ化物中に炭素を含有することとなる。炭素含有の
金属フッ化物を用いてファイバー化をおこなった場合、
散乱の原因となり好ましくない。
[Prior Art] Iron, copper, nickel, which is mixed in the optical fiber, is a factor that inhibits the ultra-low loss of the fluoride optical fiber.
Transition metals such as cobalt and oxygen are mentioned. In order to obtain a metal fluoride containing less transition metal impurities than in the past, it is generally fluorinated after purification by a solvent extraction method or an ion exchange method, but in order to reduce the oxygen content, a metal fluoride is used. Is dehydrated and baked by introducing hydrogen fluoride gas in an atmosphere of an inert gas such as nitrogen or argon. These metal fluorides are mixed with organic substances derived from raw materials or reagents, solvents, ion exchange resins, etc. in the purification process, but in such an inert atmosphere, desorption of carbon does not sufficiently occur, and the calcined metal is Carbon will be contained in the fluoride. When fiber is formed using carbon-containing metal fluoride,
It is not preferable because it causes scattering.

[問題点を解決するための手段] 本発明者らはかかる現状に鑑み鋭意検討の結果、意外に
も酸素の存在する系での処理により極めて高純度の金属
フッ化物を得ることができることを見出し本発明に到達
した。すなわち本発明はアルカリ金属、アルカリ土類金
属、ランタニド金属、ジルコニウム、ハフニウム、イッ
トリウム、インジウム、アルミニウムより選ばれる少な
くとも一種類の金属のフッ化物をフッ素化剤と酸素の混
合ガスを流通させさながら300〜700℃で処理することを
特徴とする高純度金属フッ化物の製造方法である。
[Means for Solving the Problems] As a result of intensive studies in view of the present situation, the present inventors have surprisingly found that extremely high-purity metal fluoride can be obtained by treatment in a system in which oxygen is present. The present invention has been reached. That is, the present invention is an alkali metal, an alkaline earth metal, a lanthanide metal, zirconium, hafnium, yttrium, indium, a fluoride of at least one metal selected from aluminum, while flowing a mixed gas of a fluorinating agent and oxygen 300 ~ The method for producing a high-purity metal fluoride is characterized by treating at 700 ° C.

本発明の原料となる金属フッ化物の製造方法は特に限定
されないが、本発明者らが既に提案した特開昭64-45715
号の方法が好ましい。すなわち前記金属の可溶性塩水溶
液のpHを1.0〜11に保ち、原料化合物に対し重量で0.0
05%以上の量のジエチルジチオカルバミン酸塩(DDTC)、
もしくはピロリジンジチオカルバミン酸アンモニウム(A
PDC)を添加し、生成した沈殿をロ過、除去する方法であ
る。ここで原料の金属可溶性塩としては、硫酸塩、水酸
化物、炭酸塩、重炭酸塩、塩化物、硝酸塩、酸塩化物等
が用いられる。アルカリ金属としてはLi、Na、Kが、ア
ルカリ土類金属としてはCa、Ba、Mg、Beが、ランタニド
金属としてはLa、Nb、Gd、Tb、Ybが、ジエチルジチオカ
ルバミン酸塩としては、ナトリウム塩、カリウム塩、ア
ンモニウム塩等がそれぞれ用いられる。
The method for producing the metal fluoride as the raw material of the present invention is not particularly limited, but the present inventors have already proposed JP-A-64-45715.
No. method is preferred. That is, the pH of the aqueous solution of the soluble salt of the metal is maintained at 1.0 to 11, and the weight of the starting compound is 0.0
05% or more of diethyldithiocarbamate (DDTC),
Or ammonium pyrrolidine dithiocarbamate (A
PDC) is added, and the formed precipitate is filtered and removed. Here, as the metal soluble salt of the raw material, a sulfate, a hydroxide, a carbonate, a bicarbonate, a chloride, a nitrate, an acid chloride or the like is used. Al, Li, Na, K as alkaline metals, Ca, Ba, Mg, Be as alkaline earth metals, La, Nb, Gd, Tb, Yb as lanthanide metals, sodium salt as diethyldithiocarbamate. , Potassium salt, ammonium salt and the like are used respectively.

