JP5026727B2 - Method for producing high purity cyanate ester - Google Patents

Method for producing high purity cyanate ester Download PDF

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JP5026727B2
JP5026727B2 JP2006101491A JP2006101491A JP5026727B2 JP 5026727 B2 JP5026727 B2 JP 5026727B2 JP 2006101491 A JP2006101491 A JP 2006101491A JP 2006101491 A JP2006101491 A JP 2006101491A JP 5026727 B2 JP5026727 B2 JP 5026727B2
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cyanate ester
reaction
tertiary amine
naphthols
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菅野  裕一
誠之 片桐
務 今川
文秀 竹内
正次 畑山
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Mitsubishi Gas Chemical Co Inc
Nippon Soda Co Ltd
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Description

本発明は、シアン酸エステルの工業的に有利な製造方法に関する。   The present invention relates to an industrially advantageous process for producing cyanate esters.

シアン酸エステルは、プリント基板用、電子部品の封止用、複合材料用、成形材料用及び接着材料用等として有用である。
従来、このシアン酸エステルの製造方法として、(1)ハロゲン化シアンとフェノール類を3級アミン存在下で反応させる方法、(2)アルコール系またはフェノール系のアルカリ金属塩とハロゲン化シアンとを反応させる方法が知られている。
The cyanate ester is useful for printed circuit boards, sealing electronic components, composite materials, molding materials, adhesive materials, and the like.
Conventionally, as a method for producing this cyanate ester, (1) a method in which cyanogen halide and phenols are reacted in the presence of a tertiary amine, and (2) a reaction between an alcoholic or phenolic alkali metal salt and cyanogen halide. The method of making it known is known.

しかしながら、(1)の方法は、揮発性の低い液状のジアルキルシアノアミドが副生し、生成するプレポリマーに不純物として残存し、熱硬化時に揮発してボイドを生じさせるという欠点を有する。また、(2)の方法では、アルコール系又はフェノール系化合物として水酸基の隣接位に嵩高い置換基を有するものを用いなければ、生成したシアネートがフェノキサイドと反応してイミドカーボネートを副生してしまうという問題があった。製品としてのシアン酸エステルの中に、ジアルキルシアノアミドやイミドカーボネート類等の副生物や未反応物等の不純物が存在すると、貯蔵安定性等を害し、ひいてはさらなるシアン酸エステルの制御された重合が困難となる。   However, the method (1) has a drawback that a liquid dialkylcyanoamide having low volatility is produced as a by-product and remains as an impurity in the resulting prepolymer and volatilizes during heat curing to generate voids. In the method (2), unless an alcoholic or phenolic compound having a bulky substituent at the adjacent position of the hydroxyl group is used, the produced cyanate reacts with phenoxide to produce imide carbonate as a by-product. There was a problem that. If there are impurities such as by-products such as dialkyl cyanoamides and imide carbonates and unreacted substances in the cyanate ester as a product, storage stability will be impaired, and further controlled polymerization of cyanate ester will occur. It becomes difficult.

これらの方法の改良法として、特許文献1には、水と有機溶媒との混合溶媒中、触媒量の3級アミンを用いて、置換基を有しないフェノール類のシアン酸エステルを製造する方法が提案されている。また、特許文献2、3には、反応溶媒として水を用い、アルカリ金属塩の存在下、フェノラートとハロゲン化シアンとを反応させることにより、副生物の生成が抑制され、高純度のシアン酸エステルを得る方法が提案されている。   As an improved method of these methods, Patent Document 1 discloses a method for producing a phenolic cyanate ester having no substituent using a catalytic amount of a tertiary amine in a mixed solvent of water and an organic solvent. Proposed. In Patent Documents 2 and 3, by using water as a reaction solvent and reacting phenolate with cyanogen halide in the presence of an alkali metal salt, the production of by-products is suppressed, and a high-purity cyanate ester is used. The method of obtaining is proposed.

しかしながら、特許文献1に記載の方法でもなお、イミドカーボネート類が副生することが特許文献2によって明らかにされている。また、特許文献2や3に記載された方法でも、目的物の収率等においてなお満足のいくものではなく、より効率よく高純度の目的物が得られる方法の開発が望まれていた。   However, Patent Document 2 reveals that imide carbonates are still produced as a by-product even in the method described in Patent Document 1. In addition, even the methods described in Patent Documents 2 and 3 are still not satisfactory in the yield of the target product, and the development of a method capable of obtaining a high-purity target product more efficiently has been desired.

