JPS5835515B2 - Production method of isocyanuric acid ester - Google Patents
Production method of isocyanuric acid esterInfo
- Publication number
- JPS5835515B2 JPS5835515B2 JP10962877A JP10962877A JPS5835515B2 JP S5835515 B2 JPS5835515 B2 JP S5835515B2 JP 10962877 A JP10962877 A JP 10962877A JP 10962877 A JP10962877 A JP 10962877A JP S5835515 B2 JPS5835515 B2 JP S5835515B2
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- reaction
- acid ester
- solvent
- cyanate
- yield
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Description
【発明の詳細な説明】
本発明はインシアヌル酸エステルの製造法の改良に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved method for producing incyanuric acid ester.
従来から非プロトン性極性溶媒中で脂肪族ノ・ロゲン化
化合物とシアン酸アルカリとを反応させてインシアヌル
酸エステルを製造する方法カ知られている(特公昭36
−3985号公報)。A method for producing incyanuric acid ester by reacting an aliphatic no-logogenated compound with an alkali cyanate in an aprotic polar solvent has been known (Japanese Patent Publication No. 1973).
-3985 publication).
この方法は、次の(1)及び(2)式に示す如く、中間
体としてイソシアン酸エステルが生成され、次いで同一
反応系内において、此のイソシアン酸エステルが三量化
(重合)され、インシアヌル酸エステルを生成すると考
えられている。In this method, as shown in the following formulas (1) and (2), isocyanate is produced as an intermediate, and then this isocyanate is trimerized (polymerized) in the same reaction system to produce incyanuric acid. It is thought to produce esters.
R1R2CHX+MeOCN−)R1R2CHNCO+
MeX(1)
3R1R2CHNCO→(R1R2CHNCO)3
(2)上記反応において反応系内の水分は次の(3)、
(4)及び(5)式に示す副反応を引き起し、インシア
ヌル酸エステルの著しい収率低下を来たす。R1R2CHX+MeOCN−)R1R2CHNCO+
MeX(1) 3R1R2CHNCO→(R1R2CHNCO)3
(2) In the above reaction, the moisture in the reaction system is as follows (3):
This causes the side reactions shown in formulas (4) and (5), resulting in a significant decrease in the yield of incyanuric acid ester.
(なお、上記式中R1、R2、Me及びXについては後
記する。(In the above formula, R1, R2, Me and X will be described later.
)また、反応系内の水分は上記(3)、(4)及び(5
)式に示す副反応の他に溶媒である非プロトン性極性化
合物の加水分解を引き起すなど、イソシアヌル酸エステ
ルの生成を著しく妨げるものである。) Also, moisture in the reaction system is reduced by the above (3), (4) and (5).
) In addition to the side reactions shown in the formula, it causes hydrolysis of the aprotic polar compound that is the solvent, which significantly hinders the production of isocyanuric acid ester.
従って、反応系内への水分の混入を極力避けなげればな
らない。Therefore, it is necessary to avoid the introduction of moisture into the reaction system as much as possible.
しかるに本発明に反応溶媒として用いられる非プロトン
性極性化合物および反応原料として用いられるシアン酸
アルカリは吸湿性が大きく、工業的製品中には多量の水
分を含有し、この水分を容易に除去することは困難であ
る。However, the aprotic polar compound used as a reaction solvent in the present invention and the alkali cyanate used as a reaction raw material are highly hygroscopic and contain a large amount of water in industrial products, making it difficult to easily remove this water. It is difficult.
本発明者は、イソシアヌル酸エステルの製造に際し、反
応に有害な水分を除去する方法につき、検討した結果本
発明を完成した。The present inventor completed the present invention as a result of studies on a method for removing moisture harmful to the reaction during the production of isocyanuric acid ester.
