JPS6335616B2 - - Google Patents
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- Publication number
- JPS6335616B2 JPS6335616B2 JP60054385A JP5438585A JPS6335616B2 JP S6335616 B2 JPS6335616 B2 JP S6335616B2 JP 60054385 A JP60054385 A JP 60054385A JP 5438585 A JP5438585 A JP 5438585A JP S6335616 B2 JPS6335616 B2 JP S6335616B2
- Authority
- JP
- Japan
- Prior art keywords
- acid
- molybdenum
- molybdic
- reaction
- monocarboxylic
- 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.)
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、夾雑物を殆ど含まないモノカルボン
酸モリブデン有機化合物の製造法に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a molybdenum monocarboxylate organic compound containing almost no impurities.
従来より知られているモリブデンモノカルボン
酸の製造法は、モリブデン酸のアルカリ金属塩、
アルカリ土族金属塩、ハロゲン化モリブデン、モ
リブデン酸アンモニウム、酸化モリブデンもしく
は、酸化モリブデンとアンモニアまたは、これら
の混合物とモノカルボン酸とを100〜300℃で反応
させる方法等が知られているが(特公昭52−
50768号公報)、これらの原料のうち三酸化モリブ
デンを除いては、モリブデン酸の塩類あるいはハ
ロゲン化合物である。これらの化合物とモノカル
ボン酸との反応においては、必然的に夾雑物とし
てモノカルボン酸と原料のモリブデン酸塩の塩基
成分との塩類あるいはハロゲン化物を生じ、これ
を取りのぞくことは容易な事ではない。例えばモ
リブデン酸アルカリ塩との反応に於いてモノカル
ボン酸アルカリ塩を副生しこれらは一部乳化剤と
しての性質も有しておりこれを取りのぞくことは
甚だ困難である。酸化モリブデンは塩類でなく塩
形成性夾雑物を含まない原料として知られている
が、これとモノカルボン酸との反応性は残念なが
ら極めて悪くこの反応は工業的実用性に欠けてい
るものである。
Conventionally known methods for producing molybdenum monocarboxylic acid include alkali metal salts of molybdic acid,
Methods are known in which alkaline earth metal salts, molybdenum halides, ammonium molybdate, molybdenum oxide, molybdenum oxide and ammonia, or mixtures thereof are reacted with monocarboxylic acids at 100 to 300°C (Tokuko Sho et al. 52−
50768), these raw materials, except for molybdenum trioxide, are salts of molybdic acid or halogen compounds. In the reaction of these compounds with monocarboxylic acid, salts or halides of the monocarboxylic acid and the base component of the raw material molybdate are inevitably produced as impurities, and it is not easy to remove these. do not have. For example, in the reaction with an alkali molybdate, an alkali monocarboxylic acid is produced as a by-product, and some of these also have properties as emulsifiers, and it is extremely difficult to remove them. Molybdenum oxide is known as a raw material that is not a salt and does not contain salt-forming impurities, but unfortunately the reactivity of this with monocarboxylic acids is extremely poor and this reaction lacks industrial practicality. .
本発明は、モリブデン酸とモノカルボン酸とを
効率よく反応させ、且つ不純物を含まないモノカ
ルボン酸モリブデンを製造する方法を提供するこ
とを目的とする。
An object of the present invention is to provide a method for efficiently reacting molybdic acid and monocarboxylic acid and producing molybdenum monocarboxylate free of impurities.
本発明は、沈殿法により生成したモリブデン酸
を乾燥することなく、ロ液がジフエニルアミンの
濃硫酸指示液で深青色を呈しなくなる程度まで、
またはインジゴカルミン溶液で5分間青色を保つ
程度まで水洗した後、モノカルボン酸と熱時反応
させることを特徴とするモノカルボン酸モリブデ
ンの製造方法である。
In the present invention, without drying the molybdic acid produced by the precipitation method, the filtrate is treated with a concentrated sulfuric acid indicator solution of diphenylamine to the extent that it no longer shows a deep blue color.
Alternatively, there is a method for producing molybdenum monocarboxylate, which comprises washing with an indigo carmine solution to the extent that it maintains a blue color for 5 minutes, and then reacting it with a monocarboxylic acid under heat.
