JP3137226B2 - Production method of high purity strontium chloride - Google Patents
Production method of high purity strontium chlorideInfo
- Publication number
- JP3137226B2 JP3137226B2 JP07063826A JP6382695A JP3137226B2 JP 3137226 B2 JP3137226 B2 JP 3137226B2 JP 07063826 A JP07063826 A JP 07063826A JP 6382695 A JP6382695 A JP 6382695A JP 3137226 B2 JP3137226 B2 JP 3137226B2
- Authority
- JP
- Japan
- Prior art keywords
- strontium chloride
- strontium
- hydrochloric acid
- purity
- high purity
- 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 - Fee Related
Links
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、高純度塩化ストロンチ
ウムの製造法に関し、不純物を除いた極めて高純度の塩
化ストロンチウムの製造法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing high-purity strontium chloride, and more particularly to a method for producing extremely high-purity strontium chloride excluding impurities.
【0002】[0002]
【従来技術】塩化ストロンチウムは、半導体、蛍光体、
光学レンズ等の中間原料として従来から用いられてい
る。これらの分野において使用される塩化ストロンチウ
ムは、高純度が要求される。また、近年、特に256M
バイト以上の半導体のメモリーセルのキャパシタとし
て、高誘電体チタン酸ストロンチウムが注目を集めてお
り、この原料に使用される場合、特に高純度が要求され
る。2. Description of the Related Art Strontium chloride is used in semiconductors, phosphors,
It has been conventionally used as an intermediate material for optical lenses and the like. Strontium chloride used in these fields requires high purity. In recent years, in particular, 256M
High-dielectric strontium titanate has attracted attention as a capacitor for memory cells of more than one byte, and when used as a raw material, particularly high purity is required.
【0003】半導体の場合、デバイスの信頼性に重大な
影響を及ぼすFe,Ni,Cu等の遷移金属はもちろん
のこと、Na,K等のアルカリ金属も100ppb以下
の含有量が要求され、これらの原料の不純物は極限まで
除去する必要がある。In the case of semiconductors, not only transition metals such as Fe, Ni, and Cu, which have a significant effect on device reliability, but also alkali metals such as Na and K are required to have a content of 100 ppb or less. It is necessary to remove the impurities of the raw material to the utmost.
【0004】従来、塩化ストロンチウムの精製法は、水
酸化ストロンチウム或いは炭酸ストロンチウムを塩酸に
溶解させ濃縮し結晶させるか、または炭酸ストロンチウ
ムと塩化カルシウムとを溶融し融塊を水で抽出させ濃縮
して得られる。さらに精製を必要とする場合、種々の沈
殿剤、例えば重金属は硫化水素、鉄は臭素を加えて沈殿
を除いた後、濃縮晶析及び冷却晶析を繰り返すことによ
り精製しているが、純度的に未だ十分とは言えないし、
また、工程が煩雑となりコストが高くなるなどの問題が
ある。Conventionally, strontium chloride has been purified by dissolving strontium hydroxide or strontium carbonate in hydrochloric acid and concentrating it for crystallization, or by melting strontium carbonate and calcium chloride and extracting and condensing a molten mass with water. Can be When further purification is required, various precipitants, for example, heavy metal is purified by adding hydrogen sulfide and iron to remove bromine by adding bromine, and then repeating concentration crystallization and cooling crystallization. Is still not enough
Further, there is a problem that the process becomes complicated and the cost increases.
【0005】一方、チタン酸ストロンチウムの製造法と
しては、炭酸ストロンチウムと酸化チタンとを混合し、
1100℃以上の温度で焼成した後、機械的に粉砕する
固相法により行われている。固相法では、原料中の不純
物がそのまま製品に残るため、高純度原料を使用する必
要があり、またこのようにして製造したチタン酸ストロ
ンチウムは、不純物の混入は避けられず、高純度チタン
酸ストロンチウムを得ることは難しい。この問題を解決
するため、水溶性ストロンチウム塩と水溶性チタン塩に
沈殿剤を加えて生成した沈殿を固液分離、洗浄後乾燥さ
せ、次いで焼成することによりチタン酸ストロンチウム
を製造する液相法、或いはシュウ酸溶液と水溶性ストロ
ンチウム塩及び水溶性チタン塩の混合液の反応により得
られた結晶を焼成することによりチタン酸ストロンチウ
ムを製造する方法がとられている。しかし、これらの方
法においても、原料からの不純物の混入は避けられない
ため、必ずしも十分なものではない。従って、原料の高
純度化は、必要不可欠であり、ここに上記チタン酸スト
ロンチウム等を製造するための原料として、重要な高純
度塩化ストロンチウムの製造法を提供するものである。On the other hand, as a method for producing strontium titanate, strontium carbonate and titanium oxide are mixed,
After firing at a temperature of 1100 ° C. or higher, a solid phase method of mechanically pulverizing is used. In the solid-phase method, since impurities in the raw materials remain in the product as they are, it is necessary to use high-purity raw materials.In addition, strontium titanate produced in this way cannot avoid the contamination of impurities, and high purity titanic acid cannot be avoided. It is difficult to get strontium. In order to solve this problem, a liquid phase method for producing strontium titanate by solid-liquid separation of a precipitate formed by adding a precipitant to a water-soluble strontium salt and a water-soluble titanium salt, washing and drying, and then firing, Alternatively, a method of producing strontium titanate by firing a crystal obtained by reacting a mixed solution of an oxalic acid solution with a water-soluble strontium salt and a water-soluble titanium salt has been adopted. However, even in these methods, contamination of impurities from the raw material is inevitable, so that it is not always sufficient. Therefore, high purity of the raw material is indispensable, and here, an important method for producing high purity strontium chloride is provided as a raw material for producing the strontium titanate and the like.
