JPH0892153A - Production of alkaline earth metallic salt of organic acid - Google Patents

Production of alkaline earth metallic salt of organic acid

Info

Publication number
JPH0892153A
JPH0892153A JP24845594A JP24845594A JPH0892153A JP H0892153 A JPH0892153 A JP H0892153A JP 24845594 A JP24845594 A JP 24845594A JP 24845594 A JP24845594 A JP 24845594A JP H0892153 A JPH0892153 A JP H0892153A
Authority
JP
Japan
Prior art keywords
alkaline earth
organic acid
earth metal
acid
metal salt
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
JP24845594A
Other languages
Japanese (ja)
Inventor
Kazuki Takatani
和樹 高谷
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.)
Shinto Paint Co Ltd
Original Assignee
Shinto Paint 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 Shinto Paint Co Ltd filed Critical Shinto Paint Co Ltd
Priority to JP24845594A priority Critical patent/JPH0892153A/en
Publication of JPH0892153A publication Critical patent/JPH0892153A/en
Pending legal-status Critical Current

Links

Landscapes

  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE: To economically obtain a solution of an alkaline earth metallic salt of an organic acid, containing an alkaline earth metal at a high concentration and useful as a precursor of an alkaline earth metallic oxide in the fields of fine ceramics or electronic materials. CONSTITUTION: The characteristics of this method for producing an alkaline earth metallic salt of an organic acid comprises reacting a 4-10C organic acid with an alkaline earth metallic salt in a stoichiometrically excessive amount of 0.1-1.0mol in reacting the organic acid with the alkaline earth metallic salt in a reactional solvent and producing the alkaline earth metallic salt of the organic acid.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ファインセラミックス
分野、あるいは電子材料分野における、アルカリ土類金
属酸化物前駆体として有用である、有機酸アルカリ土類
金属塩の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an organic acid alkaline earth metal salt, which is useful as an alkaline earth metal oxide precursor in the field of fine ceramics or in the field of electronic materials.

【0002】[0002]

【従来の技術】従来有機酸アルカリ土類金属塩の製造方
法としては、キシレンやミネラルスピリットなどの溶媒
を反応溶媒とし、炭素数が10以下の有機酸を用い、有
機酸に対する金属塩を理論化学当量以下、すなわちに1
モル未満反応して均一な溶液として得る方法。また、反
応溶媒なしで炭素数12〜30の脂肪族モノカルボン酸
とアルカリ土類金属塩を反応する方法(特開平4−20
8246号公報)などが提案されている。
2. Description of the Related Art Conventionally, as a method for producing an alkaline earth metal salt of an organic acid, a solvent such as xylene or mineral spirit is used as a reaction solvent, an organic acid having 10 or less carbon atoms is used, and a metal salt for the organic acid is theoretically chemistry Less than equivalent, ie 1
A method of obtaining a uniform solution by reacting less than a molar amount. Further, a method of reacting an aliphatic monocarboxylic acid having 12 to 30 carbon atoms with an alkaline earth metal salt without a reaction solvent (JP-A-4-20).
No. 8246) has been proposed.

【0003】[0003]

【発明が解決しようとする課題】しかしながら前記のキ
シレンやミネラルスピリットを反応溶媒とする方法で
は、アルカリ土類金属含有量の低い有機酸金属塩しか得
られない。また、特開平4−208246号公報による
有機酸を加熱撹拌しながらアルカリ土類金属の酸化物、
水酸化物、または炭酸塩などを添加する方法は、有機酸
に対し過剰のアルカリ土類金属塩を反応し、有機酸アル
カリ土類金属塩を生成することが出来るが、生成物は常
温では固体である。
However, the above-mentioned method using xylene or mineral spirit as a reaction solvent can only obtain an organic acid metal salt having a low alkaline earth metal content. Further, an organic acid according to JP-A-4-208246 is heated and stirred while an oxide of an alkaline earth metal,
The method of adding hydroxide, carbonate, etc. can react an excess of alkaline earth metal salt with an organic acid to produce an organic acid alkaline earth metal salt, but the product is solid at room temperature. Is.

