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JP7229028B2 - Method for producing N-mono(hydrocarbon) isocyanuric acid - Google Patents
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JP7229028B2 - Method for producing N-mono(hydrocarbon) isocyanuric acid - Google Patents

Method for producing N-mono(hydrocarbon) isocyanuric acid Download PDF

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JP7229028B2
JP7229028B2 JP2019014575A JP2019014575A JP7229028B2 JP 7229028 B2 JP7229028 B2 JP 7229028B2 JP 2019014575 A JP2019014575 A JP 2019014575A JP 2019014575 A JP2019014575 A JP 2019014575A JP 7229028 B2 JP7229028 B2 JP 7229028B2
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isocyanuric acid
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暢之 垣内
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Nissan Chemical Corp
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Description

本発明はN-モノ(炭化水素)イソシアヌル酸の製造方法の新規な製造方法に関する。 The present invention relates to a novel method for producing N-mono(hydrocarbon)isocyanuric acid.

イソシアヌル酸誘導体は、半導体分野を含めた様々な分野で用いられてきており(例えば、特許文献1~2)、その合成方法については、古くから種々の報告がなされている(例えば、非特許文献1~3)。
この状況の下、これまで本発明者らは、1つの炭化水素基を有するイソシアヌル酸誘導体の製造方法に関する報告をしている(特許文献3)。
Isocyanuric acid derivatives have been used in various fields including the semiconductor field (for example, Patent Documents 1 and 2), and various reports have been made on their synthesis methods for a long time (for example, Non-Patent Documents 1-3).
Under these circumstances, the present inventors have so far reported a method for producing an isocyanuric acid derivative having one hydrocarbon group (Patent Document 3).

国際公開第02/086624号WO 02/086624 国際公開第2013/035787号WO2013/035787 国際公開第2017/208910号WO2017/208910

Journal of American Chemical Society,75,pp.3617-3618(1953)Journal of American Chemical Society, 75, pp. 3617-3618 (1953) Tetrahedron Letters,44,pp.4399-4402(2003)Tetrahedron Letters, 44, pp. 4399-4402 (2003) Journal of Organic Chemistry,80,pp.11200-11205(2015)Journal of Organic Chemistry, 80, pp. 11200-11205 (2015)

従来知られている、1つのアルキル基を有するイソシアヌル酸誘導体の製造方法は、イソシアヌル酸の有機溶媒への溶解度が低い為、150℃以上の高温で長時間の加熱が必要となる。しかし高温反応では原料と生成物の分解による収率低下、及び逐次反応による収率と選択性の低下などが起こり、工業的に有用とはいえない。また高温で低沸点の試剤を使用する場合には密閉式の高圧反応装置が必要になるという問題もある。一方、低温反応ではイソシアヌル酸を溶解させるには大過剰の有機溶媒が必要となるので、容積効率が悪化し廃液が増加する問題が有った。
これらの問題の解決を図った特許文献3に記載の方法は、多段階の反応工程を経る必要があり、低コスト化、時間短縮化等の要因を考慮した場合、改善の余地があった。
A conventionally known method for producing an isocyanuric acid derivative having one alkyl group requires heating at a high temperature of 150° C. or higher for a long time because the solubility of isocyanuric acid in an organic solvent is low. However, the high-temperature reaction causes a decrease in yield due to decomposition of raw materials and products, and a decrease in yield and selectivity due to successive reactions, and is not industrially useful. There is also a problem that a closed high-pressure reactor is required when using a high-temperature, low-boiling reagent. On the other hand, in the low-temperature reaction, a large excess of organic solvent is required to dissolve isocyanuric acid.
The method described in Patent Document 3, which aims to solve these problems, needs to undergo a multi-step reaction process, and there is room for improvement when factors such as cost reduction and time reduction are considered.

本発明は、工業的製造に適するイソシアヌル酸誘導体の製造方法の提供を目的とし、すなわち、多段階の工程や煩雑な処理を必要とせず、目的とする誘導体の選択的な製造をワンポットにて可能とする新たな製造方法を提供することを目的とする。 The present invention aims to provide a method for producing an isocyanuric acid derivative suitable for industrial production, that is, it enables selective production of the desired derivative in one pot without requiring multi-step processes or complicated treatments. The purpose is to provide a new manufacturing method.

本発明者らは、上記の課題を解決するべく鋭意検討を行った結果、少量の溶媒に溶解させたイソシアヌル酸の過飽和溶液に、炭化水素基を導入するアルキル化剤等と塩基とを投入することにより、ワンポットにて、選択的にモノ置換体であるN-モノ(炭化水素)イソシアヌル酸が得られることを見出し、本発明を完成させた。 The present inventors have made intensive studies to solve the above problems. As a result, an alkylating agent for introducing a hydrocarbon group and a base are added to a supersaturated solution of isocyanuric acid dissolved in a small amount of solvent. Thus, the present inventors have found that a mono-substituted N-mono(hydrocarbon)isocyanuric acid can be selectively obtained in one pot, and have completed the present invention.