本発明に関連して、特許文献4には、本発明の製造方法により得られるシアン酸エステルが開示されている。また、この文献には、3−メチルテトラヒドロフランなどの有機溶媒中、3級アミンなどの塩基性化合物の存在下、対応するフェノール化合物とハロゲン化シアンとを反応させることにより、目的とするシアン酸エステルが製造できる旨も記載されている。
特公昭56−3859号公報 特開平11−255735号公報 特開平11−263767号公報 特開2005−264154号公報
In relation to the present invention, Patent Document 4 discloses a cyanate ester obtained by the production method of the present invention. Further, in this document, a target cyanate ester is obtained by reacting a corresponding phenol compound with cyanogen halide in the presence of a basic compound such as tertiary amine in an organic solvent such as 3-methyltetrahydrofuran. It is also described that can be manufactured.
Japanese Patent Publication No.56-3859 JP-A-11-255735 JP-A-11-263767 JP 2005-264154 A

本発明は、このような従来技術の実情に鑑みてなされたものであり、ジアルキルシアノアミドやイミドカーボネート類等の副生を抑制し、より高純度のシアン酸エステルを高収率で得ることができる、シアン酸エステルの製造方法を提供することを課題とする。   The present invention has been made in view of such a situation of the prior art, and can suppress by-products such as dialkyl cyanoamides and imide carbonates to obtain a higher purity cyanate ester in a high yield. An object of the present invention is to provide a process for producing a cyanate ester.

本発明者等は、後述する式(II)で表されるシアン酸エステルを効率よく製造する方法について鋭意研究した結果、水と有機溶媒との二相系溶媒中、3級アミンを塩基として用い、pHを酸性に制御しながらナフトール類とハロゲン化シアンとを反応させると、ナフトール類の損失を防止でき、かつ、ジアルキルシアノアミド及びイミドカーボネート類等の副生を抑制でき、有機層中に安定に純度の高いシアン酸エステルを生成、抽出することができることを見出し、本発明を完成するに至った。   As a result of intensive studies on a method for efficiently producing a cyanate ester represented by the formula (II) described later, the present inventors have used a tertiary amine as a base in a two-phase solvent of water and an organic solvent. , By reacting naphthols with cyanogen halide while controlling the pH to be acidic, the loss of naphthols can be prevented, and by-products such as dialkylcyanoamides and imide carbonates can be suppressed, and the organic layer is stable. It was found that a highly pure cyanate ester can be produced and extracted, and the present invention has been completed.

かくして本発明によれば、下記(1)〜(4)のシアン酸エステルの製造方法が提供される。
(1)式(I)
Thus, according to the present invention, the following methods (1) to (4) for producing cyanate esters are provided.
(1) Formula (I)

Figure 0005026727
Figure 0005026727

(式中、nは1〜50の整数を表す。)で表されるナフトール類、ハロゲン化シアン、及び3級アミンを、水と有機溶媒の二相系溶媒中、酸性条件下で反応させることを特徴とする、式(II) (In the formula, n represents an integer of 1 to 50) The naphthols, cyanogen halide, and tertiary amine represented by the above are reacted in a two-phase solvent of water and an organic solvent under acidic conditions. Characterized by the formula (II)

Figure 0005026727
Figure 0005026727

(式中、nは前記と同じ意味を表す。)で表されるシアン酸エステルの製造方法。
(2)ハロゲン化シアンの前記二相系溶媒の酸性溶液に、前記ナフトール類、及び該ナフトール類の水酸基に対し1.0〜2.0当量の3級アミンを添加して、所定時間反応させた後、この反応系にさらに0.1〜1.0当量の3級アミンを添加して反応させることを特徴とする(1)に記載のシアン酸エステルの製造方法。
(Wherein n represents the same meaning as described above).
(2) Add 1.0 to 2.0 equivalents of a tertiary amine to the naphthols and the hydroxyl group of the naphthols in an acidic solution of the cyanide halide in the two-phase solvent, and react for a predetermined time. Thereafter, 0.1 to 1.0 equivalent of a tertiary amine is further added to the reaction system for reaction, and the process for producing a cyanate ester according to (1).

(3)pH6以下の酸性条件下で反応させることを特徴とする(1)又は(2)に記載のシアン酸エステルの製造方法。
(4)前記式(I)で表されるナフトール類の水酸基に対し、0.1〜3当量の酸を用いて反応系を酸性にすることを特徴とする(1)〜(3)いずれかに記載のシアン酸エステルの製造方法。
(3) The process for producing a cyanate ester according to (1) or (2), wherein the reaction is carried out under acidic conditions of pH 6 or less.
(4) Any of (1) to (3), wherein the reaction system is acidified using 0.1 to 3 equivalents of acid with respect to the hydroxyl group of the naphthols represented by the formula (I). The manufacturing method of cyanate ester as described in any one of.

本発明の製造方法によれば、ナフトール類の損失を防止でき、かつ、ジアルキルシアノアミド及びイミドカーボネート類等の副生を抑制して、安全かつ簡便に高純度のシアン酸エステルを高収率で得ることができる。   According to the production method of the present invention, loss of naphthols can be prevented, and by-products such as dialkylcyanoamides and imide carbonates can be suppressed, and high-purity cyanate esters can be produced safely and easily in high yield. Obtainable.