【0004】[0004]

【課題を解決するための手段】本発明はアルカリ土類金
属を高濃度に含有する有機酸アルカリ土類金属塩溶液を
得る目的で鋭意研究の結果、有機酸とアルカリ土類金属
の酸化物、水酸化物、又は炭酸塩の反応において、沸点
160℃以上の反応溶媒を用いることにより有機酸2モ
ルに対し、アルカリ土類金属塩が1.1〜2モル、すな
わち有機酸2モルに対しアルカリ金属塩が理論化学当量
である1モル以上反応することが可能であることを見い
だしたことによるものである。
Means for Solving the Problems The present invention has been earnestly studied for the purpose of obtaining an organic acid alkaline earth metal salt solution containing an alkaline earth metal at a high concentration, and as a result of the research, an oxide of an organic acid and an alkaline earth metal, In the reaction of hydroxide or carbonate, 1.1 to 2 mol of the alkaline earth metal salt is used per 2 mol of the organic acid by using the reaction solvent having a boiling point of 160 ° C. or higher, that is, the alkali metal is based on 2 mol of the organic acid. This is because it was found that the metal salt can react at 1 mol or more, which is the theoretical chemical equivalent.

【0005】すなわち本発明は有機酸とアルカリ土類金
属塩を反応溶媒中で反応し、有機酸アルカリ土類金属塩
を製造する方法において、炭素数4〜10の有機酸に対
し、アルカリ土類金属塩を理論化学当量的に0.1〜
1.0モル過剰に反応させことを特徴とする有機酸アル
カリ土類金属塩の製造方法である。一般に有機酸とアル
カリ土類金属塩の反応モル比は、理論化学当量的には有
機酸2モルに対し、アルカリ土類金属塩が1.0モル未
満であり、反応生成物中の金属含有量は理論化学当量的
に決定されていた。しかし、本発明においては有機酸2
モルに対し、アルカリ土類金属塩が2モルまで反応する
ことが可能になったため、金属含有量は過剰反応率の
分、すなわちアルカリ土類金属塩0.1〜1モルに相当
する金属分だけ高くなる。ただし単にアルカリ土類金属
塩の過剰率をアップするのみでは反応中に固まりになり
やすく、極端な場合は撹拌出来なくなる。これを本発明
においては、沸点が160℃以上の有機溶剤を反応溶媒
として用いることにより、反応中の固化を避けるもので
ある。
That is, according to the present invention, an organic acid and an alkaline earth metal salt are reacted in a reaction solvent to produce an organic acid alkaline earth metal salt. The theoretical equivalent of metal salt is 0.1 to 0.1
A method for producing an alkaline earth metal salt of an organic acid, which comprises reacting in an excess of 1.0 mol. Generally, the reaction molar ratio of the organic acid and the alkaline earth metal salt is less than 1.0 mol of the alkaline earth metal salt with respect to 2 mol of the organic acid in terms of theoretical chemical equivalent, and the metal content in the reaction product is Has been determined stoichiometrically. However, in the present invention, the organic acid 2
Since it has become possible to react up to 2 moles of the alkaline earth metal salt with respect to the moles, the metal content is the excess reaction rate, that is, the metal content corresponding to 0.1 to 1 mole of the alkaline earth metal salt. Get higher However, simply increasing the excess ratio of the alkaline earth metal salt tends to cause solidification during the reaction, and in extreme cases, stirring cannot be performed. In the present invention, this is to avoid solidification during the reaction by using an organic solvent having a boiling point of 160 ° C. or higher as the reaction solvent.