キレート剤として、DDTCまたはAPDCを添加する上記金属
の水溶液としては、可溶性の水溶液はもちろん、酸化物
等の不溶性化合物を酸によって溶解し、可溶性塩にした
のちpHを調節した溶液であっても使用することができ
る。
As a chelating agent, as an aqueous solution of the above metal to which DDTC or APDC is added, it is possible to use not only a soluble aqueous solution but also a solution in which an insoluble compound such as an oxide is dissolved with an acid to form a soluble salt and then the pH is adjusted. can do.

キレート化剤を加えるpHの範囲は1.0〜11に保ってお
くことが好ましい。この範囲をはずれると遷移金属の沈
殿は十分に生成せず、精製が不十分となる。このように
して得た高純度の溶液を用いフッ素化するものである
が、フッ素化剤としてはフッ化水素酸、フッ化水素ガ
ス、フッ化アンモニウム、酸性フッ化アンモニウム、フ
ッ素ガス、ハロゲン化フッ素、三フッ化窒素等が挙げら
れる。
The pH range for adding the chelating agent is preferably maintained at 1.0 to 11. If the amount is out of this range, the precipitation of the transition metal will not be sufficiently generated and the purification will be insufficient. The high-purity solution thus obtained is used for fluorination. Examples of the fluorinating agent include hydrofluoric acid, hydrogen fluoride gas, ammonium fluoride, ammonium acid fluoride, fluorine gas, and fluorine halides. , Nitrogen trifluoride and the like.

本発明における金属の可溶性塩は、水に不溶性のフッ化
物を生成する場合が多いが、可溶性のフッ素化剤の添加
後に液を濃縮してフッ化物を析出させる。ただし、濃縮
の途中段階でフッ素化剤を添加し、反応と濃縮を同時に
おこなうこともできる。また、一旦濃縮して可溶性塩を
析出させ分離、乾燥したのちガス状のフッ素化剤と反応
させフッ化物を製造することができる。このようにして
得た金属フッ化物は、別の精製法を付加してもよい。
The soluble salt of the metal in the present invention often forms a fluoride insoluble in water, but after the addition of the soluble fluorinating agent, the liquid is concentrated to precipitate the fluoride. However, it is also possible to add the fluorinating agent in the middle stage of the concentration and simultaneously carry out the reaction and the concentration. Further, once concentrated, a soluble salt is precipitated, separated, dried, and then reacted with a gaseous fluorinating agent to produce a fluoride. The metal fluoride thus obtained may be subjected to another purification method.

本発明においては、このようにして製造した金属フッ化
物をさらに処理して、酸素および炭素を極めて少なくす
るものであり、先ず十分に乾燥したのち、フッ素化剤と
酸素の混合ガスを流通させながら300〜700℃の範囲で焼
成する。
In the present invention, the metal fluoride produced in this manner is further processed to extremely reduce oxygen and carbon. First, after sufficiently drying, while flowing a mixed gas of a fluorinating agent and oxygen. Bake in the range of 300-700 ℃.

フッ素化剤としては、フッ化水素、フッ素、三フッ化窒
素、ハロゲン化フッ素ガス等が挙げられ、このうち取扱
いやすさ、材質面等からフッ化水素が最も好ましい。こ
のフッ素化剤の濃度はガス中濃度として1〜50%の範囲
が好ましく、この範囲未満では酸素を十分に除去するこ
とができない。またこの範囲を越えると炭素を十分に飛
散させることができない。酸素の濃度は1〜50%の範囲
が好ましく、この範囲未満では炭素を十分に飛散させる
ことができず、またこの範囲を越えると酸素含有量が増
大する。焼成温度は300〜700℃の範囲が好ましく、この
範囲未満では脱酸素が十分におこなわれず、この範囲を
越えると酸素含有量が大となる。
Examples of the fluorinating agent include hydrogen fluoride, fluorine, nitrogen trifluoride, halogenated fluorine gas and the like, and among these, hydrogen fluoride is most preferable from the viewpoint of easy handling and material. The concentration of the fluorinating agent is preferably in the range of 1 to 50% as the concentration in gas, and if it is less than this range, oxygen cannot be sufficiently removed. Moreover, if it exceeds this range, carbon cannot be sufficiently scattered. The concentration of oxygen is preferably in the range of 1 to 50%, and if it is less than this range, carbon cannot be sufficiently scattered, and if it exceeds this range, the oxygen content increases. The firing temperature is preferably in the range of 300 to 700 ° C. If it is less than this range, deoxidation is not sufficiently performed, and if it exceeds this range, the oxygen content becomes large.