以下、本発明を詳細に説明する。
本発明は、前記式(I)で表されるナフトール類(以下、「ナフトール類(I)」という。)、ハロゲン化シアン及び3級アミンを、水と有機溶媒の二相系溶媒中、酸性条件下で反応させることを特徴とする、前記式(II)で表されるシアン酸エステル(以下、「シアン酸エステル(II)」という。)の製造方法である。
Hereinafter, the present invention will be described in detail.
In the present invention, naphthols represented by the above formula (I) (hereinafter referred to as “naphthols (I)”), cyanogen halide and tertiary amine are acidified in a two-phase solvent of water and an organic solvent. It is a process for producing a cyanate ester represented by the above formula (II) (hereinafter referred to as “cyanate ester (II)”), characterized by reacting under conditions.

本発明においては、前記式(I)で表されるナフトール類(I)を用いる。式(I)中、nは1〜50の整数を表し、1〜10が好ましい。   In the present invention, the naphthols (I) represented by the formula (I) are used. In formula (I), n represents an integer of 1 to 50, preferably 1 to 10.

前記ナフトール類(I)の多くは公知物質であり、公知の方法(例えば、特許3122834号、特許2866747号に記載の方法)により製造することができる。また、市販されているものをそのままナフトール類(I)として用いることもできる。   Most of the naphthols (I) are known substances and can be produced by known methods (for example, methods described in Japanese Patent Nos. 322834 and 2866747). Moreover, what is marketed can also be used as naphthols (I) as it is.

本発明に用いるハロゲン化シアンとしては、塩化シアン及び臭化シアンが挙げられる。
ハロゲン化シアンとしては、シアン化ナトリウム等の金属シアニドとハロゲンとを反応させる方法等の公知の製造方法により得られたハロゲン化シアンを用いてもよいし、市販品を用いてもよい。また、金属シアニドとハロゲンとを反応させて得られたハロゲン化シアンを含有する反応液をそのまま用いることもできる。
Examples of the cyanogen halide used in the present invention include cyanogen chloride and cyanogen bromide.
As the cyanide halide, a cyanide halide obtained by a known production method such as a method of reacting a metal cyanide such as sodium cyanide with a halogen may be used, or a commercially available product may be used. Further, a reaction solution containing cyanogen halide obtained by reacting metal cyanide and halogen can be used as it is.

ハロゲン化シアンの使用量は、ナフトール類(I)の水酸基に対して、通常0.5〜5当量、好ましくは0.8〜3当量、より好ましくは1.0〜1.5当量である。   The usage-amount of cyanogen halide is 0.5-5 equivalent normally with respect to the hydroxyl group of naphthol (I), Preferably it is 0.8-3 equivalent, More preferably, it is 1.0-1.5 equivalent.

本発明に用いる3級アミンとしては、特に制約なく、具体的には、トリメチルアミン、トリエチルアミン、トリ−n−ブチルアミン、トリアミルアミン、ジイソプロピルエチルアミン、ジエチル−n−ブチルアミン、メチルジ−n−ブチルアミン、メチルエチル−n−ブチルアミン、ドデシルジメチルアミン、トリベンジルアミン、トリエタノールアミン等の脂肪族第3級アミン;N,N−ジメチルアニリン、N,N−ジエチルアニリン、ジフェニルメチルアミン、ピリジン等の芳香族環状アミン;ジエチルシクロヘキシルアミン、トリシクロヘキシルアミン、1,4−ジアザビシクロ[2.2.2]オクタン、1,8−ジアザビシクロ[5.4.0]−7−ウンデセン、1,5−ジアザビシクロ[4.3.0]−5−ノネン等の脂肪族環状アミン;等が挙げられる。これらの中でも、収率よく目的物が得られることなどから、脂肪族第3級アミンが好ましく、トリメチルアミン、トリエチルアミン、トリ−n−ブチルアミン、ジイソプロピルエチルアミンがより好ましく、トリエチルアミンが特に好ましい。   The tertiary amine used in the present invention is not particularly limited, and specifically, trimethylamine, triethylamine, tri-n-butylamine, triamylamine, diisopropylethylamine, diethyl-n-butylamine, methyldi-n-butylamine, methylethyl -Aliphatic tertiary amines such as n-butylamine, dodecyldimethylamine, tribenzylamine, and triethanolamine; aromatic cyclic amines such as N, N-dimethylaniline, N, N-diethylaniline, diphenylmethylamine, and pyridine Diethylcyclohexylamine, tricyclohexylamine, 1,4-diazabicyclo [2.2.2] octane, 1,8-diazabicyclo [5.4.0] -7-undecene, 1,5-diazabicyclo [4.3. An aliphatic cyclic amine such as 0] -5-nonene; And the like. Among these, an aliphatic tertiary amine is preferable because the target product can be obtained in a high yield. Trimethylamine, triethylamine, tri-n-butylamine, and diisopropylethylamine are more preferable, and triethylamine is particularly preferable.