【0006】実際の反応は反応溶媒中で有機酸とアルカ
リ土類金属塩を撹拌しながら常温〜150℃で5〜60
分保つのみで可能であるが、50〜100℃で行うこと
が望ましい。原料の添加順序も特に制限はなく、反応溶
媒と有機酸を加熱撹拌しながら、アルカリ土類金属塩の
スラリーを添加して反応する方法、また逆にアルカリ土
類金属塩のスラリーを撹拌しながら有機酸を添加する方
法のいずれを採用しても差し支えない。反応後の脱水は
必要に応じ、常圧又は減圧しながら50〜200℃に加
熱撹拌すればよく、特に制限はない。
The actual reaction is carried out at room temperature to 150 ° C. for 5 to 60 while stirring the organic acid and the alkaline earth metal salt in the reaction solvent.
It can be performed only by holding for minutes, but it is preferably performed at 50 to 100 ° C. The order of addition of the raw materials is not particularly limited, while stirring the reaction solvent and the organic acid with heating, a method of reacting by adding a slurry of an alkaline earth metal salt, or conversely while stirring a slurry of an alkaline earth metal salt. Any method of adding an organic acid may be adopted. The dehydration after the reaction may be performed by heating and stirring at 50 to 200 ° C. under normal pressure or reduced pressure, if necessary, and there is no particular limitation.

【0007】本発明に用いる有機酸としては炭素数4〜
10の飽和モノカルボン酸が望ましく、例えばイソヘプ
タン酸、イソオクタン酸、イソノナノイックさん、イソ
デカノイック酸、イソデカノイック酸、イソウンデカノ
イック酸、イソトリデカノイック酸、オクチル酸、2,
2−ジメチルプロピオン酸、n−ヘプタノイック酸、n
−ノナノイック酸、さらにナフテン酸、トール油脂肪酸
も用いることが出来る。また、それらは単独、あるいは
1〜2種以上を併用することも出来る。
The organic acid used in the present invention has 4 to 4 carbon atoms.
Saturated monocarboxylic acid of 10 is desirable, for example, isoheptanoic acid, isooctanoic acid, isononanoic acid, isodecanoic acid, isodecanoic acid, isoundecanoic acid, isotridecanoic acid, octylic acid, 2,
2-dimethylpropionic acid, n-heptanoic acid, n
Nonanoic acid, naphthenic acid, tall oil fatty acid can also be used. Further, they may be used alone or in combination of 1 or 2 or more.

【0008】マグネシュウム、カルシュウム、ストロン
チュウム、バリュウムなどのアルカリ土類金属塩の原料
としては、それぞれの酸化物、水酸化物、炭酸塩、酢酸
塩を用いることが可能で、実際の使用に際しては、添加
した場合の分散性をよくするため、予め有機溶剤または
水などの均一なスラリーとして用いることが望ましい。
As a raw material for alkaline earth metal salts such as magnesium, calcium, strontium and barium, respective oxides, hydroxides, carbonates and acetates can be used. In order to improve the dispersibility when added, it is desirable to use it in advance as a uniform slurry of an organic solvent or water.

【0009】反応溶媒として用いる有機溶剤は反応生成
物が溶解するもので、沸点が160℃以上のものであれ
ば特に制限はなく、例えばエチレングリコール、ブチル
カービトール、ブチルカービトールアセテート、テルピ
ネオール、nーパラフインなどを単独あるいは2種以上
混合したものを用いることが出来る。その場合、沸点が
160℃未満の溶剤、例えばキシレンを同じ量用いた場
合に比較して低粘度になる。また沸点が160℃以上の
溶剤と、160℃未満の溶剤を併用することも可能であ
る。
The organic solvent used as the reaction solvent is one in which the reaction product is dissolved and has a boiling point of 160 ° C. or higher and is not particularly limited. For example, ethylene glycol, butyl carbitol, butyl carbitol acetate, terpineol, n. Paraffin or the like may be used alone or in combination of two or more. In that case, the viscosity becomes lower than that when a solvent having a boiling point of less than 160 ° C., for example, xylene is used in the same amount. It is also possible to use a solvent having a boiling point of 160 ° C or higher and a solvent having a boiling point of less than 160 ° C in combination.