すなわち本発明は、第1観点として、イソシアヌル酸を出発物質とするN-モノ(炭化
水素)イソシアヌル酸の製造方法であって、イソシアヌル酸の過飽和溶液を調製する工程、及び前記過飽和溶液に、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基とを添加する工程、を含む製造方法に関する。
第2観点として、前記過飽和溶液が、イソシアヌル酸とアミド系溶媒とを含む、
第1観点に記載の製造方法に関する。
第3観点として、前記添加工程が、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基に加えて、さらに相間移動触媒の添加を含む、第1観点又は第2観点に記載の製造方法に関する。
That is, the present invention provides, as a first aspect, a method for producing N-mono(hydrocarbon)isocyanuric acid using isocyanuric acid as a starting material, comprising the steps of preparing a supersaturated solution of isocyanuric acid, and adding halogen to the supersaturated solution. It relates to a process comprising adding a hydrocarbyl compound or a pseudohalogenated hydrocarbon compound and a base.
As a second aspect, the supersaturated solution contains isocyanuric acid and an amide solvent,
It relates to the manufacturing method according to the first aspect.
As a third aspect, the production method according to the first aspect or the second aspect, wherein the addition step includes adding a phase transfer catalyst in addition to the halogenated hydrocarbon compound or the pseudohalogenated hydrocarbon compound and the base. Regarding.

本発明の製造方法によれば、多段階の工程や煩雑な処理を必要とせず、ワンポットにて、N-モノ(炭化水素)イソシアヌル酸を選択的に製造することができ、量産化を見据えた工業的に有用な製造方法を提供するこができる。 According to the production method of the present invention, it is possible to selectively produce N-mono(hydrocarbon)isocyanuric acid in one pot without the need for multi-step processes or complicated treatments, and it is expected to be mass-produced. An industrially useful production method can be provided.

本発明は、(1)イソシアヌル酸の過飽和溶液を調製する工程、及び、(2)前記過飽和溶液に、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基とを添加する工程を含む、N-モノ(炭化水素)イソシアヌル酸の製造方法を対象とする。 The present invention comprises the steps of (1) preparing a supersaturated solution of isocyanuric acid, and (2) adding a halogenated hydrocarbon compound or a pseudohalogenated hydrocarbon compound and a base to the supersaturated solution. A method for producing N-mono(hydrocarbon)isocyanuric acid is of interest.

本発明に係るN-モノ(炭化水素)イソシアヌル酸は、1つの炭化水素基を有するイソシアヌル酸誘導体を指し、イソシアヌル酸の窒素原子と結合する置換基として1つの炭化水素基が導入された下記式(1)で表される化合物を指す。

Figure 0007229028000001
上記式(1)において、Rは、例えば炭素原子数1乃至10の炭化水素基を表す。当該炭化水素基は、直鎖状、分岐鎖状、環状いずれでもよく、二重結合又は三重結合を少なくとも1つ有してもよい。前記炭化水素基がアルキル基である場合、当該アルキル基として、例えば、メチル基、エチル基、n-プロピル基、イソプロピル基、n-ブチル基、イソブチル基、n-ペンチル基、n-ヘキシル基、n-ヘプチル基、n-オクチル基、n-ペンチル基、n-ノニル基、n-デシル基、シクロヘキシルメチル基、及びシクロペンチルメチル基が挙げられる。アルキル基を除く前記炭化水素基として、例えば、ベンジル基、アリル基、及びプロパルギル基が挙げられる。 The N-mono (hydrocarbon) isocyanuric acid according to the present invention refers to an isocyanuric acid derivative having one hydrocarbon group, and the following formula in which one hydrocarbon group is introduced as a substituent bonded to the nitrogen atom of isocyanuric acid It refers to a compound represented by (1).
Figure 0007229028000001
In formula (1) above, R represents, for example, a hydrocarbon group having 1 to 10 carbon atoms. The hydrocarbon group may be linear, branched or cyclic, and may have at least one double bond or triple bond. When the hydrocarbon group is an alkyl group, examples of the alkyl group include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, n-pentyl group, n-hexyl group, n-heptyl, n-octyl, n-pentyl, n-nonyl, n-decyl, cyclohexylmethyl, and cyclopentylmethyl groups. Examples of the hydrocarbon groups other than alkyl groups include benzyl, allyl, and propargyl groups.

以下、本発明に係る各工程について説明する。 Each step according to the present invention will be described below.

