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JPH03208815A - Production of fluoride - Google Patents

Production of fluoride

Info

Publication number
JPH03208815A
JPH03208815A JP121690A JP121690A JPH03208815A JP H03208815 A JPH03208815 A JP H03208815A JP 121690 A JP121690 A JP 121690A JP 121690 A JP121690 A JP 121690A JP H03208815 A JPH03208815 A JP H03208815A
Authority
JP
Japan
Prior art keywords
fluoride
chloride
magnesium
ionization tendency
calcium
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
JP121690A
Other languages
Japanese (ja)
Inventor
Tadashi Ogasawara
忠司 小笠原
Yoshitake Natsume
義丈 夏目
Kenji Fujita
健治 藤田
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.)
Osaka Titanium Co Ltd
Original Assignee
Osaka Titanium 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 Osaka Titanium Co Ltd filed Critical Osaka Titanium Co Ltd
Priority to JP121690A priority Critical patent/JPH03208815A/en
Publication of JPH03208815A publication Critical patent/JPH03208815A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F5/00Compounds of magnesium
    • C01F5/26Magnesium halides
    • C01F5/28Fluorides

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PURPOSE:To obtain the fluoride of an element having a low ionization tendency without any difficulty in filtering the product and any problem relating to the environment by allowing the chloride of an element having a low ionization tendency to react with the fluoride of an element having a higher ionization tendency than the former element in their molten state. CONSTITUTION:The chloride of an element having a low ionization tendency is allowed to react with the fluoride of an element having a higher ionization tendency than the former element in their molten state to obtain the fluoride of the element having a lower ionization tendency. In this method, when the chloride of an element having a lower ionization tendency and the chloride of an element having a higher ionization tendency are mixed, the melting rate is increased when the fluoride of the element having a higher ionization tendency is subjected to a reaction, and the reaction proceeds rapidly. Magnesium chloride is allowed to react with calcium fluoride by this method to obtain magnesium fluoride.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はぶつ化物、特にぶつ化マグネシウムの製造方法
に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a process for producing a carbide, particularly magnesium carbide.

(従来の技術) ぶつ化アルミニウム(Aj!Fs)、フルオロアルミン
酸ソーダ(Nas^IF、)、ふう化ナトリウム(Na
F)、ふう化マグネシウム(MgFt)など、種々のふ
つ化物が工業的に利用されている。
(Prior art) Aluminum fluoride (Aj!Fs), sodium fluoroaluminate (Nas^IF, ), sodium fluoride (Na
F), various fluorides such as magnesium fluoride (MgFt) are used industrially.

このようなぶつ化物の中で、ぶつ化マグネシウムはレン
ズのコーテイング材あるいはレーザー赤外線機器の窓材
等に使用されており、その製造方法としては、従来いろ
いろな方法が用いられ、あるいは提案されている0例え
ば、■塩化マグネシウムとふう化水素酸とを反応させる
方法、■ふう化アンモニウムと炭酸マグネシウムを反応
させる方法、などである。
Among these agglomerates, magnesium agglomerate is used as a coating material for lenses or as a window material for laser infrared equipment, and various methods have been used or proposed to produce it. 0 Examples include (1) a method of reacting magnesium chloride with hydrofluoric acid, (2) a method of reacting ammonium fluoride with magnesium carbonate, and the like.

このうち、■の方法は塩化マグネシウム水溶液にふつ化
水素酸水溶液を加え、下記(1)の反応MgCj!i+
2HF−4NgF□+2)ICj!・・(1)によりふ
う化マグネシウムを得る方法であるが、得られるぶつ化
マグネシウムは微細なコロイド状となり濾過しにくいた
め生産性が悪い、また、ぶつ化水素酸を取扱うので、設
備対策など環境面における十分な配慮が必要である。
Among these methods, method (2) adds a hydrofluoric acid aqueous solution to a magnesium chloride aqueous solution, and the following reaction (1) MgCj! i+
2HF-4NgF□+2)ICj! ...This is a method for obtaining magnesium fluoride using (1), but the resulting magnesium fluoride becomes a fine colloid and is difficult to filter, resulting in poor productivity.Also, since hydrofluoric acid is handled, there are environmental issues such as equipment measures. Sufficient consideration must be given to these aspects.