【0010】[0010]

【実施例】【Example】

実施例1 還流冷却管付き300ml反応用ビーカーにナフテン酸
(酸価200)100gとブチルカービトール9gを仕
込み、撹拌しながら40〜60℃に昇温後、酸化マグネ
シュウム11.7gと水20gからなる均一スラリーを
徐々に添加し、その後50〜95℃で約60分反応し
た。その後150℃まで昇温して脱水した後約50℃に
冷却した。その後n−ヘキサン50gで希釈し、珪藻土
(ラジオライト900)を用いて減圧ろ過をした。その
濾液をロータリエバポレーターで濃縮した結果、マグネ
シュウム5.5%を含む褐色透明の溶液が得られた。
Example 1 100 g of naphthenic acid (acid value 200) and 9 g of butyl carbitol were charged into a 300 ml reaction beaker equipped with a reflux condenser and heated to 40 to 60 ° C. with stirring, and then 11.7 g of magnesium oxide and 20 g of water. The uniform slurry was gradually added and then reacted at 50 to 95 ° C for about 60 minutes. After that, the temperature was raised to 150 ° C. to dehydrate, and then cooled to about 50 ° C. After that, it was diluted with 50 g of n-hexane and filtered under reduced pressure using diatomaceous earth (Radiolite 900). As a result of concentrating the filtrate with a rotary evaporator, a brown transparent solution containing 5.5% of magnesium was obtained.

【0011】実施例2 実施例1と同じ反応容器にオクチル酸(酸価385)1
00gとテルピネオール20gを仕込み、撹拌しながら
40〜60℃に昇温後、酸化マグネシュウム29.9g
と水35gからなる均一スラリーを徐々に添加し、その
後50〜95℃で約60分反応した。さらに120℃ま
で昇温して脱水後約50℃に冷却した。その後実施例1
と同じ方法で希釈し、ろ過、濃縮を行った結果、マグネ
シュウム含有量が11.5%の淡黄色透明な液体が得ら
れた。
Example 2 Octylic acid (acid value 385) 1 was placed in the same reaction vessel as in Example 1.
00 g and terpineol 20 g were charged, the temperature was raised to 40 to 60 ° C. with stirring, and then magnesium oxide 29.9 g
A uniform slurry of 35 g of water and 35 g of water was gradually added, and then the mixture was reacted at 50 to 95 ° C. for about 60 minutes. The temperature was further raised to 120 ° C., dehydrated and then cooled to about 50 ° C. Then Example 1
As a result of diluting in the same manner as above, filtering and concentrating, a pale yellow transparent liquid having a magnesium content of 11.5% was obtained.

【0012】実施例3 実施例1と同じ反応容器にセカノイック酸(酸価38
5)75gとブチルカービトールアセテート65gを仕
込み、撹拌しながら40〜60℃に昇温後、水酸化カル
シュウム28.6gとn−ヘキサン40gからなる均一
スラリーを徐々に添加し、その後50〜95℃で約60
分反応した。その後実施例1と同じ方法で希釈、ろ過、
濃縮を行った結果、カルシュウムを9.5%含有した無
色透明な液体が得られた。
Example 3 In the same reaction vessel as in Example 1, secanoic acid (acid value 38
5) 75 g and butyl carbitol acetate 65 g were charged, the temperature was raised to 40 to 60 ° C. with stirring, and then a uniform slurry of calcium hydroxide 28.6 g and n-hexane 40 g was gradually added, and then 50 to 95 ° C. About 60
It reacted for a minute. Dilution, filtration, and
As a result of concentration, a colorless transparent liquid containing 9.5% calcium was obtained.

【0013】実施例4 実施例1と同じ反応容器にオクチル酸75gとブチルカ
ービトール77gを仕込み室温で撹拌しながら40〜6
0℃に昇温後、水酸化ストロンチュウム103gを徐々
に添加し、その後50〜95℃で60分反応した。その
後実施例1と同じ方法で希釈、ろ過、濃縮を行った結
果、ストロンチュウム17%含有した無色透明な液体が
得られた。
Example 4 The same reaction vessel as in Example 1 was charged with 75 g of octylic acid and 77 g of butyl carbitol and stirred at room temperature for 40-6.
After the temperature was raised to 0 ° C., 103 g of strontium hydroxide was gradually added, and then the mixture was reacted at 50 to 95 ° C. for 60 minutes. After that, dilution, filtration, and concentration were carried out in the same manner as in Example 1, and as a result, a colorless transparent liquid containing 17% of strontium was obtained.