3級アミンの使用量は、ナフトール類(I)の水酸基に対して、通常1.0〜10当量であり、好ましくは1.0〜3.5当量、より好ましくは2.0〜3.0当量である。このような範囲で3級アミンを用いることにより、収率よく目的とするシアン酸エステルを得ることができる。   The amount of the tertiary amine used is usually 1.0 to 10 equivalents, preferably 1.0 to 3.5 equivalents, more preferably 2.0 to 3.0 equivalents relative to the hydroxyl group of the naphthols (I). Is equivalent. By using a tertiary amine in such a range, the target cyanate ester can be obtained with good yield.

また、後述するように、原料を残存させずに反応を完結させることができ、目的物を収率よく得ることができることから、3級アミンは分割して用いるのが好ましい。   Further, as will be described later, since the reaction can be completed without leaving the raw material, and the target product can be obtained with good yield, the tertiary amine is preferably used in divided portions.

本発明においては、反応溶媒として、水と有機溶媒との二相系溶媒を用いる。二相系溶媒を用いることで、塩基として3級アミンを用いても、低揮発性で液状のジアルキルシアノアミドの副生を抑制することができる。   In the present invention, a two-phase solvent of water and an organic solvent is used as the reaction solvent. By using a two-phase solvent, even if a tertiary amine is used as a base, by-product formation of a low-volatile and liquid dialkylcyanoamide can be suppressed.

また、本発明の製造方法によれば、いかなるときも攪拌を停止することにより反応の進行を停止させることができる。そのため、有害物質の発生等、万が一のトラブルにも迅速な対応が可能である。また、各種用途に対して障害となる塩素イオン等を水相に除去することができるため、高品質な製品を製造することができる。したがって、本発明の製造方法は工業的規模での実施に適している。   Further, according to the production method of the present invention, the progress of the reaction can be stopped by stopping stirring at any time. For this reason, it is possible to respond promptly to troubles such as the generation of harmful substances. Moreover, since chlorine ions etc. which become obstacles to various uses can be removed to the aqueous phase, a high-quality product can be produced. Therefore, the production method of the present invention is suitable for implementation on an industrial scale.

前記二相系溶媒に用いる水としては、特に制約されず、水道水であっても、蒸留水であっても、脱イオン水であってもよい。効率よく目的とするシアン酸エステルを得る上では、不純物の少ない蒸留水や脱イオン水の使用が好ましい。   The water used for the two-phase solvent is not particularly limited, and may be tap water, distilled water, or deionized water. In order to efficiently obtain the target cyanate ester, it is preferable to use distilled water or deionized water with few impurities.

前記二相系溶媒に用いる有機溶媒としては、水と非混和性で、反応に不活性なものであれば特に制約はない。具体的には、塩化メチレン、クロロホルム、四塩化炭素、クロロベンゼン、ブロモベンゼン等のハロゲン化炭化水素系溶媒;n−ヘキサン、シクロヘキサン、イソオクタン、シクロヘキサノン、シクロぺンタノン、2−ブタノン等の脂肪族系溶媒;ベンゼン、トルエン、キシレン、エチルベンゼン等の芳香族系溶媒;メチルエチルケトン、メチルイソブチルケトン等のケトン系溶媒;ベンゾニトリル等のニトリル系溶媒;ニトロベンゼン等のニトロ系溶媒;ジエチルエーテル、ジイソプロピルエーテル、テトラヒドロフラン等のエーテル系溶媒;酢酸エチル、安息香酸エチル等のエステル系溶媒;等が挙げられる。   The organic solvent used for the two-phase solvent is not particularly limited as long as it is immiscible with water and inert to the reaction. Specifically, halogenated hydrocarbon solvents such as methylene chloride, chloroform, carbon tetrachloride, chlorobenzene and bromobenzene; aliphatic solvents such as n-hexane, cyclohexane, isooctane, cyclohexanone, cyclopentanone and 2-butanone Aromatic solvents such as benzene, toluene, xylene and ethylbenzene; ketone solvents such as methyl ethyl ketone and methyl isobutyl ketone; nitrile solvents such as benzonitrile; nitro solvents such as nitrobenzene; diethyl ether, diisopropyl ether, tetrahydrofuran, etc. Ether solvents; ester solvents such as ethyl acetate and ethyl benzoate; and the like.

用いる二相系溶媒において、水と有機溶媒との使用割合は、水と有機溶媒との重量比で、通常、水:有機溶媒=1:100〜100:1、好ましくは1:10〜10:1、より好ましくは1:5〜5:1の範囲である。   In the two-phase solvent used, the ratio of water to organic solvent used is the weight ratio of water to organic solvent, usually water: organic solvent = 1: 100 to 100: 1, preferably 1:10 to 10: 1, more preferably in the range of 1: 5 to 5: 1.

また、二相系溶媒の使用量は、特に制限されないが、ナフトール類(I)1重量部に対して、通常0.1〜100重量部、好ましくは1〜50重量部である。   Moreover, the usage-amount of a two-phase type solvent is although it does not restrict | limit in particular, It is 0.1-100 weight part normally with respect to 1 weight part of naphthols (I), Preferably it is 1-50 weight part.