以下本発明を実施例により具体的に説明する。The present invention will be specifically described below with reference to examples.

実施例1 市販試薬塩化アルミニウム六水塩100gを2ビーカー
に入れ、超純水を1加えて溶解しpHを調整したのち
ピロリジンジチオカルバミン酸アンモニウムを0.5g加
え、液を分液ロートに移しクロロホルムにて抽出した。
この精製液にフッ化水素酸を加え、加熱濃縮してフッ化
アルミニウム三水塩の結晶を得た。結晶をロ過後四フッ
化エチレン樹脂製の乾燥炉で乾燥し、乾燥物を白金皿に
入れ白金製の炉心管を用いて高純度エアーとフッ化水素
ガスを各0.5/min流通させながら600℃で2時間焼成
し、高純度のフッ化アルミニウムを得た。この分析結果
を第1表に示した。
Example 1 Commercially available reagent 100 g of aluminum chloride hexahydrate was placed in a 2 beaker, 1 of ultrapure water was added to dissolve and adjust pH, 0.5 g of ammonium pyrrolidinedithiocarbamate was added, and the solution was transferred to a separating funnel and chloroform was added. Extracted.
Hydrofluoric acid was added to this purified solution, and the mixture was heated and concentrated to obtain aluminum fluoride trihydrate crystals. The crystals are filtered and dried in a tetrafluoroethylene resin drying oven, and the dried product is placed in a platinum dish and a platinum furnace tube is used to flow high-purity air and hydrogen fluoride gas at 0.5 / min each at 600 ° C. And baked for 2 hours to obtain high-purity aluminum fluoride. The results of this analysis are shown in Table 1.

実施例2 市販試薬酸塩化ジルコニウム500gを5ビーカーに入
れ、超純水を加え、溶解して全量を5とした。この溶
液をメンブレンフィルター(孔径0.2μm)でロ過し、
不溶性の不純物を除去した。次いで、内径26mm、長さ50
0mmのカラムに陽イオン交換樹脂を高さ300mmまで充填
し、ロ過液を11ml/cm/minで通液した。イオン交換精製
された液にアンモニア水を加え水酸化物とし、ロ過した
のちフッ化水素酸を加えて加熱濃縮後、フッ化ジルコニ
ウムの三水塩結晶を得た。この結晶を白金皿に入れ白金
性の炉心管を用い高純度エアー1/min、フッ酸ガス
0.5/minで流通させながら500℃で2時間焼成し、高
純度のフッ化ジルコニウムを得た。この分析結果を第1
表に示した。
Example 2 500 g of a commercially available reagent zirconium oxychloride was placed in a 5 beaker, and ultrapure water was added to dissolve it to make a total amount of 5. Filter this solution through a membrane filter (pore size 0.2 μm),
Insoluble impurities were removed. Next, inner diameter 26 mm, length 50
A 0 mm column was packed with a cation exchange resin to a height of 300 mm, and the filtration liquid was passed at 11 ml / cm / min. Aqueous ammonia was added to the ion-exchange purified liquid to form a hydroxide, which was filtered and then hydrofluoric acid was added to the solution and the mixture was heated and concentrated to obtain trihydrate crystals of zirconium fluoride. Place this crystal in a platinum dish and use a platinum core tube to obtain high-purity air 1 / min and hydrofluoric acid gas.
Firing was performed at 500 ° C. for 2 hours while flowing at 0.5 / min to obtain high-purity zirconium fluoride. This analysis result is the first
Shown in the table.