また、■のふう化アンモニウムと炭酸マグネシウムを反
応させる方法は、反応の進行が前記(1)の反応よりも
穏やかな 2 NHJ + MgCO5→MgFz+(NHa)□
CO,・・(2)の反応によりふう化マグネシウムを得
る方法であるが、原料、すなわち、ぶつ化アンモニウム
および炭酸マグネシウムの価格が高く、コスト面で問題
がある。
In addition, in the method (2) of reacting ammonium fluoride and magnesium carbonate, the reaction progresses more slowly than the reaction (1) above.2NHJ + MgCO5→MgFz+(NHa)
This is a method for obtaining magnesium fluoride by the reaction of CO,...(2), but the raw materials, ie, ammonium fluoride and magnesium carbonate, are expensive, and there is a problem in terms of cost.

(発明が解決しようとする課題) 本発明は、上記のような生成物の濾過操作の困難性や環
境面における対策など工程上の問題がなく、しかも安価
なぶつ化マグネシウムの製造方法を徒供することを目的
とする。
(Problems to be Solved by the Invention) The present invention provides an inexpensive method for producing magnesium carbide that is free from process problems such as the difficulty of filtering the product and environmental measures as described above. The purpose is to

(課題を解決するための手段) 本発明の要旨は、 [溶融状態で、イオン化傾向の小さい元素の塩化物にこ
の元素より大きいイオン化傾向を示す元素のふっ化物を
反応させ、イオン化傾向の小さい元素のふう化物を得る
ことを特徴とするふつ化物の製造方法」にある。
(Means for Solving the Problems) The gist of the present invention is as follows: [In a molten state, a chloride of an element with a small ionization tendency is reacted with a fluoride of an element that has a larger ionization tendency than this element, A method for producing a fluoride characterized by obtaining a fluoride.

金属をイオン化傾向の大きい順に並べると、Li1に、
 Ba、 Ca、 Na、 Mg5Affi、ZnSF
e、 Ni、 −・となっており、イオン化傾向の大き
い元素、小さい元素は、これらの中から必要に応じて選
べばよい。
When metals are arranged in descending order of ionization tendency, in Li1,
Ba, Ca, Na, Mg5Affi, ZnSF
e, Ni, -. Elements with a large ionization tendency and elements with a small ionization tendency may be selected from these as necessary.

従って、例えばイオン化傾向の小さい元素の塩化物とし
て塩化マグネシウムを、この元素(Mg)より大きいイ
オン化傾向を示す元素のふつ化物としてぶつ化カルシウ
ムを、それぞれ原料として用い、溶融状態の塩化マグネ
シウムにふつ化カルシウムを反応させることによりぶつ
化マグネシウムを製造することができる。
Therefore, for example, magnesium chloride is used as a chloride of an element with a small ionization tendency, and calcium fluoride is used as a fluoride of an element with a larger ionization tendency than this element (Mg). Magnesium carbide can be produced by reacting calcium.

前記のイオン化傾向の小さい元素の塩化物にこの元素よ
り大きいイオン化傾向を示す元素の塩化物を混合してお
くと、この大きいイオン化傾向を示す元素のふつ化物を
反応させる際、融解速度が速く、反応がすみやかに進行
する。
By mixing the chloride of an element with a smaller ionization tendency with the chloride of an element with a larger ionization tendency, the melting rate will be faster when reacting with the fluoride of the element with a larger ionization tendency. The reaction proceeds quickly.