モリブデン酸は現在は三酸化モリブデンをアル
カリに溶解してモリブデン酸塩を作り、この液に
強酸を加えモリブデン酸の結晶を作る方法が行わ
れておりモリブデン酸とモノカルボン酸との反応
がうまくおこなわれないのはモリブデン酸をつく
つた際の無機酸が一部含まれておりこれがモノカ
ルボン酸との反応を阻害していることを見出だ
し、これら不純物を除去したモリブデン酸とモノ
カルボン酸とを反応させることにより、従来殆ど
行われていないか、又は省りみられなかつた該反
応を工業的に効率よく行いうると共に夾雑物を含
まない純粋のモノカルボン酸モリブデンの製造に
成巧したものである。 Currently, molybdic acid is produced by dissolving molybdenum trioxide in an alkali to make a molybdate salt, and then adding a strong acid to this solution to form molybdic acid crystals, which allows the reaction between molybdic acid and monocarboxylic acid to occur successfully. They discovered that the reason why molybdic acid was not produced was that it contained some inorganic acid that inhibited the reaction with monocarboxylic acid when making molybdic acid. By reacting, this reaction, which has rarely been carried out or has not been neglected, can be carried out industrially and efficiently, and it has been successfully produced to produce pure molybdenum monocarboxylate free of impurities. .
一旦H2MoO4またはH2MoO4・H2Oとしてとり
出したもの(乾燥したもの)に就いて水洗を幾ら
おこなつても無機酸は殆ど除去されない。これは
恐らく結晶が凝集している為か、あるいは結晶水
中に無機酸が取り込まれていて、単なる水洗では
除去されないものと考えられる。このことに着目
して結晶として取り出し乾燥する前の段階で即ち
水濡れの状態時に、ロ液がジフエニルアミンの濃
硫酸指示液で深青色を呈しなくなる程度まで、ま
たはインジゴカルミン溶液で5分間青色を保つ程
度まで水洗することにより、無機酸及びその他の
夾雑物を殆ど含まないモリブデン酸を得ることが
出来ることを見出だした。驚くべきことに、この
モリブデン酸の当量を用いたモノカルボン酸との
反応は殆ど100%近くおこなわれた。また、因み
に再結晶によるモリブデン酸の精製法は現在のと
ころ知られていない。 Once taken out as H 2 MoO 4 or H 2 MoO 4 .H 2 O (dried), the inorganic acid is hardly removed no matter how many times it is washed with water. This is probably because the crystals are agglomerated, or perhaps the inorganic acid is incorporated into the crystallization water and cannot be removed by simple water washing. Focusing on this, before taking it out as a crystal and drying it, i.e. when it is wet with water, the filtrate remains blue with a concentrated sulfuric acid indicator solution of diphenylamine until it no longer shows a deep blue color, or with an indigo carmine solution for 5 minutes. It has been found that molybdic acid containing almost no inorganic acids and other impurities can be obtained by washing with water to a certain extent. Surprisingly, the reaction with the monocarboxylic acid using this equivalent amount of molybdic acid was almost 100% complete. Additionally, there is currently no known method for purifying molybdic acid by recrystallization.
本発明方法により得られるモノカルボン酸モリ
ブデンは、プロピレンの如きオレフインのエポキ
シ化を含む種々の反応における触媒として使用さ
れる。 The molybdenum monocarboxylate obtained by the process of the present invention is used as a catalyst in various reactions including the epoxidation of olefins such as propylene.
本発明で用いられるモノカルボン酸としては、
炭素数2〜30或いはそれ以上の脂肪族モノカルボ
ン酸、脂環式モノカルボン酸或いは芳香族モノカ
ルボン酸を用いることができる。 As the monocarboxylic acid used in the present invention,
Aliphatic monocarboxylic acids, alicyclic monocarboxylic acids, or aromatic monocarboxylic acids having 2 to 30 or more carbon atoms can be used.
即ち、酢酸、プロピレン酸、ブタン酸、ペンタ
ン酸、ヘキサン酸の如き低級脂肪酸、エナント
酸、オクタン酸、2―エチルヘキサン酸、カプリ
ル酸、カプリン酸の如き中級脂肪酸、ラウリン
酸、パルミチン酸、オレイン酸の如き高級脂肪
酸、シクロペンタン酸、シクロヘキサン酸、シク
ロカプリン酸、或いはナフテン酸の如き脂環式モ
ノカルボン酸、或いは安息香酸、1または2ナフ
トエ酸、o―,m―またはp―トルイル酸、フエ
ニル酢酸等の芳香族カルボン酸を使用しうる。 That is, lower fatty acids such as acetic acid, propylene acid, butanoic acid, pentanoic acid, hexanoic acid, intermediate fatty acids such as enanthic acid, octanoic acid, 2-ethylhexanoic acid, caprylic acid, capric acid, lauric acid, palmitic acid, and oleic acid. Higher fatty acids such as cyclopentanoic acid, cyclohexanoic acid, cyclocapric acid, or cycloaliphatic monocarboxylic acids such as naphthenic acid, or benzoic acid, mono- or di-naphthoic acid, o-, m- or p-toluic acid, phenyl Aromatic carboxylic acids such as acetic acid may be used.