本発明の製造方法においては、酸性条件下で反応を行う。
酸性条件としては、pH6以下であるのが好ましく、イミドカーボネート等の副生物の生成抑制のために、pH1以下であるのがより好ましい。
In the production method of the present invention, the reaction is carried out under acidic conditions.
The acidic condition is preferably pH 6 or less, and more preferably pH 1 or less in order to suppress the formation of by-products such as imide carbonate.

反応系を酸性条件とするには、反応系に酸を添加すればよい。酸の添加量は、酸性条件で反応を行うことができる量であれば、特に限定されないが、収率よく目的とするシアン酸エステルを得る上では、ナフトール類(I)の水酸基に対して、0.1〜3当量の酸を添加することによるのが好ましい。   In order to make the reaction system acidic, an acid may be added to the reaction system. The amount of acid added is not particularly limited as long as the reaction can be carried out under acidic conditions. However, in order to obtain the desired cyanate ester in a high yield, the amount of acid added to the hydroxyl group of naphthols (I) Preference is given to adding 0.1 to 3 equivalents of acid.

用いる酸としては、塩酸、硝酸、硫酸、燐酸等の無機酸;酢酸、乳酸、プロピオン酸などの有機酸;が挙げられる。中でも、無機酸の使用が好ましく、塩酸の使用が特に好ましい。   Examples of the acid to be used include inorganic acids such as hydrochloric acid, nitric acid, sulfuric acid and phosphoric acid; organic acids such as acetic acid, lactic acid and propionic acid. Among these, use of an inorganic acid is preferable, and use of hydrochloric acid is particularly preferable.

ナフトール類(I)とハロゲン化シアンとの反応は、ハロゲン化シアン、ナフトール類(I)及び3級アミンを、前記二相系溶媒中、酸性条件下で撹拌することによって行うことができる。   The reaction of naphthols (I) and cyanogen halide can be carried out by stirring cyanogen halide, naphthols (I) and tertiary amine in the above two-phase solvent under acidic conditions.

具体的には、(i)前記二相系溶媒に、ハロゲン化シアン、ナフトール類(I)及び3級アミンの所定量を添加して、全容を撹拌する方法、(ii)ハロゲン化シアン及びナフトール類(I)の二相系溶媒の溶液中に、3級アミンを添加して、全容を撹拌する方法、(iii)ハロゲン化シアン及び3級アミンの二相系溶媒の溶液中に、ナフトール類(I)(又はナフトール類(I)の溶液)を添加して、全容を撹拌する方法、(iv)3級アミン及びナフトール類(I)の二相系溶媒の溶液中に、ハロゲン化シアンの水溶液を添加して、全容を撹拌する方法、(v)ハロゲン化シアンの二相系溶媒溶液中に、ナフトール類(I)及び3級アミンを添加して、全容を撹拌する方法等が挙げられる。   Specifically, (i) a method of adding a predetermined amount of cyanogen halide, naphthols (I) and tertiary amine to the two-phase solvent and stirring the whole volume, (ii) cyanogen halide and naphthol A method in which a tertiary amine is added to a solution of a biphasic solvent of the class (I) and the whole volume is stirred; (iii) a naphthol compound in a biphasic solvent of a cyanogen halide and a tertiary amine. (I) (or a solution of naphthols (I)) and the whole volume is stirred; (iv) a solution of a tertiary amine and a naphthol (I) in a two-phase solvent solution of cyanogen halide Examples include a method of stirring the entire volume by adding an aqueous solution, and a method of stirring the entire volume by adding (v) a naphthol (I) and a tertiary amine to a two-phase solvent solution of cyanogen halide. .

これらの中でも、収率よく目的とするシアン酸エステルを得る上では、(v)の方法が好ましい。(v)の方法の場合、副反応を抑制する上では、ナフトール類(I)及び3級アミンを適当な有機溶媒で希釈した溶液を添加するのが好ましい。ナフトール類(I)及び3級アミンを溶解させる有機溶媒としては、用いる二相系溶媒の有機溶媒と同じものであっても異なるものであっても構わない。   Among these, the method (v) is preferable for obtaining the target cyanate ester in a high yield. In the case of the method (v), it is preferable to add a solution obtained by diluting the naphthols (I) and the tertiary amine with an appropriate organic solvent in order to suppress side reactions. The organic solvent for dissolving the naphthols (I) and the tertiary amine may be the same as or different from the organic solvent of the two-phase solvent used.