(1)イソシアヌル酸の過飽和溶液を調製する工程
本工程は、出発物質であるイソシアヌル酸の過飽和溶液を調製する工程である。
当該過飽和溶液の調製に使用する溶媒として、特にアミド系溶媒を好適な溶媒として挙げることができる。
アミド系溶媒としては、例えば、N-メチルホルムアミド、N,N-ジメチルホルムアミド、N,N-ジエチルホルムアミド、N-メチルアセトアミド、N,N-ジメチルアセトアミド、N,N-ジメチルイソブチルアミド、N-メチル-2-ピロリドン、3-メトキシ-N,N-ジメチルプロパンアミド、3-ブトキシ-N,N-ジメチルプロパンアミド、1,3-ジメチル-2-イミダゾリジノン等を挙げることができるが、これらに限定
されない。これら溶媒は一種を単独で、また二種以上を混合して使用してもよい。
また、アミド系溶媒に加えて、本発明の効果を損ねない範囲において、アミド系溶媒以外のその他溶媒を併用してもよい。
(1) Step of preparing a supersaturated solution of isocyanuric acid This step is a step of preparing a supersaturated solution of isocyanuric acid as a starting material.
As the solvent used for preparing the supersaturated solution, an amide-based solvent is particularly suitable.
Examples of amide solvents include N-methylformamide, N,N-dimethylformamide, N,N-diethylformamide, N-methylacetamide, N,N-dimethylacetamide, N,N-dimethylisobutyramide, N-methyl -2-pyrrolidone, 3-methoxy-N,N-dimethylpropanamide, 3-butoxy-N,N-dimethylpropanamide, 1,3-dimethyl-2-imidazolidinone and the like, but these include Not limited. These solvents may be used singly or in combination of two or more.
In addition to the amide-based solvent, other solvents than the amide-based solvent may be used in combination within a range that does not impair the effects of the present invention.

当該過飽和溶液を調製するには、上記アミド系溶媒に、後述する冷却時において過飽和となる量のイソシアヌル酸を添加した後、系内を加熱してイソシアヌル酸を完全に溶解させ、その後、冷却すればよい。
このときの加熱温度は使用するアミド系溶媒の沸点以下の温度とすることができ、例えば80℃~150℃である。
To prepare the supersaturated solution, after adding an amount of isocyanuric acid that becomes supersaturated at the time of cooling, which will be described later, to the amide solvent, the system is heated to completely dissolve the isocyanuric acid, and then cooled. Just do it.
The heating temperature at this time can be a temperature below the boiling point of the amide solvent used, for example , 80°C to 150°C.

イソシアヌル酸が完全に溶解し、均一な溶液状となったことを確認した後、イソシアヌル酸の析出が生じないように系内を徐々に冷却し、イソシアヌル酸の過飽和溶液を得る。
このときの最終的な冷却温度は、後述する(2)工程で使用するハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物の融点以上乃至沸点以下の温度とすることができる。上記ハロゲン化又は擬ハロゲン化炭化水素化合物の選択にもよるが、最終的な冷却温度は、例えば30℃乃至60℃程度とすることができる。最終的な冷却温度は、目的とするN-モノ(炭化水素)イソシアヌル酸の製造に係る選択性を考慮するとより低温であることが好ましいが、低温下でのイソシアヌル酸析出の発生を考慮し、適宜選択すればよい。
After confirming that the isocyanuric acid has completely dissolved and becomes a uniform solution, the system is gradually cooled so as not to precipitate the isocyanuric acid to obtain a supersaturated solution of isocyanuric acid.
The final cooling temperature at this time can be a temperature above the melting point and below the boiling point of the halogenated hydrocarbon compound or pseudohalogenated hydrocarbon compound used in step (2) described later. Depending on the selection of the halogenated or pseudohalogenated hydrocarbon compound, the final cooling temperature can be, for example, about 30°C to 60°C. The final cooling temperature is preferably lower in consideration of the selectivity related to the production of the desired N-mono (hydrocarbon) isocyanuric acid, but considering the occurrence of isocyanuric acid precipitation at low temperatures, It can be selected as appropriate.

(2)前記過飽和溶液に、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基とを添加する工程
本工程は、前述の(1)工程で得た過飽和溶液に、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基とを添加する工程である。
(2) A step of adding a halogenated hydrocarbon compound or a pseudohalogenated hydrocarbon compound and a base to the supersaturated solution. Alternatively, it is a step of adding a pseudohalogenated hydrocarbon compound and a base.

上記ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物は、いわゆるアルキル化剤等と呼ばれる炭化水素基を導入することを目的として用いられる化合物を挙げることができる。 Examples of the halogenated hydrocarbon compound or the pseudohalogenated hydrocarbon compound include compounds used for the purpose of introducing a hydrocarbon group called an alkylating agent.

ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物としては、下記式(2)で表される化合物を挙げることができる。
R-X (2)
式中、Rは式(1)で例示したように、炭素原子数1乃至10の炭化水素基を表し、当該炭化水素基は、直鎖状、分岐鎖状、環状いずれでもよく、二重結合又は三重結合を少なくとも1つ有してもよい。
またXはハロゲン原子又は擬ハロゲン基を表す。
Examples of halogenated hydrocarbon compounds or pseudo-halogenated hydrocarbon compounds include compounds represented by the following formula (2).
RX (2)
In the formula, R represents a hydrocarbon group having 1 to 10 carbon atoms as exemplified in formula (1), and the hydrocarbon group may be linear, branched, or cyclic, and has a double bond. Alternatively, it may have at least one triple bond.
Also, X represents a halogen atom or a pseudohalogen group.