また、本発明におけるモノカルボン酸とモリブ
デン酸の反応は極めて容易に定量的に行なわれる
ので、両者ほヾ等モル量を用いて反応を行わせる
ことが出来、反応温度は150℃から280℃特に220
〜230℃の範囲内の温度で行うのが好ましい。反
応は、反応に不活性な溶剤例えばプロピルベンゼ
ン(B.P.159℃)、クメン(B.P.152℃)、トリメチ
ルベンゼン(B.P.165℃〜176℃)、或いはデカン
(B.P.174℃)等の溶媒、あるいはそれらの混合
物、又は沸点150℃以上の石油系溶媒中で行えば
よい。 Furthermore, since the reaction between monocarboxylic acid and molybdic acid in the present invention is carried out very easily and quantitatively, the reaction can be carried out using equimolar amounts of both, and the reaction temperature is between 150°C and 280°C, particularly. 220
Preferably, it is carried out at a temperature within the range of -230°C. The reaction is carried out using an inert solvent such as propylbenzene (BP 159°C), cumene (BP 152°C), trimethylbenzene (BP 165°C to 176°C), or decane (BP 174°C), or a mixture thereof, or a boiling point It may be carried out in a petroleum solvent at a temperature of 150°C or higher.
また、反応生成物を触媒等として用いる場合に
は、反応生成物を溶媒から分離することなくその
まゝの形で使用しうる。 Furthermore, when the reaction product is used as a catalyst or the like, the reaction product can be used as it is without being separated from the solvent.
つぎに、本発明の実施例を記載する。 Next, examples of the present invention will be described.
実施例 1
600grの水に三酸化モリブデン220grを投入し、
28%アンモニア水192grを滴下し弱く加温しなが
ら撹はんを行い液が透明になつた後61%硝酸
220grを滴下更に加熱下約5時間撹はんした後、
室温まで冷却しその後12時間放置したところ反応
容器の底にモリブデン酸の結晶が沈殿した。上澄
み液を捨て、これに蒸留水1500c.c.を加え撹はん放
置および沈殿を分離する操作を4回繰り返した後
モリブデン酸をロ別しロ別されたロ紙上のモリブ
デン酸に更に水を注ぎ水洗を行いそのロ液が直ち
にジフエニールアミンの濃硫酸指示液で深青色を
呈しなくなるまで、またはインジゴカルミン溶液
で5分間青色を保つまで充分に水洗をした後低温
で乾燥した。Example 1 220g of molybdenum trioxide was added to 600g of water,
Drop 192g of 28% ammonia water and stir while heating gently until the liquid becomes clear, then add 61% nitric acid.
After adding 220gr dropwise and stirring for about 5 hours under heating,
When the mixture was cooled to room temperature and left for 12 hours, crystals of molybdic acid precipitated at the bottom of the reaction vessel. Discard the supernatant liquid, add 1500 c.c. of distilled water, leave to stir, and separate the precipitate. After repeating the operation four times, separate the molybdic acid and add water to the separated molybdic acid on the paper. After pouring and washing with water, the filtrate was immediately thoroughly washed with water using a concentrated sulfuric acid indicator solution of diphenylamine until it no longer showed a deep blue color, or with an indigo carmine solution until it remained blue for 5 minutes, and then dried at a low temperature.
この方法で得たモリブデン酸H2MoO4200grお
よび酸価221.1のナフテン酸627grを、石油系溶剤
(シエル化学製:商品名ロース,b.p.155℃〜194
℃)200grに混合し約12時間220℃〜230℃におい
て加熱撹はん反応後未反応のモリブデン酸をロ別
して取りのぞきMo11.6%を含有するモリブデン
ナフテネートの溶液を得た。 200 gr of molybdic acid H 2 MoO 4 obtained by this method and 627 gr of naphthenic acid with an acid value of 221.1 were mixed with a petroleum solvent (manufactured by Ciel Chemical: trade name: Loose, bp 155°C to 194° C.