【0006】[0006]
【問題点を解決するための具体的手段】本発明者らは、
前記問題点を解決するための手段を鋭意検討した結果、
塩化ストロンチウム溶液を塩酸による再結晶法で塩化ス
トロンチウムの結晶を析出するにあたり、スラリー中の
塩酸濃度を10〜25%の範囲で析出させ、更に結晶の
1〜5重量倍の高純度液で洗浄することにより、遷移金
属のFe、Ni、Cuは、各0.02ppm以下、アル
カリ金属のNa、Kは、各0.05ppm以下、アルカ
リ土類金属のBa、Caは、各10ppm以下と極めて
高純度の塩化ストロンチウム結晶が得られることを見い
出し本発明に到達した。[Specific means for solving the problem]
As a result of earnestly studying means for solving the above problems,
When the strontium chloride solution is used to precipitate strontium chloride crystals by a recrystallization method using hydrochloric acid, the concentration of hydrochloric acid in the slurry is precipitated in the range of 10 to 25%, and the slurry is further washed with a high-purity liquid 1 to 5 times the weight of the crystals. Thereby, the transition metals Fe, Ni, and Cu are 0.02 ppm or less, the alkali metals Na and K are 0.05 ppm or less, and the alkaline earth metals Ba and Ca are 10 ppm or less. The present inventors have found that strontium chloride crystals of the formula (1) can be obtained, and have reached the present invention.
【0007】以下、この方法について説明する。ストロ
ンチウム塩としては、塩化ストロンチウムを用いるが、
中間原料の炭酸ストロンチウムや水酸化ストロンチウム
を塩酸に溶解して用いてもよく、最終的に塩化ストロン
チウムの形であればよい。Hereinafter, this method will be described. As the strontium salt, strontium chloride is used,
Strontium carbonate or strontium hydroxide as an intermediate raw material may be used by dissolving it in hydrochloric acid, and may be in the form of strontium chloride finally.
【0008】得られた塩化ストロンチウム溶液と塩酸溶
液を混合すると、共通イオン効果で塩化ストロンチウム
の結晶が析出してくる。この時、析出スラリーの塩酸濃
度が高いほど塩化ストロンチウム結晶の収率は高くなる
が、原料塩化ストロンチウムに含まれるアルカリ土類金
属のBaが、析出した結晶に含まれ、原料塩化ストロン
チウムよりも高くなる。しかし、このBaもある一定の
塩酸濃度以下にすれば低下することが判明した。即ち、
精製を終了した時点の析出スラリーの塩酸濃度を10〜
25%の範囲で結晶を取り出すことによりBaを除くこ
とが出来る。When the obtained strontium chloride solution and hydrochloric acid solution are mixed, strontium chloride crystals are precipitated by the common ion effect. At this time, the higher the hydrochloric acid concentration of the precipitated slurry, the higher the yield of strontium chloride crystals, but the alkaline earth metal Ba contained in the raw strontium chloride is included in the precipitated crystals and becomes higher than the raw strontium chloride. . However, it has been found that this Ba also decreases when the concentration of hydrochloric acid is reduced to a certain level or less. That is,
When the concentration of hydrochloric acid in the precipitation slurry at the end of the purification is 10 to
Ba can be removed by extracting crystals in the range of 25%.