(作用) 本発明方法の具体的な例として、ぶつ化マグネシウムの
製造について説明する。
(Function) As a specific example of the method of the present invention, production of magnesium butoxide will be explained.

第1図は上記本発明方法に基づくぶつ化マグネシウムの
製造工程の一例を示す概略工程(A工程)回である。
FIG. 1 is a schematic process (Step A) showing an example of the manufacturing process of magnesium butoxide based on the method of the present invention.

同図に示す工程においては、まず、塩化マグネシウムを
融解する0次に、ふう化カルシウムを溶融状態の塩化マ
グネシウム中に投入する。ふり化カルシウムは融解し、
塩化マグネシウムと下記(3)式のように反応してふり
化マグネシウムと塩化カルシウムを生成する。
In the process shown in the figure, first, magnesium chloride is melted, and then calcium fluoride is poured into the molten magnesium chloride. Calcium fluoride melts,
It reacts with magnesium chloride as shown in equation (3) below to produce magnesium fluoride and calcium chloride.

MgCj! t+CaFi →MgF1+CaCj! 
z  ・・(3)次いで、前記(3)式の反応により生
成したふう化マグネシウムと塩化カルシウムの混合塩を
冷却固化し、得られた固体塩に水を加える。塩化カルシ
ウムは水に対する溶解度が大きいので溶解し、溶解度の
小さいぶつ化マグネシウムは溶解せず、水に懸濁した状
態で残る。この懸濁液を濾過することによりふり化マグ
ネシウムを得ることができる。
MgCj! t+CaFi →MgF1+CaCj!
z...(3) Next, the mixed salt of magnesium fluoride and calcium chloride produced by the reaction of formula (3) above is cooled and solidified, and water is added to the obtained solid salt. Calcium chloride has a high solubility in water, so it dissolves, while magnesium chloride, which has a low solubility, does not dissolve and remains suspended in water. Magnesium fluoride can be obtained by filtering this suspension.

このようにして得られたぶつ化マグネシウム中に、空気
中の酸素と反応して生じた酸化マグネ;。
Magnesium oxide produced by reaction with oxygen in the air in the magnesium carbide thus obtained.

ラム(MgO)や酸化カルシウム(Cab)が不純物と
して混在している場合は、これらの不純物を酸により溶
解、除去する。用いる酸は、塩酸でもよいが、ふう化マ
グネシウムを溶解しない酢酸が好適である。
If rum (MgO) and calcium oxide (Cab) are mixed as impurities, these impurities are dissolved and removed with acid. The acid used may be hydrochloric acid, but acetic acid, which does not dissolve magnesium fluoride, is preferred.

最後に、付着している酸を水で洗浄し、乾燥してぶつ化
マグネシウムを得ることができる。
Finally, the adhering acid is washed with water and dried to obtain magnesium carbide.

上記の製造工程において、塩化マグネシウムを融解する
際、破線で示したように塩化カルシウムを混合、融解し
、混合溶融塩としておくと、この溶融塩にふつ化カルシ
ウムを加えたときの融解速度が塩化マグネシウムのみの
場合よりも大きく、塩化マグネシウムとふう化カルシウ
ムとの反応がすみやかに進行する。
In the above manufacturing process, when melting magnesium chloride, if calcium chloride is mixed and melted to form a mixed molten salt as shown by the broken line, the melting rate when calcium fluoride is added to this molten salt will be The reaction between magnesium chloride and calcium fluoride proceeds more rapidly than when using only magnesium.