すなわち本発明の要旨は、非プロトン性極性溶媒中で脂
肪族ハロゲン化化合物と、シアン酸アルカリとを反応さ
せ、インシアヌル酸エステルを製造するに当り、溶媒お
よびシアン酸アルカリを反応器に仕込み、次いで脱水蒸
留を行った後、脂肪族ハロゲン化化合物を加えて反応さ
せることを特徴とするイソシアヌル酸エステルの製造法
に存する。That is, the gist of the present invention is to react an aliphatic halogenated compound and an alkali cyanate in an aprotic polar solvent to produce an incyanuric acid ester.The solvent and the alkali cyanate are charged into a reactor, and then The present invention relates to a method for producing an isocyanuric acid ester, which is characterized in that after dehydration distillation, an aliphatic halogenated compound is added and reacted.
本発明の脱水蒸留としては上記溶媒及びシアン酸アルカ
リを反応容器に仕込み、次いで常圧または減圧で該溶媒
の一部を蒸留することにより溶媒とともに含有水分を除
去する方法、反応溶媒、反応諸原料及び反応中間体に不
活性かつ水と共沸混合物を生ずるような有機溶媒、たと
えばベンゼントルエン、キシレン等を加えて、該有機溶
媒とともに、反応溶媒及びシアン酸アルカリに含有され
る水分を共沸蒸留する方法等を挙げることができる。The dehydration distillation of the present invention includes a method in which the above-mentioned solvent and alkali cyanate are charged into a reaction vessel, and then a part of the solvent is distilled under normal pressure or reduced pressure to remove water contained together with the solvent, reaction solvent, and reaction raw materials. Then, an inert organic solvent that forms an azeotrope with water, such as benzene-toluene or xylene, is added to the reaction intermediate, and water contained in the reaction solvent and alkali cyanate is removed by azeotropic distillation along with the organic solvent. Examples of methods include:
本発明で用いられる非プロトン性極性溶媒としては、例
えばジメチルホルムアミド、ジメチルスルホキシド、N
−メチルアセタミド、アセトニトリル、テトラメチル尿
素などを挙げることが出来る。Examples of the aprotic polar solvent used in the present invention include dimethylformamide, dimethyl sulfoxide, N
- Methylacetamide, acetonitrile, tetramethylurea, etc. can be mentioned.
脂肪族ハロゲン化化合物としては一般に
R1R2CHXなる化学式で表わされる化合物で、式中
Xは・・ロゲン原子(塩素、臭素もしくは沃素)を示し
、また、R1、R2は水素原子もしくは脂肪族炭化水素
基、あるいは部分置換炭化水素基を表わし、R1、R2
はそれぞれ同一でも、別異でも差支えない。The aliphatic halogenated compound is generally a compound represented by the chemical formula R1R2CHX, where X represents a logen atom (chlorine, bromine or iodine), and R1 and R2 are a hydrogen atom or an aliphatic hydrocarbon group, Or it represents a partially substituted hydrocarbon group, R1, R2
may be the same or different.
脂肪族炭化水素基としては、アルキル基、アルケニル基
、アルキニル基、アラルキル基、シクロアルキル基、シ
クロアルケニル基であり、部分置換脂肪族炭化水素基と
は脂肪族炭化水素基の水素原子の1個または2個以上が
ハロゲン原子、ニトロ基、シアン基、カルボニル基、ア
ルコキシ基のいずれかで置換されていてもよく、また、
R1、R2の末端の水素原子がそれぞれメチレン基、メ
チン基、フェニレン基、酸素原子、硫黄原子、カルボニ
ル基などに置換され、R1、R2が環状構造をとってい
る場合でも差支えない。Examples of aliphatic hydrocarbon groups include alkyl groups, alkenyl groups, alkynyl groups, aralkyl groups, cycloalkyl groups, and cycloalkenyl groups, and a partially substituted aliphatic hydrocarbon group refers to one hydrogen atom of the aliphatic hydrocarbon group. or two or more may be substituted with a halogen atom, a nitro group, a cyan group, a carbonyl group, or an alkoxy group, and
There is no problem even when the terminal hydrogen atoms of R1 and R2 are each substituted with a methylene group, a methine group, a phenylene group, an oxygen atom, a sulfur atom, a carbonyl group, etc., and R1 and R2 have a cyclic structure.