【0009】一方、得られた塩化ストロンチウム結晶そ
のままでは精製度が十分とは言えず、この結晶を高純度
液で結晶重量の1〜5重量倍の量で洗浄することにより
高純度塩化ストロンチウムが得られる。On the other hand, the purity of the obtained strontium chloride crystal cannot be said to be sufficient as it is, and the high purity strontium chloride can be obtained by washing the crystal with a high purity liquid in an amount of 1 to 5 times the weight of the crystal. Can be
【0010】高純度液としては、純水、塩酸、精製塩化
ストロンチウム飽和溶液、アルコール類等が用いられる
が、収率、価格、純度の面から適宜洗浄水の種類を選択
すればよい。また、洗浄水量は、得られた塩化ストロン
チウム結晶の1〜5重量倍の量で洗浄する必要がある。
洗浄水量が少ないと十分に精製された塩化ストロンチウ
ムは得られない。一方、洗浄水量をこれ以上多くしても
精製度は上がらず、また収率の低下及び洗浄水の使用に
よる価格上昇が生じ、経済的でない。As the high purity liquid, pure water, hydrochloric acid, purified strontium chloride saturated solution, alcohols and the like are used. The type of washing water may be appropriately selected from the viewpoint of yield, price and purity. Further, it is necessary to wash the washing water in an amount of 1 to 5 times by weight of the obtained strontium chloride crystal.
If the amount of washing water is small, sufficiently purified strontium chloride cannot be obtained. On the other hand, if the amount of washing water is further increased, the degree of purification will not be improved, and the yield will decrease and the price will increase due to the use of washing water, which is not economical.
【0011】析出及び固液分離時の温度については、特
に限定しないが溶解度の低い低温度の方が収率もよくな
るためなるべく低温度の方が好ましい。精製方法として
は、塩酸にストロンチウム塩を添加する方法、逆にスト
ロンチウム塩に塩酸を添加する方法、塩酸とストロンチ
ウム塩を同時に添加する方法等のいずれの方法でも高純
度塩化ストロンチウム結晶が得られ限定されるものでは
ない。The temperature at the time of precipitation and solid-liquid separation is not particularly limited, but the lower the temperature, the lower the solubility is. As a purification method, a method of adding strontium salt to hydrochloric acid, a method of adding hydrochloric acid to strontium salt, a method of simultaneously adding hydrochloric acid and strontium salt, and the like, can provide high-purity strontium chloride crystals and are limited. Not something.
【0012】[0012]
【実施例】以下、実施例により本発明を具体的に説明す
る。 実施例1〜4、比較例1,2 300Lテフロン槽に工業用35%塩酸溶液150Kg
を仕込んだ後、撹拌しながら、表1に示した塩酸濃度に
なるよう所定量の30%塩化ストロンチウム溶液を添加
した。次に、このスラリーを25℃に冷却した後、樹脂
製の濾過器で固液分離を行い、得られた結晶と等重量の
エタノールで結晶を洗浄した。この結晶の分析を行い、
その結果を表1に示した。尚、分析値は、100%塩化
ストロンチウムに換算した値である。The present invention will be described below in detail with reference to examples. Examples 1-4, Comparative Examples 1 and 2 150 kg of industrial 35% hydrochloric acid solution in a 300 L Teflon tank
After charging, a predetermined amount of a 30% strontium chloride solution was added while stirring to obtain the hydrochloric acid concentration shown in Table 1. Next, after cooling the slurry to 25 ° C., solid-liquid separation was performed using a resin filter, and the crystals were washed with ethanol having the same weight as the obtained crystals. Analysis of this crystal,
The results are shown in Table 1. The analytical values are values converted to 100% strontium chloride.
【0013】[0013]
【表1】 [Table 1]
【0014】実施例5〜7、比較例3,4 300Lテフロン槽に工業用35%塩酸溶液150Kg
を仕込んだ後、撹拌しながら30%塩化ストロンチウム
溶液90Kgを添加した。次に、このスラリーを25℃
に冷却した後、樹脂製の濾過器で固液分離を行い、得ら
れた結晶の洗浄試験をエタノールを用いて行った。この
結晶の分析を行い、その結果を表2に示した。尚、分析
値は、100%塩化ストロンチウムに換算した値であ
る。Examples 5-7, Comparative Examples 3, 4 150 kg of a 35% hydrochloric acid solution for industrial use in a 300 L Teflon tank
After the addition, 90 kg of a 30% strontium chloride solution was added with stirring. Next, the slurry was cooled to 25 ° C.
After cooling, a solid-liquid separation was performed with a resin filter, and a washing test of the obtained crystals was performed using ethanol. The crystals were analyzed, and the results are shown in Table 2. The analytical values are values converted to 100% strontium chloride.
【0015】[0015]
【表2】 [Table 2]
【0016】実施例8〜10、比較例5,6 300Lテフロン槽に30%塩化ストロンチウム溶液1
50Kgを仕込んだ後、攪拌しながら工業用35%塩酸
溶液150Kgを添加した。次に、このスラリーを25
℃に冷却した後、樹脂製の濾過器で固液分離を行い、得
られた結晶の洗浄試験を試薬特級35%塩酸溶液を用い
て行った。この結晶の分析を行い、その結果を表3に示
した。尚、分析値は、100%塩化ストロンチウムに換
算した値である。Examples 8 to 10 and Comparative Examples 5 and 6 30% strontium chloride solution 1 in a 300 L Teflon tank
After charging 50 kg, 150 kg of an industrial 35% hydrochloric acid solution was added with stirring. Next, this slurry was added to 25
After cooling to ° C., solid-liquid separation was performed using a resin filter, and a washing test of the obtained crystals was performed using a special grade 35% hydrochloric acid solution of a reagent. The crystals were analyzed, and the results are shown in Table 3. The analytical values are values converted to 100% strontium chloride.