また、ぶつ化マグネシウムは(3)式の反応により生成
するので、塩化マグネシウムとふう化カルシウムを等モ
ル反応させればよいのであるが、ぶつ化カルシウムが未
反応のまま残ると、前記の「冷却」工程で固化したぶつ
化マグネシウムと塩化カルシウムの混合塩中に残留し、
次の水による「溶解」工程で溶解せずぶつ化マグネシウ
ム中に不純物として残ることになる。従って、ぶつ化カ
ルシウムが残らないように塩化マグネシウムの投入量を
(3)式から算出される理論量よりも多くし、塩化マグ
ネシウムのふつ化カルシウムに対するモル比が1.1以
上となるようにする。このようにしてぶつ化カルシウム
が未反応のまま残ることがないようにするのが望ましい
、なお、未反応の塩化マグネシウムが冷却固化した混合
塩中に混入しても、「溶解」工程で水に溶解するので容
易に除去される。
Moreover, since magnesium butoxide is produced by the reaction of formula (3), it is sufficient to react equimolar amounts of magnesium chloride and calcium fluoride, but if calcium butoxide remains unreacted, the above-mentioned "cooling Remaining in the mixed salt of magnesium butoxide and calcium chloride solidified in the `` process,
It does not dissolve in the next "dissolution" step with water and remains as an impurity in the fragmented magnesium. Therefore, in order to prevent calcium fluoride from remaining, the amount of magnesium chloride added should be greater than the theoretical amount calculated from equation (3), and the molar ratio of magnesium chloride to calcium fluoride should be 1.1 or more. . It is desirable to prevent calcium chloride from remaining unreacted in this way. Furthermore, even if unreacted magnesium chloride gets mixed into the cooled and solidified mixed salt, it will not dissolve in the water during the "dissolution" process. It dissolves and is easily removed.

上記の製造工程(A工程)では溶融状態の塩化マグネシ
ウム中にぶつ化カルシウムを投入したが、塩化マグネシ
ウムとぶつ化カルシウムを同時に融解してもよく、ある
いは更に塩化カルシウムを加え王者を同時に融解しても
よい。
In the above manufacturing process (Step A), calcium butoxide was added to molten magnesium chloride, but magnesium chloride and calcium butoxide may be melted at the same time, or calcium chloride may be further added and the champion may be melted at the same time. Good too.

上記の製造工程(A工程)では、(3)式の反応により
生成した混合塩を冷却し、この混合塩中の塩化カルシウ
ムや塩化マグネシウムを水で抽出して除去した。しかし
、これら塩化物の融点(Ca(/! *ニア72”C1
MgCj!iニア14℃)がぶつ化マグネシウムの融点
(1260℃)より低いことを利用して、第2図のB工
程に示すように、両者の融点間の温度、すなわち、前記
の塩化物は溶融状態にありぶつ化マグネシウムが固体の
状態を示す温度傾城まで冷却し、次いで濾過し、濾過器
を通過した融液を前工程へ戻して再利用してもよい、な
お、固体塩として得られるぶつ化マグネシウム中に酸化
により生成する酸化マグネシウムや酸化カルシウム(融
点、 Hg(h2800″C,Cab:2572°C)
が前記のように不純物として混入してくる場合には、冷
却後酸により溶解、除去しなければならない。
In the above manufacturing process (Step A), the mixed salt produced by the reaction of formula (3) was cooled, and calcium chloride and magnesium chloride in this mixed salt were removed by extraction with water. However, the melting point of these chlorides (Ca(/! *Near 72"C1
MgCj! Taking advantage of the fact that the temperature (near 14°C) is lower than the melting point of magnesium chloride (1260°C), as shown in step B in Figure 2, the temperature between the melting points of both, that is, the chloride is in a molten state. It is possible to cool down to a temperature at which the magnesium salt present in the solid state is in a solid state, and then filter it, and the melt that has passed through the filter may be returned to the previous step and reused. Magnesium oxide and calcium oxide produced by oxidation in magnesium (melting point, Hg (h2800″C, Cab: 2572°C)
If it is mixed in as an impurity as described above, it must be dissolved and removed with acid after cooling.