上記ハロゲン原子としては、ヨウ素原子、臭素原子、塩基原子及びフッ素原子から選ぶことができる。
Xがハロゲン原子を表す場合、式(2)で表される化合物はハロゲン化炭化水素化合物であり、例えばヨウ化メチル、臭化エチル、臭化プロピル、臭化アリル、及び臭化プロパルギルが挙げられるが、これらに限定されるものではない。
The halogen atom can be selected from an iodine atom, a bromine atom, a basic atom and a fluorine atom.
When X represents a halogen atom, the compound represented by formula (2) is a halogenated hydrocarbon compound, such as methyl iodide, ethyl bromide, propyl bromide, allyl bromide, and propargyl bromide. However, it is not limited to these.

上記擬ハロゲン基としては、例えば、メタンスルホニルオキシ基等のアルキルスルホニルオキシ基;トリフルオロメタンスルホニルオキシ基、ノナフルオロブタンスルホニルオキシ基等のフルオロアルキルスルホニルオキシ基;ベンゼンスルホニルオキシ基、トルエンスルホニルオキシ基等の芳香族スルホニルオキシ基等が挙げられる。
Xが擬ハロゲン基を表す場合、式(2)で表される化合物は擬ハロゲン化炭化水素化合物であり、例えば、p-トルエンスルホン酸メチル、p-トルエンスルホン酸メタンスルホン酸エチル等を挙げることができるが、これらに限定されるものではない。
Examples of the pseudohalogen group include alkylsulfonyloxy groups such as methanesulfonyloxy group; fluoroalkylsulfonyloxy groups such as trifluoromethanesulfonyloxy group and nonafluorobutanesulfonyloxy group; benzenesulfonyloxy group, toluenesulfonyloxy group and the like. and aromatic sulfonyloxy groups.
When X represents a pseudohalogen group, the compound represented by formula (2) is a pseudohalogenated hydrocarbon compound, and examples thereof include methyl p-toluenesulfonate and ethyl p-toluenesulfonate methanesulfonate. can be used, but is not limited to these.

ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物は、前記イソシアヌル酸過飽和溶液中のイソシアヌル酸1モル当量に対して、0.3モル当量乃至1.5モル当量にて使用することができる。 The halogenated hydrocarbon compound or the pseudohalogenated hydrocarbon compound can be used in an amount of 0.3 to 1.5 molar equivalents with respect to 1 molar equivalent of isocyanuric acid in the supersaturated solution of isocyanuric acid.

上記塩基としては、無機塩基を好適に用いることができる。
上記無機塩基としては、例えば炭酸ナトリウム、炭酸カリウム等のアルカリ金属炭酸塩;例えば炭酸カルシウム、炭酸マグネシウム等のアルカリ土類金属炭酸塩;例えば炭酸水素ナトリウム、炭酸水素カリウム等のアルカリ金属炭酸水素塩などが挙げられる。これらの中でもアルカリ金属炭酸塩が好ましく、炭酸ナトリウムを好ましく用いることができる。これら無機塩基は、単独で用いてもよいし、2種以上を混合して用いてもよい。また、無水物を用いてもよいし、水和物を用いてもよい。
上記無機塩基は、前記過飽和溶液中のイソシアヌル酸1モル当量に対して、0.3モル当量乃至1.5モル当量にて使用することができる。
An inorganic base can be preferably used as the base.
Examples of the inorganic base include alkali metal carbonates such as sodium carbonate and potassium carbonate; alkaline earth metal carbonates such as calcium carbonate and magnesium carbonate; and alkali metal hydrogen carbonates such as sodium hydrogen carbonate and potassium hydrogen carbonate. is mentioned. Among these, alkali metal carbonates are preferred, and sodium carbonate can be preferably used. These inorganic bases may be used alone or in combination of two or more. Moreover, an anhydride may be used and a hydrate may be used.
The inorganic base can be used in an amount of 0.3 to 1.5 molar equivalents with respect to 1 molar equivalent of isocyanuric acid in the supersaturated solution.