【0014】実施例5 実施例1と同じ反応容器にオクチル酸60gとブチルカ
ービトール72gを仕込み撹拌しながら40〜60℃に
昇温後、水酸化バリュウム98gを徐々に添加し、その
後50〜95℃で60分反応した。その後実施例1と同
じ方法で希釈、ろ過、濃縮を行った結果、バリュウム2
2%を含有した無色透明な液体が得られた。
Example 5 60 g of octylic acid and 72 g of butyl carbitol were charged in the same reaction vessel as in Example 1, the temperature was raised to 40 to 60 ° C. with stirring, 98 g of barium hydroxide was gradually added, and then 50 to 95. The reaction was carried out at 60 ° C for 60 minutes. After that, dilution, filtration, and concentration were performed in the same manner as in Example 1, and as a result,
A colorless transparent liquid containing 2% was obtained.

【0015】実施例6 実施例1と同じ反応容器にネオデカン酸(酸価320)
80gとミネラルスピリット69gを仕込み、撹拌しな
がら40〜60℃に昇温後、水酸化カルシュウム28g
とn−ヘキサン40gからなる均一スラリーを徐々に添
加し、その後50〜95℃で約60分反応した。その後
ミネラルスピリットを還流させながら140℃まで昇温
して脱水した。実施例1と同じ方法でろ過を行った結
果、カルシュウムを8.0%含有した淡黄色透明な液体
が得られた。
Example 6 Neodecanoic acid (acid value 320) was placed in the same reaction vessel as in Example 1.
Charge 80 g and 69 g of mineral spirits, heat to 40-60 ° C with stirring, and then add 28 g of calcium hydroxide.
A uniform slurry consisting of 40 g of n-hexane and 40 g of n-hexane was gradually added, and then reacted at 50 to 95 ° C. for about 60 minutes. Then, the mineral spirit was refluxed to raise the temperature to 140 ° C. for dehydration. As a result of filtration by the same method as in Example 1, a pale yellow transparent liquid containing 8.0% of calcium was obtained.

【0016】実施例7 実施例1と同じ反応容器にイソヘプタノイック酸(酸価
430)60gとテルピネオール94.3gを仕込み、
撹拌しながら40〜60℃に昇温後、水酸化バリュウム
60gとn−ヘキサン40gからなる均一スラリーを徐
々に添加し、その後50〜95℃で約60分反応した。
その後140℃まで昇温して脱水した。実施例1と同じ
方法でろ過、濃縮を行った結果、バリュウムを23.0
%含有した淡黄色透明な液体が得られた。
Example 7 The same reaction vessel as in Example 1 was charged with 60 g of isoheptanoic acid (acid value 430) and 94.3 g of terpineol,
After the temperature was raised to 40 to 60 ° C. with stirring, a uniform slurry of 60 g of barium hydroxide and 40 g of n-hexane was gradually added, and then reacted at 50 to 95 ° C. for about 60 minutes.
Then, the temperature was raised to 140 ° C. for dehydration. As a result of performing filtration and concentration in the same manner as in Example 1, 23.0% of barium was obtained.
% Pale yellow transparent liquid was obtained.

【0017】比較例1(実施例1の比較例) 実施例1の条件の内、ナフテン酸100g(酸価20
0)に対し、酸化マグネシュウム7.7gを用いたこと
以外は実施例1と同じ条件で操作した。その結果得られ
た溶液中のマグネシュウム含有量は3.5%であった。 比較例2(実施例1の比較例) 実施例1の条件の内、ブチルカービトールを用いないで
反応した。その結果、反応初期の段階で反応物が固化し
撹拌不能になった。
Comparative Example 1 (Comparative Example of Example 1) Under the conditions of Example 1, 100 g of naphthenic acid (acid value 20
In contrast to 0), operation was performed under the same conditions as in Example 1 except that 7.7 g of magnesium oxide was used. The content of magnesium in the resulting solution was 3.5%. Comparative Example 2 (Comparative Example of Example 1) Under the conditions of Example 1, the reaction was carried out without using butyl carbitol. As a result, the reaction product solidified in the initial stage of the reaction and stirring became impossible.