上記の説明は塩化マグネシウムとふっ化カルシウムから
ぶつ化マグネシウムを製造する場合であるが、イオン化
傾向を考慮して塩化物とぶつ化物を組み合わせれば、例
えば下記(4)式の反応によりぶつ化ナトリウム(Na
F)を得ることができる。
The above explanation is for producing magnesium fluoride from magnesium chloride and calcium fluoride, but if chloride and fluoride are combined in consideration of their ionization tendency, for example, sodium fluoride can be produced by the reaction of formula (4) below. (Na
F) can be obtained.

2NaCj!+CaFx =2NaF+CaC1z  
・・(4)さらに、ぶつ化リチウム(LiF)を用いれ
ば、他のふっ化物、例えばぶつ化バリウム(BaFi)
、ぶつ化カリウム(KF)なども容易に生成させること
ができる。ただし、生成物(ふう化物および塩化物)が
どちらも水溶性でぶつ化物を分離できない場合には、例
えば水のかわりにアルコールを使用するなど、「溶解」
工程における溶媒を適当に選択しなければならない。
2NaCj! +CaFx =2NaF+CaC1z
...(4) Furthermore, if lithium butoxide (LiF) is used, other fluorides such as barium butoxide (BaFi) can be used.
, potassium butoxide (KF), etc. can also be easily produced. However, if the products (fluoride and chloride) are both water-soluble and it is not possible to separate the fluorides, "dissolution" may be used, for example by using alcohol instead of water.
The solvent in the process must be selected appropriately.

(実施例1) 上部に蓋が取り付けられ、内部を不活性雰囲気にして融
解物の酸化を防ぐためのArガスの入口および出口と、
温度針を設けである石英製の円筒型容器(内径100m
m、高さ200m5+)に350gの塩化マグネシウム
を入れ、この容器全体を抵抗加熱炉に装入して塩化マグ
ネシウムの融点(714℃)以上の800℃に昇温した
。塩化マグネシウムが充分融解した後にふつ化カルシウ
ム100gを徐々に加え溶融状態で塩化マグネシウムと
反応させた。
(Example 1) A lid was attached to the top, and an inlet and an outlet for Ar gas to create an inert atmosphere inside and prevent oxidation of the melt;
A cylindrical container made of quartz with a temperature needle (inner diameter 100 m)
350 g of magnesium chloride was placed in a container (m, height 200 m5+), and the entire container was placed in a resistance heating furnace and heated to 800° C., which is higher than the melting point of magnesium chloride (714° C.). After the magnesium chloride was sufficiently melted, 100 g of calcium fluoride was gradually added to react with the magnesium chloride in a molten state.

その後、室温まで徐々に冷却した梅、得られた固化塩を
水で十分洗浄して、フィルターで濾過し、未反応の塩化
マグネシウムと反応により生成した塩化カルシウムを溶
解除去し、ぶつ化マグネシウムを分離した。
After that, the plums were gradually cooled to room temperature, and the solidified salt obtained was thoroughly washed with water and filtered to dissolve and remove the unreacted magnesium chloride and calcium chloride produced by the reaction, and the magnesium chloride was separated. did.

このふつ化マグネシウム中に酸化マグネシウムが検出さ
れたので、酢酸(5%)で洗浄し、さらに水で洗浄した
後、105°Cで乾燥した。これにより75gのふつ化
マグネシウム(純度=98%以上)を得ることができた
Since magnesium oxide was detected in this magnesium fluoride, it was washed with acetic acid (5%), further washed with water, and then dried at 105°C. As a result, 75 g of magnesium fluoride (purity = 98% or more) could be obtained.

(実施例2) 実施例1と同じ容器を使用し、塩化マグネシウム350
gと塩化カルシウム250gを混合した塩を800℃で
融解した0次いで、この混合塩にぶつ化カルシウム25
0gを徐々に加え、溶融状態で塩化マグネシウムと反応
させた。
(Example 2) Using the same container as in Example 1, magnesium chloride 350
A mixture of 250 g of calcium chloride and 250 g of calcium chloride was melted at 800°C.
0 g was gradually added to react with magnesium chloride in a molten state.