また(2)工程において、更に相間移動触媒を添加してもよい。
相間移動触媒としては、例えばベンジルトリメチルアンモニウムクロリド、ベンジルトリエチルアンモニウムクロリド、テトラメチルアンモニウムクロリド、テトラn-ブチルアンモニウムブロミド、硫酸水素テトラn-ブチルアンモニウム等の四級アンモニウム塩;例えばテトラフェニルホスホニウムブロミド等の四級ホスホニウム塩;例えば12-クラウン-4、18-クラウン-6等のクラウンエーテル類などが挙げられる。これらの中でも、四級アンモニウム塩を好ましい相間移動触媒として挙げることができる。これら相間移動触媒はそれぞれ単独で用いてもよいし、2種類以上を混合して用いてもよい。
上記相間移動触媒を使用する場合、その使用量は、前記過飽和溶液中のイソシアヌル酸1モル当量に対して、0.01モル当量乃至1.5モル当量にて使用することができる。
Moreover, in the step (2), a phase transfer catalyst may be added.
Examples of phase transfer catalysts include quaternary ammonium salts such as benzyltrimethylammonium chloride, benzyltriethylammonium chloride, tetramethylammonium chloride, tetra-n-butylammonium bromide, and tetra-n-butylammonium hydrogensulfate; quaternary phosphonium salts; crown ethers such as 12-crown-4, 18-crown-6 and the like. Among these, quaternary ammonium salts can be mentioned as preferable phase transfer catalysts. These phase transfer catalysts may be used alone or in combination of two or more.
When the phase transfer catalyst is used, it can be used in an amount of 0.01 to 1.5 molar equivalents with respect to 1 molar equivalent of isocyanuric acid in the supersaturated solution.

上記ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と塩基、また所望により相間移動触媒の添加は、前述の(1)のイソシアヌル酸の過飽和溶液を得る工程に引き続いて実施する。すなわち、前記(1)工程にて最終的に到達した冷却温度にて、上記ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物、塩基、そして所望により相間移動触媒を添加する。
これらを添加終了後、系内で、N-モノ(炭化水素)イソシアヌル酸が生成する反応が進行する。添加後、系内を撹拌することにより、N-モノ(炭化水素)イソシアヌル酸の生成をより進行させることができる。
添加後、反応温度(系内の温度)を前記(1)工程にて最終的に到達した冷却温度に保ってもよいし、低温下でのイソシアヌル酸析出の発生を考慮し、適宜選択すればよい。
また反応時間は、反応温度や、使用するハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物、塩基の種類、相間移動触媒の有無及び種類にもよるが、例えば0.1時間乃至10時間である。
The halogenated hydrocarbon compound or pseudohalogenated hydrocarbon compound, the base, and optionally the addition of the phase transfer catalyst are carried out subsequent to the above step (1) of obtaining a supersaturated solution of isocyanuric acid. That is, at the cooling temperature finally reached in the step (1), the above halogenated hydrocarbon compound or pseudohalogenated hydrocarbon compound, a base, and optionally a phase transfer catalyst are added.
After completion of the addition of these, a reaction to produce N-mono(hydrocarbon)isocyanuric acid proceeds in the system. By stirring the inside of the system after the addition, the production of N-mono(hydrocarbon)isocyanuric acid can be further promoted.
After the addition, the reaction temperature (temperature in the system) may be maintained at the cooling temperature finally reached in the step (1), or may be appropriately selected in consideration of the occurrence of isocyanuric acid precipitation at low temperatures. good.
The reaction time is, for example, 0.1 to 10 hours, depending on the reaction temperature, the halogenated hydrocarbon compound or pseudohalogenated hydrocarbon compound used, the type of base, and the presence or absence and type of phase transfer catalyst. .

なお、上記ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と塩基、また相間移動触媒を使用する場合の、それらの添加の順序は特に限定されない。好ましくは先に液状である成分を添加し、その後に固体の成分を添加すること、例えばハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物を添加し、その後、塩基、並びに使用する場合には相間移動触媒を添加することで、イソシアヌル酸の析出が発生し難いものとすることができる。 When the above halogenated hydrocarbon compound or pseudohalogenated hydrocarbon compound and a base, or a phase transfer catalyst is used, the order of their addition is not particularly limited. Preferably, the liquid component is added first, followed by the solid component, e.g., the halogenated hydrocarbon compound or pseudohalogenated hydrocarbon compound, followed by the base and, if used, interphase By adding a transfer catalyst, precipitation of isocyanuric acid can be made difficult to occur.