なお、前述のように、3級アミンは所定量を分割して添加するのが好ましい。
3級アミンを分割して添加する方法としては、反応系にナフトール類(I)及び3級アミンの一部を有機溶媒で溶解させたものを滴下して所定時間反応させた後、さらに、残りの3級アミン(又は3級アミンの有機溶媒溶液)を滴下して反応を完結させる方法が挙げられる。
As described above, the tertiary amine is preferably added in a predetermined amount.
As a method of adding the tertiary amine in a divided manner, the naphthol (I) and a part of the tertiary amine dissolved in an organic solvent are dropped into the reaction system and reacted for a predetermined time, and then the remaining amount The tertiary amine (or the organic solvent solution of tertiary amine) is dripped and the reaction is completed.

より具体的には、反応系に、ナフトール類(I)及びナフトール類(I)の水酸基に対して1.0〜2.0当量の3級アミンを添加し、所定時間反応させた後、さらに0.1〜1.0当量の3級アミンを添加して反応させる方法が好ましい。このような方法により目的物を収率よく得ることができる。   More specifically, naphthols (I) and a tertiary amine equivalent to 1.0 to 2.0 equivalents of a hydroxyl group of naphthols (I) are added to the reaction system and reacted for a predetermined time. A method in which 0.1 to 1.0 equivalent of a tertiary amine is added and reacted is preferred. By such a method, the target product can be obtained with good yield.

反応温度は、ハロゲン化シアンとして塩化シアンを用いる場合は、通常−20〜+20℃の範囲である。より安全に反応を行う上では、−10〜0℃の範囲が好ましい。ハロゲン化シアンとして臭化シアンを用いる場合は、−5〜+50℃の範囲が好ましい。
反応時間は反応規模にもよるが、通常、数分から数時間である。
The reaction temperature is usually in the range of -20 to + 20 ° C when cyanogen chloride is used as the cyanogen halide. In order to perform the reaction more safely, a range of −10 to 0 ° C. is preferable. When cyanogen bromide is used as the cyanogen halide, a range of −5 to + 50 ° C. is preferable.
Although the reaction time depends on the reaction scale, it is usually from several minutes to several hours.

反応終了後は、通常の後処理操作、及び所望により分離・精製操作を行うことにより、目的とするシアン酸エステル(II)を単離することができる。   After completion of the reaction, the desired cyanate ester (II) can be isolated by carrying out ordinary post-treatment operations and, if desired, separation / purification operations.

具体的には、反応液からシアン酸エステル(II)を含む有機溶媒層を分取し、水洗後、濃縮または溶媒置換すればよい。濃縮する場合には、減圧下80℃以下の温度に加熱して有機溶媒を留去するのが好ましい。温度を高くしすぎると重合が始まるおそれがあるため好ましくない。   Specifically, an organic solvent layer containing cyanate ester (II) is separated from the reaction solution, washed with water, and then concentrated or solvent-substituted. In the case of concentration, it is preferable to distill off the organic solvent by heating to a temperature of 80 ° C. or lower under reduced pressure. An excessively high temperature is not preferable because polymerization may start.

得られるシアン酸エステル(II)の純度は、液体クロマトグラフィー又はIRスペクトル法等で分析することができる。   The purity of the obtained cyanate ester (II) can be analyzed by liquid chromatography, IR spectroscopy or the like.

本発明によれば、副生物の生成を抑え、高純度のシアン酸エステル(II)を高収率で得ることができる。
得られるシアン酸エステル(II)は、プリント基板用、電子部品の封止用、複合材料用、成形材料用及び接着材料用等として有用である。
According to the present invention, production of by-products can be suppressed, and high-purity cyanate ester (II) can be obtained in high yield.
The obtained cyanate ester (II) is useful for printed circuit boards, for sealing electronic components, for composite materials, for molding materials, and for adhesive materials.

以下、実施例により本発明をさらに詳細に説明する。但し、本発明はこれらの実施例により何ら限定されるものではない。   Hereinafter, the present invention will be described in more detail with reference to examples. However, the present invention is not limited to these examples.

(実施例1)
温度計、攪拌器、滴下漏斗及び還流冷却器を取りつけた反応器を予め0〜5℃に冷却しておき、その中に塩化シアン7.47g(0.122mol)、35%塩酸9.75g(0.0935mol)、水76ml、塩化メチレン44mlを仕込んだ。
Example 1
A reactor equipped with a thermometer, a stirrer, a dropping funnel and a reflux condenser was previously cooled to 0 to 5 ° C., and 7.47 g (0.122 mol) of cyanogen chloride and 9.75 g of 35% hydrochloric acid ( 0.0935 mol), 76 ml of water, and 44 ml of methylene chloride were charged.