【0017】[0017]
【表3】 [Table 3]
【0018】実施例11 300Lテフロン槽に純水40Kgと炭酸ストロンチウ
ム40Kgを仕込んだ後、攪拌しながら工業用35%塩
酸225Kgを添加した。次に、このスラリーを25℃
に冷却した後、樹脂製の濾過器で固液分離を行い、得ら
れた結晶を実施例9で得られた塩化ストロンチウムの飽
和溶液を結晶の1.5重量倍で洗浄した。この結晶の分
析を行った結果、Fe、Ni、Cuは、各0.02pp
m以下、Na、Kは、各0.05ppm以下、Ba、C
aは、それぞれ7ppmと6ppmであった。尚、分析
値は、100%塩化ストロンチウムに換算した値であ
る。Example 11 After charging 40 kg of pure water and 40 kg of strontium carbonate into a 300 L Teflon tank, 225 kg of industrial 35% hydrochloric acid was added with stirring. Next, the slurry was cooled to 25 ° C.
After that, solid-liquid separation was carried out using a resin filter, and the obtained crystals were washed with a saturated solution of strontium chloride obtained in Example 9 at 1.5 times the weight of the crystals. As a result of analyzing this crystal, Fe, Ni, and Cu were found to be 0.02 pp each.
m, Na and K are each 0.05 ppm or less, Ba, C
a was 7 ppm and 6 ppm, respectively. The analytical values are values converted to 100% strontium chloride.
【0019】[0019]
【発明の効果】本発明の方法により、半導体分野等にお
いて要求される不純物の極めて少ない高純度塩化ストロ
ンチウムを得ることが可能となった。According to the method of the present invention, it has become possible to obtain high-purity strontium chloride having extremely few impurities required in the field of semiconductors and the like.
フロントページの続き (56)参考文献 特開 昭61−270215(JP,A) 特開 平6−343978(JP,A) 特開 平2−233520(JP,A) 特公 昭46−23491(JP,B1) (58)調査した分野(Int.Cl.7,DB名) C01F 11/32 CA(STN)Continuation of front page (56) References JP-A-61-270215 (JP, A) JP-A-6-343978 (JP, A) JP-A-2-233520 (JP, A) JP-B-46-23491 (JP, A) , B1) (58) Field surveyed (Int. Cl. 7 , DB name) C01F 11/32 CA (STN)
Claims (2)
あたり、晶出スラリーの塩酸濃度を10〜25%の範囲
で晶出させることを特徴とする高純度塩化ストロンチウ
ムの製造法。1. A method for producing high-purity strontium chloride, comprising purifying strontium chloride with hydrochloric acid by crystallizing the crystallization slurry at a hydrochloric acid concentration of 10 to 25%.
ロンチウム結晶を少なくとも析出量の1〜5重量倍の高
純度液で洗浄することを特徴とする高純度塩化ストロン
チウムの製造法。2. A method for producing high-purity strontium chloride, comprising washing the strontium chloride crystal obtained by the method according to claim 1 with a high-purity liquid at least 1 to 5 times the weight of the deposited amount.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP07063826A JP3137226B2 (en) | 1995-03-23 | 1995-03-23 | Production method of high purity strontium chloride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP07063826A JP3137226B2 (en) | 1995-03-23 | 1995-03-23 | Production method of high purity strontium chloride |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08259228A JPH08259228A (en) | 1996-10-08 |
JP3137226B2 true JP3137226B2 (en) | 2001-02-19 |
Family
ID=13240562
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JP07063826A Expired - Fee Related JP3137226B2 (en) | 1995-03-23 | 1995-03-23 | Production method of high purity strontium chloride |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102092759B (en) * | 2009-12-09 | 2013-01-16 | 贵州红星发展股份有限公司 | Method for preparing strontium dichloride hexahydrate |
CN106745150B (en) * | 2017-03-06 | 2018-12-25 | 中国科学院青海盐湖研究所 | The preparation method of toothpaste strontium chloride |
CN109157981B (en) * | 2018-09-17 | 2020-03-17 | 中国核动力研究设计院 | Method and device for removing aluminum in radioactive strontium chloride solution |
-
1995
- 1995-03-23 JP JP07063826A patent/JP3137226B2/en not_active Expired - Fee Related
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Publication number | Publication date |
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JPH08259228A (en) | 1996-10-08 |
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