以下、実施例を挙げて本発明をより具体的に説明するが、本発明は下記の実施例に限定されるものではない。
なお実施例において、試料の調製及び物性の分析に使用した装置及び条件は、以下のと
おりである。
(1)HPLC:(株)島津製作所製 LC-2010A HTシステム
・カラム:HyperCarb(Thermo)、5μm、4.6×100mm
・オーブン:40℃
・検出器:UV210nm
・流速:1.0mL/分
・溶離液及び条件:A液=HPLC用アセトニトリル、B液=0.1質量%リン酸水溶液
0min B液90%→20min B液5%(グラジエーション)
20min~25min B液5%(継続)
25min B液5%→25.1min B液50%(グラジエーション)
25.1min~30min B液90%(継続)
・定量分析用内部標準物質:p-キシレン(モノメチルイソシアヌル酸の収率を内部標準で定量し、ジメチルイソシアヌル酸とトリメチルイソシアヌル酸の収率はピークの面積から感度比=1として計算した。)
・保持時間:イソシアヌル酸…2.3分、モノメチルイソシアヌル酸3.5分、ジメチルイソシアヌル酸7.0分、トリメチルイソシアヌル酸12.2分、p-キシレン16.0分
(2)H-NMR:日本電子株式会社製 JNM-ECA500
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited to the following examples.
In the examples, the equipment and conditions used for sample preparation and physical property analysis are as follows.
(1) HPLC: Shimadzu Corporation LC-2010A HT system column: HyperCarb (Thermo), 5 μm, 4.6 × 100 mm
・Oven: 40℃
・Detector: UV210nm
・Flow rate: 1.0 mL/min ・Eluent and conditions: A solution = acetonitrile for HPLC, B solution = 0.1 mass% phosphoric acid aqueous solution 0 min B solution 90% → 20 min B solution 5% (gradation)
20min-25min B liquid 5% (continued)
25 min B liquid 5% → 25.1 min B liquid 50% (gradation)
25.1min - 30min B liquid 90% (continued)
・ Internal standard substance for quantitative analysis: p-xylene (The yield of monomethylisocyanuric acid was quantified with an internal standard, and the yields of dimethylisocyanuric acid and trimethylisocyanuric acid were calculated from the peak areas with the sensitivity ratio = 1.)
Retention time: isocyanuric acid: 2.3 minutes, monomethylisocyanuric acid: 3.5 minutes, dimethylisocyanuric acid: 7.0 minutes, trimethylisocyanuric acid: 12.2 minutes, p-xylene: 16.0 minutes (2) 1 H-NMR : JNM-ECA500 manufactured by JEOL Ltd.

[実施例1] 過飽和条件での反応
ガラス製反応容器に、イソシアヌル酸(日産化学(株)製、商品名CA-P、以下同様。)1.04gとN,N-ジメチルホルムアミド(関東化学(株)製、特級、以下同様。)20.0gを入れ、120℃で撹拌し均一に溶解させた。その後、得られた溶液を徐々に40℃まで冷却していった。
過飽和となりイソシアヌル酸の固体が析出していないことを確認してから、ヨウ化メチル(東京化成工業(株)、以下同様。)1.14g、炭酸ナトリウム(関東化学(株)、特級、以下同様。)0.21gを順次加えた。
その後、得られた混合物を40℃のまま7時間撹拌したが、反応容器の底部に炭酸ナトリウムの溶け残りがあるものの、反応が進行して溶解度が低いイソシアヌル酸が減少し、溶解度が高いジメチルイソシアヌル酸(DMe-ICA)に変化した為、反応液からイソシアヌル酸の固体の析出は無く、淡黄色の溶液のままであった。
反応液をHPLC用アセトニトリル(関東化学株式会社)と純水を用いてメスフラスコにて希釈し、サンプリングして内部標準物質p-キシレンを加えてHPLCにて定量分析した。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸(MMe-ICA)が29.1%、そしてジメチルイソシアヌル酸(DMe-ICA)が7.9%、トリメチルイソシアヌル酸(TMe-ICA)が0.9%であった。得られた結果を表1に示す。
[Example 1] Reaction under supersaturated conditions In a glass reaction vessel, 1.04 g of isocyanuric acid (manufactured by Nissan Chemical Industries, Ltd., trade name CA-P, the same shall apply hereinafter) and N,N-dimethylformamide (Kanto Kagaku ( 20.0 g of special grade manufactured by Kabushiki Kaisha, Ltd. was added, and stirred at 120° C. to dissolve uniformly. The resulting solution was then gradually cooled to 40°C.
After confirming that the solid of isocyanuric acid is not precipitated due to supersaturation, methyl iodide (Tokyo Chemical Industry Co., Ltd., the same applies hereinafter) 1.14 g, sodium carbonate (Kanto Chemical Co., special grade, the same applies hereinafter) .) 0.21 g were added sequentially.
After that, the resulting mixture was stirred at 40° C. for 7 hours, but although there was undissolved sodium carbonate at the bottom of the reaction vessel, the reaction proceeded to reduce the amount of isocyanuric acid with low solubility and dimethylisocyanuric acid with high solubility. Since the solution was changed to an acid (DMe-ICA), no solid isocyanuric acid precipitated from the reaction solution, and remained a pale yellow solution.
The reaction solution was diluted with acetonitrile for HPLC (Kanto Kagaku Co., Ltd.) and pure water in a volumetric flask, sampled, p-xylene added as an internal standard, and quantitatively analyzed by HPLC.
As a result, the quantitative yield based on methyl iodide was 29.1% for the target monomethylisocyanuric acid (MMe-ICA), 7.9% for dimethylisocyanuric acid (DMe-ICA), and 7.9% for trimethylisocyanuric acid ( TMe-ICA) was 0.9%. Table 1 shows the results obtained.