シアン酸アルカリとしては一般にMeOCNまたはMe
NCOなる化学式で表わされる化合物で、Meはアルカ
リ金属原子を示す。The alkali cyanate is generally MeOCN or Me.
In the compound represented by the chemical formula NCO, Me represents an alkali metal atom.
代表的なものはシアン酸リチウム、シアン酸カリウム、
シアン酸す) IJウムの単一もしくは二種以上の混合
物である。Typical examples are lithium cyanate, potassium cyanate,
It is a single type of cyanic acid or a mixture of two or more types.
脂肪族ハロゲン化化合物とシアン酸アルカリとの反応量
比は、脂肪族ハロゲン化化合物1モルに対しシアン酸ア
ルカ!70.8〜5.0モルの範囲が好ましく、両者と
も純度が良いものであれば大体等モル近辺の量を使用す
ることが出来る。The reaction amount ratio of aliphatic halogenated compound and alkali cyanate is 1 mole of aliphatic halogenated compound to alkali cyanate! The range of 70.8 to 5.0 moles is preferable, and as long as both have good purity, approximately equimolar amounts can be used.
しかし反応を速く終了させたい場合には、シアン酸アル
カリを計算量よりやや過剰量使用することが好ましく、
必ずしも前記モル比に限定されるものではない。However, if you want to complete the reaction quickly, it is preferable to use alkali cyanate in an amount slightly in excess of the calculated amount.
The molar ratio is not necessarily limited to the above molar ratio.
反応温度は前記したような溶媒を使用する場合50〜2
50℃、一般には70〜150℃で反応が円滑に進行す
る。The reaction temperature is 50 to 2 when using the above-mentioned solvent.
The reaction proceeds smoothly at 50°C, generally from 70 to 150°C.
反応時間は脂肪族ハロゲン化化合物、シアン酸アルカリ
の量とか種類とかにより、また溶媒の量などにより一部
に言うことは出来ないが、通常1〜20時間である。The reaction time depends on the amount and type of aliphatic halogenated compound and alkali cyanate, as well as the amount of solvent, but it is usually 1 to 20 hours.
反応溶媒の使用量は操作の難易とか、反応時間に関係す
るものであって、溶媒が多ければ短かく、少なげれば長
い傾向にあり、特に限定されるものではないが、シアン
酸アルカリの重量の約1〜10倍の範囲が好ましい。The amount of reaction solvent used is related to the difficulty of operation and the reaction time, and the more solvent there is, the shorter the reaction time, and the less it is, the longer it will be. A range of about 1 to 10 times the weight is preferred.
本発明は脂肪族ハロゲン化化合物とシアン酸アルカリの
反応によりインシアヌル酸エステルを製造する製造方法
に有効であるが、該反応の際反応系に沃化アルカリ、臭
化アルカリなどの反応促進剤を用いてもよい。The present invention is effective in the production method of producing incyanuric acid ester by the reaction of an aliphatic halogenated compound and an alkali cyanate, but a reaction accelerator such as an alkali iodide or an alkali bromide is used in the reaction system during the reaction. It's okay.
また、副反応抑制剤として酢酸カルシウム、安息香酸カ
ルシウムなどの周期律表中第2族の金属塩を用いる方法
においても同様の効果を有する。Further, a similar effect can be obtained in a method using a metal salt of Group 2 in the periodic table, such as calcium acetate or calcium benzoate, as a side reaction inhibitor.
次に本発明を実施例を挙げて説明するが、本発明は以下
の実施例に限定されるものではない。Next, the present invention will be explained with reference to examples, but the present invention is not limited to the following examples.