C) 200gr and heated and stirred at 220 DEG C. to 230 DEG C. for about 12 hours. Unreacted molybdic acid was filtered off and removed to obtain a solution of molybdenum naphthenate containing 11.6% Mo.
またロ別して得られた未反応のモリブデン酸
H2MoO4は、9.8grであつた。即ち使用したモリ
ブデン酸にたいする反応率は、95.1%であつた。 Also, unreacted molybdic acid obtained by filtration
H 2 MoO 4 was 9.8 gr. That is, the reaction rate with respect to the molybdic acid used was 95.1%.
実施例 2
実施例1と同じ方法で得たモリブデン酸
H2MoO4200grおよび2―エチルヘキシル酸356gr
を石油系溶剤680grに混合し実施例1と同じ方法
で反応せしめたところMo9.8%を含有するモリブ
デン2―エチルヘキソエートの溶液を得た。Example 2 Molybdic acid obtained by the same method as Example 1
H 2 MoO 4 200gr and 2-ethylhexylic acid 356gr
was mixed with 680 gr of petroleum solvent and reacted in the same manner as in Example 1 to obtain a solution of molybdenum 2-ethylhexoate containing 9.8% Mo.
また未反応モリブデン酸H2MoO4は、4grであ
つた。即ち使用したモリブデンに対する反応率は
98%であつた。 Further, unreacted molybdic acid H 2 MoO 4 was 4 gr. In other words, the reaction rate for the molybdenum used is
It was 98%.
実施例 3
実施例1のナフテン酸の代りに、同モル数のプ
タン酸、カプリル酸又はオレイン酸を用いて実施
例1と同様にモリブデン酸と反応させたところ、
実施例1と殆んど同じ反応率で夫々の酸のモリブ
デン塩が得られた。Example 3 Instead of naphthenic acid in Example 1, the same number of moles of butanoic acid, caprylic acid, or oleic acid was used to react with molybdic acid in the same manner as in Example 1.
Molybdenum salts of each acid were obtained at almost the same reaction rate as in Example 1.
比較例
市販の三酸化モリブデンMoO372gr、酸価221.1
のナフテン酸254gr、石油系溶剤200grを混合し実
施例1と同じ方法で反応したところMo0.3%を含
有するモリブデンナフテネートの溶液を得た。Comparative example Commercially available molybdenum trioxide MoO 3 72gr, acid value 221.1
254g of naphthenic acid and 200g of petroleum solvent were mixed and reacted in the same manner as in Example 1 to obtain a solution of molybdenum naphthenate containing 0.3% Mo.
未反応の三酸化モリブデンMoO3は70grであつ
た即ち使用した三酸化モリブデンに対する反応率
は28%しかなかつた。 Unreacted molybdenum trioxide MoO 3 was 70 gr, ie, the reaction rate with respect to the molybdenum trioxide used was only 28%.
Claims (1)
ることなく、ロ液がジフエニルアミンの濃硫酸指
示液で深青色を呈しなくなる程度まで、またはイ
ンジゴカルミン溶液で5分間青色を保つ程度まで
水洗した後、モノカルボン酸と熱時反応させるこ
とを特徴とするモノカルボン酸モリブデンの製造
方法。1. Without drying the molybdic acid produced by the precipitation method, wash it with water until the filtrate no longer shows a deep blue color with a concentrated sulfuric acid indicator solution of diphenylamine, or until it remains blue for 5 minutes with an indigo carmine solution, and then dissolve the monocarboxylic acid. A method for producing molybdenum monocarboxylate, which comprises reacting with an acid under heat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5438585A JPS61215344A (en) | 1985-03-20 | 1985-03-20 | Production of molybdenum monocarboxylate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5438585A JPS61215344A (en) | 1985-03-20 | 1985-03-20 | Production of molybdenum monocarboxylate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61215344A JPS61215344A (en) | 1986-09-25 |
| JPS6335616B2 true JPS6335616B2 (en) | 1988-07-15 |
Family
ID=12969213
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5438585A Granted JPS61215344A (en) | 1985-03-20 | 1985-03-20 | Production of molybdenum monocarboxylate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61215344A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100332584B1 (en) | 1998-04-21 | 2002-04-15 | 노미야마 아키히콰 | Molybdenum soap-containing metal soaps and processes for producing the same |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5250768A (en) * | 1975-10-22 | 1977-04-23 | Seiko Epson Corp | Solar cell watch |
-
1985
- 1985-03-20 JP JP5438585A patent/JPS61215344A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61215344A (en) | 1986-09-25 |
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