[実施例2] 相間移動触媒を用いた過飽和条件での反応
ガラス製反応容器に、イソシアヌル酸1.04gとN,N-ジメチルホルムアミド20.0gを入れ、120℃で撹拌し均一に溶解させた。その後、得られた溶液を徐々に40℃まで冷却していった。
過飽和となりイソシアヌル酸の固体が析出していないことを確認してから、ヨウ化メチル1.14gを加えた。その後、テトラメチルアンモニウムクロリド(東京化成工業(株)製、以下同様)0.23gと炭酸ナトリウム0.21gを順次加えた。
その後、得られた混合物を40℃のまま7時間撹拌したが、反応容器の底部に炭酸ナトリウムの溶け残りがあるものの、反応が進行して溶解度が低いイソシアヌル酸が減少し、溶解度が高いジメチルイソシアヌル酸(DMe-ICA)に変化した為、反応液からイソシアヌル酸の固体の析出は無く、テトラメチルアンモニウムクロリド由来と思われる僅か
な濁りがある淡黄色の溶液のままであった。
反応液をHPLC用アセトニトリル(関東化学株式会社)と純水を用いてメスフラスコにて希釈し、サンプリングして内部標準物質p-キシレンを加えてHPLCにて定量分析した。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸(MMe-ICA)が33.7%、そしてジメチルイソシアヌル酸(DMe-ICA)が8.0%、トリメチルイソシアヌル酸(TMe-ICA)が0.8%であった。得られた結果を表1に示す。
[Example 2] Reaction under supersaturation conditions using a phase transfer catalyst 1.04 g of isocyanuric acid and 20.0 g of N,N-dimethylformamide were placed in a glass reaction vessel and stirred at 120°C to dissolve uniformly. . The resulting solution was then gradually cooled to 40°C.
After confirming that the mixture became supersaturated and no solid isocyanuric acid was precipitated, 1.14 g of methyl iodide was added. Thereafter, 0.23 g of tetramethylammonium chloride (manufactured by Tokyo Kasei Kogyo Co., Ltd., hereinafter the same) and 0.21 g of sodium carbonate were sequentially added.
After that, the resulting mixture was stirred at 40° C. for 7 hours, but although there was undissolved sodium carbonate at the bottom of the reaction vessel, the reaction proceeded to reduce the amount of isocyanuric acid with low solubility and dimethylisocyanuric acid with high solubility. Since the solution was changed to an acid (DMe-ICA), no solid isocyanuric acid precipitated from the reaction solution, and the solution remained as a pale yellow solution with slight turbidity thought to be derived from tetramethylammonium chloride.
The reaction solution was diluted with acetonitrile for HPLC (Kanto Kagaku Co., Ltd.) and pure water in a volumetric flask, sampled, p-xylene added as an internal standard, and quantitatively analyzed by HPLC.
As a result, the quantitative yield based on methyl iodide was 33.7% for the target monomethylisocyanuric acid (MMe-ICA), 8.0% for dimethylisocyanuric acid (DMe-ICA), and 8.0% for trimethylisocyanuric acid ( TMe-ICA) was 0.8%. Table 1 shows the results obtained.

[実施例3] 過飽和条件での反応
撹拌時間を7時間の代わりに1.5時間とした以外は、実施例1と同様の方法で、反応及び定量分析を行った。なお、この際、同様に、イソシアヌル酸の固体の析出は確認されなかった。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸が21.4%、そしてジメチルイソシアヌル酸が1.7%、トリメチルイソシアヌル酸が0.1%であった。得られた結果を表1に示す。
[Example 3] Reaction under supersaturated conditions Reaction and quantitative analysis were performed in the same manner as in Example 1, except that the stirring time was changed from 7 hours to 1.5 hours. At this time, similarly, no deposition of solid isocyanuric acid was confirmed.
As a result, the quantitative yield based on methyl iodide was 21.4% for monomethylisocyanuric acid, 1.7% for dimethylisocyanuric acid, and 0.1% for trimethylisocyanuric acid. Table 1 shows the results obtained.

[実施例4] 過飽和条件での反応
撹拌時間を7時間の代わりに0.5時間とした以外は、実施例1と同様の方法で、反応及び定量分析を行った。なお、この際、同様に、イソシアヌル酸の固体の析出は確認されなかった。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸が12.4%、そしてジメチルイソシアヌル酸が1.8%、トリメチルイソシアヌル酸が0.1%であった。得られた結果を表1に示す。
[Example 4] Reaction under supersaturated conditions Reaction and quantitative analysis were performed in the same manner as in Example 1, except that the stirring time was changed from 7 hours to 0.5 hours. At this time, similarly, no deposition of solid isocyanuric acid was confirmed.
As a result, the quantitative yield based on methyl iodide was 12.4% for monomethylisocyanuric acid, 1.8% for dimethylisocyanuric acid, and 0.1% for trimethylisocyanuric acid. Table 1 shows the results obtained.