実施例 1
301の反応器に水分0.12%のジエチルホルムアミ
ド10に9、純度94%、水分0.3%のシアン酸カリ
ウム4.5kg、トルエン0.3kgを加え、攪拌しな
から110’GK加熱し、単蒸留によりトルエン0.1
5に9を留去した。Example 1 Add 10 to 9 parts of diethylformamide with a water content of 0.12%, 4.5 kg of potassium cyanate with a purity of 94% and a water content of 0.3%, and 0.3 kg of toluene to a 301 reactor, and add 110' without stirring. GK heating, toluene 0.1 by simple distillation
9 was distilled off to 5.
系内の残留水分は0.02%であった。The residual moisture in the system was 0.02%.
次いで120℃に昇温し、沃化メチル4.32kgを3
時間を要して仕込み、100〜120℃で3時間攪拌を
続けてから冷却した。Next, the temperature was raised to 120°C, and 4.32 kg of methyl iodide was added to 3
It took a long time to prepare the mixture, and the mixture was continuously stirred at 100 to 120°C for 3 hours, and then cooled.
反応混合物を遠心分離し、固形物をジエチルホルムアミ
ドで洗浄し、f液を合わせて減圧蒸留(67〜69℃7
15朋Hg)してジエチルホルムアミドを回収した。The reaction mixture was centrifuged, the solid was washed with diethylformamide, and the liquid f was combined and distilled under reduced pressure (67-69℃, 7℃).
15 Hg) to recover diethylformamide.
蒸留残渣を水中に投入して析出する結晶を戸別し、メタ
ノールより再結晶すると、融点176〜177℃のイン
シアヌル酸トリメチル1.54kyが得られた。The distillation residue was poured into water, and the precipitated crystals were separated and recrystallized from methanol to obtain 1.54 ky of trimethyl incyanurate with a melting point of 176-177°C.
これは収率約89%(沃化メチル基準)である。This is a yield of about 89% (based on methyl iodide).
比較例 1
反応器内にトルエンを加えず共沸蒸留による脱水操作を
行なわない以外は、実施例1と同様の方法にてインシア
ヌル酸トリメチルを得た。Comparative Example 1 Trimethyl incyanurate was obtained in the same manner as in Example 1, except that toluene was not added to the reactor and dehydration by azeotropic distillation was not performed.
該収量は1.13に9であり、収率は約65%である。The yield is 1.13 to 9, which is about 65%.
実施例 2
実施例1と同様の反応器に水分0.1%のジメチルアセ
タミド10に、p、純度94.5%、水分062%ノシ
アン酸カリウム2.83kg、m−キシレン0.1に9
を加え、攪拌しながら120℃に加熱し、単蒸留により
m−キシレン0.07に9を留去した。Example 2 Into the same reactor as in Example 1, 10% dimethylacetamide with 0.1% moisture, 2.83 kg of potassium nocyanate, 94.5% purity, 62% moisture, and 0.1 m-xylene were added. 9
was added and heated to 120° C. with stirring, and 9 was distilled off to 0.07 m-xylene by simple distillation.
系内の残留水分は0.03%であった。The residual moisture in the system was 0.03%.
次いで130℃に昇温し、臭化n−プロピル3.7に!
gを4時間かかつて加えた。Then, the temperature was raised to 130°C to give 3.7 n-propyl bromide!
g was added for 4 hours.
その後同温度で2時間攪拌して冷却した。Thereafter, the mixture was stirred at the same temperature for 2 hours and cooled.
反応混合物を遠心分離し、固形物をジメチルアセタミド
で洗浄し、F液を合わせ減圧蒸留(83〜b
タミドを回収した。The reaction mixture was centrifuged, the solid matter was washed with dimethylacetamide, and the solution F was combined and distilled under reduced pressure (83-b) Tamide was recovered.
蒸留残渣に水、ベンゼンを加え、反応生成物をベンゼン
で抽出し、ベンゼンを留去後、減圧蒸留(116〜b
してイソシアヌル酸) IJ n−プロピル2.4kg
を得た。Add water and benzene to the distillation residue, extract the reaction product with benzene, distill off the benzene, and then distill under reduced pressure (116-b to produce isocyanuric acid) IJ n-propyl 2.4 kg
I got it.