比較例1〜4 フッ酸ガスを焼成時に流通させない以外は実施例1と同
様にした(比較例1)。高純度エアーを焼成時に流通さ
せない以外は実施例1と同様にした(比較例2)。フッ
酸ガスを焼成時に流通させない以外は実施例2と同様に
した(比較例3)。高純度エアーを焼成時に流通させな
い以外は実施例2と同様にした(比較例4)。これらの
分析結果を第1表に示した。
Comparative Examples 1 to 4 The same procedure as in Example 1 was carried out except that the hydrofluoric acid gas was not passed during firing (Comparative Example 1). The same procedure was performed as in Example 1 except that high-purity air was not passed during firing (Comparative Example 2). The same procedure was performed as in Example 2 except that the hydrofluoric acid gas was not passed during firing (Comparative Example 3). The same procedure was performed as in Example 2 except that high-purity air was not passed during firing (Comparative Example 4). The results of these analyzes are shown in Table 1.

[発明の効果] 本発明の方法によれば、光ファイバー等の原料となる高
純度金属フッ化物を効率よく得ることができ、特に酸
素、炭素の極めて少ない金属フッ化物を得ることができ
るものである。
[Effects of the Invention] According to the method of the present invention, it is possible to efficiently obtain a high-purity metal fluoride as a raw material for an optical fiber or the like, and particularly to obtain a metal fluoride containing very little oxygen and carbon. .

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】アルカリ金属、アルカリ土類金属、ランタ
ニド金属、ジルコニウム、ハフニウム、イットリウム、
インジウム、アルミニウムより選ばれる少なくとも一種
類の金属のフッ化物をフッ素化剤と酸素の混合ガスを流
通させさながら300〜700℃で処理することを特徴とする
高純度金属フッ化物の製造方法。
1. An alkali metal, an alkaline earth metal, a lanthanide metal, zirconium, hafnium, yttrium,
A method for producing a high-purity metal fluoride, which comprises treating a fluoride of at least one metal selected from indium and aluminum at 300 to 700 ° C. while circulating a mixed gas of a fluorinating agent and oxygen.
JP27523389A 1989-10-23 1989-10-23 Method for producing high-purity metal fluoride Expired - Lifetime JPH0617207B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27523389A JPH0617207B2 (en) 1989-10-23 1989-10-23 Method for producing high-purity metal fluoride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27523389A JPH0617207B2 (en) 1989-10-23 1989-10-23 Method for producing high-purity metal fluoride

Publications (2)

Publication Number Publication Date
JPH03137003A JPH03137003A (en) 1991-06-11
JPH0617207B2 true JPH0617207B2 (en) 1994-03-09

Family

ID=17552555

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27523389A Expired - Lifetime JPH0617207B2 (en) 1989-10-23 1989-10-23 Method for producing high-purity metal fluoride

Country Status (1)

Country Link
JP (1) JPH0617207B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4676622B2 (en) * 2001-02-08 2011-04-27 ステラケミファ株式会社 Method for reducing oxygen and carbon components in fluoride
WO2005005316A1 (en) * 2003-07-11 2005-01-20 Honeywell Specialty Chemicals Seelze Gmbh Process for the manufacture of high purity metal fluorides
JP4724859B2 (en) * 2005-09-09 2011-07-13 独立行政法人 日本原子力研究開発機構 Method for converting metal nitride to halide
CN120641499A (en) * 2023-02-14 2025-09-12 斯泰拉化工公司 Inorganic filler for low dielectric loss resin composition, slurry composition for low dielectric loss resin composition, low dielectric loss resin composition, molded article for high-frequency device, and high-frequency device

Also Published As

Publication number Publication date
JPH03137003A (en) 1991-06-11

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