[実施例5] イソシアヌル酸過剰量での反応
ヨウ化メチルの量を0.57gとし、撹拌時間を7時間の代わりに4時間とした以外は、実施例1と同様の方法で、反応及び定量分析を行った。なお、この際、同様に、イソシアヌル酸の固体の析出は確認されなかった。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸が52.5%、そしてジメチルイソシアヌル酸が10.5%、トリメチルイソシアヌル酸が1.0%であった。得られた結果を表1に示す。
[Example 5] Reaction with an excessive amount of isocyanuric acid Reaction and quantification were carried out in the same manner as in Example 1, except that the amount of methyl iodide was changed to 0.57 g and the stirring time was changed to 4 hours instead of 7 hours. Analysis was carried out. At this time, similarly, no deposition of solid isocyanuric acid was confirmed.
As a result, the quantitative yield based on methyl iodide was 52.5% for monomethylisocyanuric acid, 10.5% for dimethylisocyanuric acid, and 1.0% for trimethylisocyanuric acid. Table 1 shows the results obtained.

[実施例6] イソシアヌル酸過剰量での反応
ヨウ化メチルの量を0.57gとした以外は、実施例1と同様の方法で、反応及び定量分析を行った。なお、この際、同様に、イソシアヌル酸の固体の析出は確認されなかった。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸が49.5%、そしてジメチルイソシアヌル酸が7.5%、トリメチルイソシアヌル酸が0.8%であった。得られた結果を表1に示す。
[Example 6] Reaction with excessive amount of isocyanuric acid Reaction and quantitative analysis were performed in the same manner as in Example 1, except that the amount of methyl iodide was changed to 0.57 g. At this time, similarly, no deposition of solid isocyanuric acid was confirmed.
As a result, the quantitative yield based on methyl iodide was 49.5% for monomethylisocyanuric acid, 7.5% for dimethylisocyanuric acid, and 0.8% for trimethylisocyanuric acid. Table 1 shows the results obtained.

[実施例7] 溶媒量を削減しての反応
N,N-ジメチルホルムアミドの量を15.0gとした以外は、実施例1と同様の方法で、反応及び定量分析を行った。なお、この際、同様に、イソシアヌル酸の固体の析出は確認されなかった。
その結果、ヨウ化メチル基準での定量収率は、目的とするモノメチルイソシアヌル酸が22.7%、そしてジメチルイソシアヌル酸が5.6%、トリメチルイソシアヌル酸が0.7%であった。得られた結果を表1に示す。
[Example 7] Reaction with reduced amount of solvent Reaction and quantitative analysis were performed in the same manner as in Example 1, except that the amount of N,N-dimethylformamide was changed to 15.0 g. At this time, similarly, no deposition of solid isocyanuric acid was confirmed.
As a result, the quantitative yields based on methyl iodide were 22.7% for monomethylisocyanuric acid, 5.6% for dimethylisocyanuric acid, and 0.7% for trimethylisocyanuric acid. Table 1 shows the results obtained.

Figure 0007229028000002
Figure 0007229028000002

以上のように、本発明の製造方法によれば、ワンポットにて、目的とするイソシアヌル酸のモノ置換体であるN-モノ(炭化水素)イソシアヌル酸を生産効率よく選択的に得られることが確認された。 As described above, according to the production method of the present invention, it was confirmed that N-mono(hydrocarbon)isocyanuric acid, which is the desired mono-substituted isocyanuric acid, can be selectively obtained in one pot with high production efficiency. was done.

Claims (3)

イソシアヌル酸を出発物質とするN-モノ(炭化水素)イソシアヌル酸の製造方法であって、
イソシアヌル酸の過飽和溶液を調製する工程であって、イソシアヌル酸を溶媒に添加し80℃以上に加熱溶解し、均一な溶液状とする段階、その後60℃以下に冷却する段階を含む、イソシアヌル酸含有溶液を調製する工程、及び
前記過飽和溶液に、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基とを添加する工程、
を含む製造方法。
A method for producing N-mono(hydrocarbon)isocyanuric acid using isocyanuric acid as a starting material,
A process of preparing a supersaturated solution of isocyanuric acid, comprising the steps of adding isocyanuric acid to a solvent, heating and dissolving it at 80° C. or higher to form a uniform solution, and then cooling to 60° C. or lower, containing isocyanuric acid. preparing a solution, and adding a halogenated hydrocarbon compound or a pseudohalogenated hydrocarbon compound and a base to the supersaturated solution;
Manufacturing method including.
前記過飽和溶液が、イソシアヌル酸とアミド系溶媒とを含む、
請求項1に記載の製造方法。
The supersaturated solution contains isocyanuric acid and an amide solvent,
The manufacturing method according to claim 1.
前記添加工程が、ハロゲン化炭化水素化合物又は擬ハロゲン化炭化水素化合物と、塩基に加えて、さらに相間移動触媒の添加を含む、
請求項1又は請求項2に記載の製造方法。
wherein the adding step comprises addition of a halogenated hydrocarbon compound or a pseudohalogenated hydrocarbon compound and a base, as well as a phase transfer catalyst;
The manufacturing method according to claim 1 or 2.
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