この場合は、実施例1に比較してふっ化カルシウムの融
解が速く、ぶつ化カルシウムの投入開始から反応終了ま
での時間は実施例1の約1/3であった。
In this case, the melting of calcium fluoride was faster than in Example 1, and the time from the start of adding calcium fluoride to the end of the reaction was about 1/3 that of Example 1.

その後の処理も実施例1と同様に行い、190gのふつ
化マグネシウム(純度:98%以上)を得ることができ
た。
The subsequent treatment was carried out in the same manner as in Example 1, and 190 g of magnesium fluoride (purity: 98% or more) could be obtained.

(発明の効果) 本発明方法によると、原料を溶融状態で反応させること
により目的のふつ化物を得ることができる。操作上の困
難性がなく、環境面における特別な対策を講じる必要も
ない、しかも、高価な原料を必要とせず、実用的価値は
極めて大きい。
(Effects of the Invention) According to the method of the present invention, a desired fluoride can be obtained by reacting raw materials in a molten state. It is not difficult to operate, does not require special environmental measures, and does not require expensive raw materials, so it has great practical value.

【図面の簡単な説明】[Brief explanation of drawings]

第1図および第2図は本発明方法によるふう化マグネシ
ウムの製造工程の一例を示す概略工程図で第1図はA工
程図、第2図はB工程図である。
1 and 2 are schematic process diagrams showing an example of the manufacturing process of magnesium fluoride according to the method of the present invention. FIG. 1 is a process diagram of A, and FIG. 2 is a diagram of process B.

Claims (2)

【特許請求の範囲】[Claims] (1)溶融状態で、イオン化傾向の小さい元素の塩化物
にこの元素より大きいイオン化傾向を示す元素のふっ化
物を反応させ、イオン化傾向の小さい元素のふっ化物を
得ることを特徴とするふっ化物の製造方法。
(1) A method of producing a fluoride characterized by reacting a chloride of an element with a small ionization tendency with a fluoride of an element showing a larger ionization tendency than the element in a molten state to obtain a fluoride of an element with a small ionization tendency. Production method.
(2)イオン化傾向の小さい元素の塩化物にこの元素よ
り大きいイオン化傾向を示す元素の塩化物を混合し、溶
融状態で前記の大きいイオン化傾向を示す元素のふっ化
物を反応させてイオン化傾向の小さい元素のふっ化物を
得ることを特徴とするふっ化物の製造方法。(3)溶融
状態で、塩化マグネシウムにふっ化カルシウムを反応さ
せることを特徴とするふっ化マグネシウムの製造方法。
(2) Mix the chloride of an element with a small ionization tendency with the chloride of an element with a larger ionization tendency than this element, and react with the fluoride of the element with a larger ionization tendency in the molten state. A method for producing fluoride, characterized by obtaining elemental fluoride. (3) A method for producing magnesium fluoride, which comprises reacting magnesium chloride with calcium fluoride in a molten state.
JP121690A 1990-01-08 1990-01-08 Production of fluoride Pending JPH03208815A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP121690A JPH03208815A (en) 1990-01-08 1990-01-08 Production of fluoride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP121690A JPH03208815A (en) 1990-01-08 1990-01-08 Production of fluoride

Publications (1)

Publication Number Publication Date
JPH03208815A true JPH03208815A (en) 1991-09-12

Family

ID=11495275

Family Applications (1)

Application Number Title Priority Date Filing Date
JP121690A Pending JPH03208815A (en) 1990-01-08 1990-01-08 Production of fluoride

Country Status (1)

Country Link
JP (1) JPH03208815A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008081380A (en) * 2006-09-29 2008-04-10 Hitachi Chem Co Ltd Processing liquid and method for forming fluoride-coated film

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008081380A (en) * 2006-09-29 2008-04-10 Hitachi Chem Co Ltd Processing liquid and method for forming fluoride-coated film

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