反応器内の温度を−5〜+5℃、pH1以下を保ちながら、そこへ、1−ナフトールアラルキル(新日鐵化学社製、以下にて同じ。)20g(0.0935mol)、及びトリエチルアミン18.88g(0.187mol)を塩化メチレン92mlに溶解した溶液を1時間かけて滴下し、滴下終了後、同温度で15分間撹拌した。反応液を分液し、有機層を分取した。得られた有機層を水100mlで2回洗浄した後、減圧下で濃縮し、最終的に80℃で1時間濃縮乾固させて、目的とするシアン酸エステル23.2gを得た。   While maintaining the temperature in the reactor at −5 to + 5 ° C. and pH 1 or less, 20 g (0.0935 mol) of 1-naphthol aralkyl (manufactured by Nippon Steel Chemical Co., Ltd., the same applies below) and triethylamine 18. A solution in which 88 g (0.187 mol) was dissolved in 92 ml of methylene chloride was added dropwise over 1 hour. After completion of the addition, the solution was stirred at the same temperature for 15 minutes. The reaction solution was separated, and the organic layer was separated. The obtained organic layer was washed twice with 100 ml of water, concentrated under reduced pressure, and finally concentrated to dryness at 80 ° C. for 1 hour to obtain 23.2 g of the intended cyanate ester.

得られたシアン酸エステルを液体クロマトグラフィー及びIRスペクトルにより分析したところ、原料が約10%残存した。副反応により生じるジエチルシアノアミドの含有率は0.1重量%以下であった。また、硝酸銀を用いた電位差滴定で検出された塩素イオンは10ppm以下であった。   When the obtained cyanate ester was analyzed by liquid chromatography and IR spectrum, about 10% of the raw material remained. The content of diethylcyanoamide generated by the side reaction was 0.1% by weight or less. Moreover, the chlorine ion detected by potentiometric titration using silver nitrate was 10 ppm or less.

(実施例2)
温度計、攪拌器、滴下漏斗及び還流冷却器を取りつけた反応器を予め0〜5℃に冷却しておき、そこへ塩化シアン7.47g(0.122mol)、35%塩酸9.75g(0.0935mol)、水76ml、及び塩化メチレン44mlを仕込んだ。
(Example 2)
A reactor equipped with a thermometer, a stirrer, a dropping funnel and a reflux condenser was previously cooled to 0 to 5 ° C., to which 7.47 g (0.122 mol) of cyanogen chloride and 9.75 g (0% of 35% hydrochloric acid) 0935 mol), 76 ml of water, and 44 ml of methylene chloride.

この反応器内の温度を−5〜+5℃、pHを1以下を保ちながら、撹拌下、1−ナフトールアラルキル20g(0.0935mol)、及びトリエチルアミン14.16g(0.14mol)を塩化メチレン92mlに溶解した溶液を1時間かけて滴下し、滴下終了後、更にトリエチルアミン4.72g(0.047mol)を15分間かけて滴下した。   While maintaining the temperature in the reactor at -5 to + 5 ° C. and maintaining the pH at 1 or less, 20 g (0.0935 mol) of 1-naphthol aralkyl and 14.16 g (0.14 mol) of triethylamine were added to 92 ml of methylene chloride. The dissolved solution was added dropwise over 1 hour, and after completion of the addition, 4.72 g (0.047 mol) of triethylamine was further added dropwise over 15 minutes.

滴下終了後、同温度で15分間撹拌後、反応液を分液し、有機層を分取した。得られた有機層を水100mlで2回洗浄した後、減圧下で濃縮し、最終的に80℃で1時間濃縮乾固させて、目的とするシアン酸エステル23.5gを得た。   After completion of dropping, the reaction solution was separated after stirring at the same temperature for 15 minutes, and the organic layer was separated. The obtained organic layer was washed twice with 100 ml of water, then concentrated under reduced pressure, and finally concentrated to dryness at 80 ° C. for 1 hour to obtain 23.5 g of the intended cyanate ester.

得られたシアン酸エステルを、液体クロマトグラフィー及びIRスペクトルにより分析したところ、原料ピークは検出されなかった。副反応により生じるジエチルシアノアミドの含有率は0.1重量%以下であった。また、硝酸銀を用いた電位差滴定で検出された塩素イオンは10ppm以下であった。   When the obtained cyanate ester was analyzed by liquid chromatography and IR spectrum, no starting material peak was detected. The content of diethylcyanoamide generated by the side reaction was 0.1% by weight or less. Moreover, the chlorine ion detected by potentiometric titration using silver nitrate was 10 ppm or less.

(比較例1)
温度計、攪拌器、滴下漏斗及び還流冷却器を取りつけた反応器を予め0〜5℃に冷却しておき、その中に塩化シアン7.47g(0.122mol)、塩化メチレン44mlを仕込んだ。
反応器内の温度を−6〜−2℃とし、そこへ、塩化メチレン92mlで溶解した1−ナフトールアラルキル20g(0.0935mol)と、トリエチルアミン10.39g(0.103mol)溶液をこの反応器内に1時間かけて滴下し、滴下終了後、同温度で15分間撹拌した。
(Comparative Example 1)
A reactor equipped with a thermometer, a stirrer, a dropping funnel and a reflux condenser was previously cooled to 0 to 5 ° C., and 7.47 g (0.122 mol) of cyanogen chloride and 44 ml of methylene chloride were charged therein.
The temperature in the reactor was set to −6 to −2 ° C., and 20 g (0.0935 mol) of 1-naphthol aralkyl dissolved in 92 ml of methylene chloride and 10.39 g (0.103 mol) of triethylamine were added to the reactor. Was added dropwise over 1 hour, and after completion of the dropwise addition, the mixture was stirred at the same temperature for 15 minutes.