【0018】比較例3(実施例2の比較例) オクチル酸100gに対し、酸化マグネシュウム14.
8gを用いたこと以外は実施例2と同じ条件で操作し
た。その結果得られた溶液中のマグネシュウム含有量は
5.1%であった。
Comparative Example 3 (Comparative Example of Example 2) 100 g of octylic acid was mixed with 14.3 g of magnesium oxide.
It operated under the same conditions as in Example 2 except that 8 g was used. The resulting solution had a magnesium content of 5.1%.

【0019】比較例4(実施例2の比較例) 実施例2の条件の内、テルピネオールをキシレンに変更
して反応し、実施例2と同じ条件で操作した。その結果
マグネシュウム含有量が11%の固体が得られた。
Comparative Example 4 (Comparative Example of Example 2) Of the conditions of Example 2, terpineol was changed to xylene to react, and the same conditions as in Example 2 were used. As a result, a solid having a magnesium content of 11% was obtained.

【0020】比較例5 実施例1と同じ反応容器に酢酸120gを仕込み、常温
で撹判しながら、水酸化カルシュウム74gとキシレン
100gからなるスラリーを添加し、その後100℃ま
で昇温して反応したところ白濁し、さらに30分間保温
撹判を継続したが透明にならなかった。
Comparative Example 5 120 g of acetic acid was charged into the same reaction vessel as in Example 1, and while stirring at room temperature, a slurry of 74 g of calcium hydroxide and 100 g of xylene was added, and the temperature was raised to 100 ° C. to react. However, it became cloudy, and the stirring was continued for 30 minutes, but it did not become transparent.

【0021】比較例6 実施例1と同じ反応容器にステアリン酸(酸価204)
100gを仕込み加熱溶解し、撹判しながら90℃で水
酸化マグネシュウム7.8gを添加して30分間反応
後、110℃に昇温して脱水後、キシレン50gを少し
ずつ添加したところ、不透明なペースト状になった。
Comparative Example 6 Stearic acid (acid value 204) was placed in the same reaction vessel as in Example 1.
When 100 g was charged and dissolved by heating, 7.8 g of magnesium hydroxide was added at 90 ° C. with stirring, the mixture was reacted for 30 minutes, heated to 110 ° C. and dehydrated, and 50 g of xylene was added little by little. It became a paste.

【0022】[0022]

【発明の効果】ファインセラミックス分野や、電子材料
分野におけるアルカリ土類金属酸化物前駆体として有用
である、アルカリ土類金属を高濃度に含有する有機酸ア
ルカリ土類金属塩溶液を、経済的に得られるようになっ
た。
INDUSTRIAL APPLICABILITY An organic acid alkaline earth metal salt solution containing a high concentration of alkaline earth metal, which is useful as an alkaline earth metal oxide precursor in the field of fine ceramics and electronic materials, is economically prepared. I got it.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機酸とアルカリ土類金属塩を反応溶媒
中で反応し、有機酸アルカリ土類金属塩を製造する方法
において、炭素数4〜10の有機酸に対し、アルカリ土
類金属塩を理論化学当量的に0.1〜1.0モル過剰に
反応させことを特徴とする有機酸アルカリ土類金属塩の
製造方法。
1. A method for producing an organic acid alkaline earth metal salt by reacting an organic acid and an alkaline earth metal salt in a reaction solvent, wherein an alkaline earth metal salt is added to an organic acid having 4 to 10 carbon atoms. Is a stoichiometrically stoichiometrically equivalent to 0.1 to 1.0 molar excess, and a method for producing an alkaline earth metal salt of an organic acid.
【請求項2】 反応溶媒として沸点が160℃以上の有
機溶剤を用いる請求項1記載の有機酸アルカリ土類金属
塩の製造方法。
2. The method for producing an organic acid alkaline earth metal salt according to claim 1, wherein an organic solvent having a boiling point of 160 ° C. or higher is used as a reaction solvent.
JP24845594A 1994-09-16 1994-09-16 Production of alkaline earth metallic salt of organic acid Pending JPH0892153A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24845594A JPH0892153A (en) 1994-09-16 1994-09-16 Production of alkaline earth metallic salt of organic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24845594A JPH0892153A (en) 1994-09-16 1994-09-16 Production of alkaline earth metallic salt of organic acid