これは収率約94%(臭化n−プロピル基準)である。This is a yield of about 94% (based on n-propyl bromide).
比較例 2
反応器内xm−キシレンを加えず共沸蒸留による脱水操
作を行なわない以外は、実施例2と同様の方法にてイン
シアヌル酸トリn−プロピルを得た。Comparative Example 2 Tri-n-propyl incyanurate was obtained in the same manner as in Example 2, except that xm-xylene was not added to the reactor and the dehydration operation by azeotropic distillation was not performed.
該収量は1.71kgであり、収率は約67%である。The yield is 1.71 kg, and the yield is about 67%.
実施例 3
目皿10段の精留塔を有する8m″の反応器に水分0.
6%のジメチルホルムアミド4000kp、純度85%
、水分0.36%のシアン酸ナトリウム2000k19
、無水塩化カルシウム200kg、臭化カリウム10k
gを仕込み、攪拌しながら温度90〜95℃、圧力12
5 mvtHg、還流5でジメチルホルムアミド294
kgを留出させた。Example 3 An 8 m″ reactor with a rectification column with 10 perforated plates was heated to 0.0 m of water.
6% dimethylformamide 4000kp, purity 85%
, Sodium cyanate 2000k19 with a moisture content of 0.36%
, anhydrous calcium chloride 200kg, potassium bromide 10k
g, and while stirring, the temperature was 90-95℃ and the pressure was 12℃.
Dimethylformamide 294 at 5 mvtHg, reflux 5
kg was distilled out.
系内の残留水分は0.05%であった。The residual moisture in the system was 0.05%.
次いで温度を130℃に昇温し、塩化アルリル(CH2
=CHCH2C1)2050kyを2.5時間かかつて
加えた。Then, the temperature was raised to 130°C, and allyl chloride (CH2
=CHCH2C1) 2050ky was added for 2.5 hours.
その後1.5時間同温度に維持して冷却した。Thereafter, the temperature was maintained at the same temperature for 1.5 hours and cooled.
反応混合物を遠心分離し、固形物をジメチルホルムアミ
ドで洗浄し、涙液を合わせ減圧蒸留してジメチルホルム
アミドを回収した。The reaction mixture was centrifuged, the solids were washed with dimethylformamide, and the lachrymal fluids were combined and distilled under reduced pressure to recover dimethylformamide.
蒸留残渣にトルエンを加えて濾過後トルエンを留去し、
減圧蒸留(123〜b
ルリル2104kgを得た。Toluene is added to the distillation residue, and after filtration, the toluene is distilled off.
Vacuum distillation (123-b) 2104 kg of luril was obtained.
これは収率約94%(塩化アルリル基準)である。This is a yield of about 94% (based on allyl chloride).
比較例 3
ジメチルアミドを留去しないこと以外は、実施例3と同
様の方法にてイソシアヌル酸トリアルリルを得た。Comparative Example 3 Triallyl isocyanurate was obtained in the same manner as in Example 3 except that dimethylamide was not distilled off.
該収量は1455に9であり、収率は約65%である。The yield is 9 in 1455, which is about 65%.
実施例 4
攪拌機、温度計を付した11の反応器に水分0.5%の
テトラメチル尿素600f、純度98.5%、水分0.
2%のシアン酸カリウム85f?及びベンゼン30f?
を加え、攪拌しながら80′cK加熱し、単蒸留により
ベンゼン152を留去した。Example 4 In 11 reactors equipped with a stirrer and a thermometer, 600 f of tetramethylurea with a water content of 0.5%, a purity of 98.5%, and a water content of 0.
2% potassium cyanate 85f? and benzene 30f?
was added and heated to 80'cK with stirring, and 152 benzene was distilled off by simple distillation.
系内の残留水分は0,02%であった。The residual moisture in the system was 0.02%.
次いで臭化5ee−ブチル137rを加え、130℃に
昇温し、同温度で5時間反応した。Next, 5ee-butyl bromide 137r was added, the temperature was raised to 130°C, and the reaction was carried out at the same temperature for 5 hours.