反応溶液に水100mlを加えて分液した後、有機層を水100mlで2回洗浄した。有機層を減圧下で濃縮し、最終的に80℃で1時間濃縮乾固し、目的とするシアン酸エステル23.5gを得た。
得られたシアン酸エステルを、液体クロマトグラフィーにて分析したところ、副反応により生じるジエチルシアノアミドが、3.3重量%不純物として含まれていた。
After adding 100 ml of water to the reaction solution for liquid separation, the organic layer was washed twice with 100 ml of water. The organic layer was concentrated under reduced pressure and finally concentrated to dryness at 80 ° C. for 1 hour to obtain 23.5 g of the intended cyanate ester.
The obtained cyanate ester was analyzed by liquid chromatography. As a result, diethylcyanoamide produced by the side reaction was contained as 3.3 wt% impurities.

(比較例2)
温度計、攪拌器、滴下漏斗及び還流冷却器を取りつけた反応器を予め0〜5℃に冷却しておき、その中に塩化シアン7.47g(0.122mol)、水82ml、塩化メチレン44mlを仕込んだ。
(Comparative Example 2)
A reactor equipped with a thermometer, stirrer, dropping funnel and reflux condenser was previously cooled to 0 to 5 ° C., and 7.47 g (0.122 mol) of cyanogen chloride, 82 ml of water and 44 ml of methylene chloride were contained therein. Prepared.

反応器内の温度を−5〜+5℃とし、そこへ、1−ナフトールアラルキル20g(0.0935mol)、及びトリエチルアミン14.16g(0.14mol)を塩化メチレン92mlに溶解した溶液を1時間かけて滴下し、滴下終了後、更にトリエチルアミン4.72g(0.047mol)を15分間かけて滴下した。滴下終了後、同温度で15分間撹拌したところ、有機溶媒不溶性の重合物が生成した。有機層を液体クロマトグラフィーにて分析したが、目的物も原料も検出されなかった。

The temperature in the reactor was set to −5 to + 5 ° C., and a solution of 20 g (0.0935 mol) of 1-naphthol aralkyl and 14.16 g (0.14 mol) of triethylamine in 92 ml of methylene chloride was added over 1 hour. After dropping, 4.72 g (0.047 mol) of triethylamine was further added dropwise over 15 minutes. After completion of the dropwise addition, the mixture was stirred at the same temperature for 15 minutes, whereby an organic solvent insoluble polymer was formed. The organic layer was analyzed by liquid chromatography, but neither the target product nor the raw material was detected.

Claims (4)

式(I)
Figure 0005026727
(式中、nは1〜50の整数を表す。)で表されるナフトール類、ハロゲン化シアン及び3級アミンを、水と有機溶媒の二相系溶媒中、酸性条件下で反応させることを特徴とする、式(II)
Figure 0005026727
(式中、nは前記と同じ意味を表す。)で表されるシアン酸エステルの製造方法。
Formula (I)
Figure 0005026727
(Wherein n represents an integer of 1 to 50), naphthols represented by the formula, cyanogen halide and tertiary amine are reacted in a two-phase solvent of water and an organic solvent under acidic conditions. Characteristic formula (II)
Figure 0005026727
(Wherein n represents the same meaning as described above).
ハロゲン化シアンの前記二相系溶媒の酸性溶液に、前記ナフトール類、及び該ナフトール類の水酸基に対し1.0〜2.0当量の3級アミンを添加して反応させた後、この反応系にさらに0.1〜1.0当量の3級アミンを添加して反応させることを特徴とする請求項1に記載のシアン酸エステルの製造方法。 In an acidic solution of the biphasic solvent cyanogen halide, the naphthols, and was allowed to reaction with the addition of tertiary amine of 1.0 to 2.0 equivalents relative to the hydroxyl group of the naphthol, the reaction The method for producing a cyanate ester according to claim 1, wherein 0.1 to 1.0 equivalent of a tertiary amine is further added to the system and reacted. pH6以下の酸性条件下で反応させることを特徴とする請求項1又は2に記載のシアン酸エステルの製造方法。   The method for producing a cyanate ester according to claim 1 or 2, wherein the reaction is carried out under acidic conditions of pH 6 or less. 前記式(I)で表されるナフトール類の水酸基に対し、0.1〜3当量の酸を用いて反応系を酸性にすることを特徴とする請求項1〜3のいずれかに記載のシアン酸エステルの製造方法。   The cyanide according to any one of claims 1 to 3, wherein the reaction system is acidified with 0.1 to 3 equivalents of acid with respect to the hydroxyl group of the naphthols represented by the formula (I). Production method of acid ester.
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