Publications (1)

Publication Number Publication Date
JPH0892153A true JPH0892153A (en) 1996-04-09

Family

ID=17178395

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24845594A Pending JPH0892153A (en) 1994-09-16 1994-09-16 Production of alkaline earth metallic salt of organic acid

Country Status (1)

Country Link
JP (1) JPH0892153A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1415976A1 (en) 2002-10-28 2004-05-06 Nof Corporation Organic acid metal salt and coating liquid containing the same for forming a metal oxide film
JP2004168754A (en) * 2002-10-28 2004-06-17 Nof Corp Organic acid metal salt and metal oxide film-forming coating liquid containing the same
JP2006160920A (en) * 2004-12-08 2006-06-22 San Nopco Ltd Fatty acid metal salt composition

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1415976A1 (en) 2002-10-28 2004-05-06 Nof Corporation Organic acid metal salt and coating liquid containing the same for forming a metal oxide film
JP2004168754A (en) * 2002-10-28 2004-06-17 Nof Corp Organic acid metal salt and metal oxide film-forming coating liquid containing the same
CN1331951C (en) * 2002-10-28 2007-08-15 日本油脂株式会社 Ogranic acid metal salt and coating liquid contg. same for forming metal xoide film
JP4677711B2 (en) * 2002-10-28 2011-04-27 日油株式会社 Organic acid metal salt and coating liquid for forming metal oxide thin film containing the same
JP2006160920A (en) * 2004-12-08 2006-06-22 San Nopco Ltd Fatty acid metal salt composition
JP4608619B2 (en) * 2004-12-08 2011-01-12 サンノプコ株式会社 Lubricant for coated paper

Similar Documents

Publication Publication Date Title
CN107567434B (en) Decarboxylative ketonization process for fatty acids or fatty acid derivatives
JP2015500791A (en) 5-sulfoisophthalates and process for producing the same
US3431298A (en) Process for the preparation of oxadicarboxylic acids
JPH0656850A (en) Organic cerium(iv) compound, its preparation and application
AU771484B2 (en) Process for the preparation of a pyridinemethanol compound
JPH0892153A (en) Production of alkaline earth metallic salt of organic acid
JP5820242B2 (en) Method for producing metal salt of perfluoroalkylsulfonic acid
US4550180A (en) Method for manufacture of N-formylaspartic anhydride
US2528803A (en) Preparation of metallic soaps
WO1988005773A1 (en) Process for preparing tetrakis (3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionyloxymethyl)methane
US6054600A (en) Non-toxic solvent soluble group IV and V metal acid salt complexes using polyether acid anhydrides
US5760265A (en) Process for preparation of an ester utilizing an esterifying catalyst
CN112300203B (en) Modification method of aluminum alkoxide
JP3225303B2 (en) Method for producing molybdenum monocarboxylate
JPS62283987A (en) Cobalt compound containing boron
JP2927880B2 (en) Method for producing 4,4'-dihydroxy-3,3 ', 5,5'-tetramethyldiphenylmethane
JP4556381B2 (en) Process for producing aliphatic monocarboxylic acid tin salt
US2654767A (en) Process of alcoholysis
CN108821966B (en) Method for synthesizing 3,3' - (1,4-phenylene) bis-glutaric acid
JP3839130B2 (en) Method for producing molybdenum-containing composite metal soap
JPH10120615A (en) Production of fatty acid metallic soap containing fatty acid salt of molybdenum
RU2612220C1 (en) Method of producing nickel 2-ethylhexanoate
JPH0210763B2 (en)
KR100468640B1 (en) Process for preparing a pure melamine Derivative
RU2186733C2 (en) Method of synthesis of metal sulfide