冷却後、反応混合物を濾過し、モレキュラーシーブス−
4Aを用いて脱水したテトラメチル尿素で固形物を洗浄
し、p液を合わせて分留し、沸点100〜102℃のイ
ソシアン酸−5ee−ブチル72.3Pを得た。After cooling, the reaction mixture was filtered and washed with molecular sieves.
The solid matter was washed with tetramethylurea dehydrated using 4A, and the p liquid was combined and fractionated to obtain 72.3P of 5ee-butyl isocyanate having a boiling point of 100 to 102°C.
これは収率約73%(臭化−5ec−ブチル基準)であ
る。This is a yield of about 73% (based on 5ec-butyl bromide).
比較例 4
反応器内にベンゼンを加えず共沸蒸留による脱水操作を
行なわない以外は、実施例4と同様の方法にてイソシア
ン酸−5ec−ブチルを得た。Comparative Example 4 5ec-butyl isocyanate was obtained in the same manner as in Example 4, except that benzene was not added to the reactor and the dehydration operation by azeotropic distillation was not performed.
該収量は42.5?であり、収率は約43%である。The yield is 42.5? The yield is about 43%.
実施例 5
実施例4と同様の反応器に水分0.2%のジメチルスル
ホキシド500S’、純度94%、水分o、 1%のシ
アン酸ナトリウム100tを加え、攪拌しながら減圧下
85〜87℃/25wHgでジメチルスルホキシド10
0Lf?を留去した。Example 5 In a reactor similar to Example 4, 100 tons of dimethyl sulfoxide 500S' with a water content of 0.2%, a purity of 94%, a water content of o, and 1% sodium cyanate were added, and the mixture was heated at 85 to 87°C under reduced pressure with stirring. Dimethyl sulfoxide 10 at 25 wHg
0Lf? was removed.
系内の残留水分は0.01%であった。The residual moisture in the system was 0.01%.
次いで臭化−1−アミル151グを加え、700 mm
Hg減圧790℃で20時間反応した。Next, 151 g of 1-amyl bromide was added, and 700 mm
The reaction was carried out at 790° C. under reduced pressure of Hg for 20 hours.
冷却後、反応混合物を沢過し、固形物をモレキュラーシ
ーブス−4Aを用いて完全に脱水したジメチルスルホキ
シドで洗浄し、涙液を合わせて分留すると、沸点120
〜123℃のイソシアン酸−i−アミル72.3fが得
られた。After cooling, the reaction mixture was filtered, the solid was washed with dimethyl sulfoxide completely dehydrated using molecular sieves-4A, and the lachrymal fluid was combined and fractionated to give a boiling point of 120
72.3f of i-amyl isocyanate was obtained at ~123°C.
これは収率約64%(臭化−1−アミル基準)である。This is a yield of about 64% (based on 1-amyl bromide).
比較例 5
ジメチルスルホキシドを留去しないこと以外は、実施例
5と同様の方法にてイソシアン酸−1−アルミを得た。Comparative Example 5 1-Aluminum isocyanate was obtained in the same manner as in Example 5 except that dimethyl sulfoxide was not distilled off.
該収量は40.7?であり、収率は約36%である。The yield is 40.7? The yield is about 36%.
Claims (1)
物と、シアン酸アルカリとを反応させ、インシアヌル酸
エステルを製造するに当り、溶媒およ**びシアン酸ア
ルカリを反応器に仕込み、次いで脱水蒸留を行った後、
脂肪族ハロゲン化化合物を加えて反応させることを特徴
とするイソシアヌル酸エステルの製造法。1. To produce incyanuric acid ester by reacting an aliphatic... rogogenated compound with an alkali cyanate in an aprotic polar solvent, the solvent and the alkali cyanate are charged into a reactor, and then After dehydration and distillation,
A method for producing an isocyanuric acid ester, which comprises adding and reacting an aliphatic halogenated compound.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10962877A JPS5835515B2 (en) | 1977-09-12 | 1977-09-12 | Production method of isocyanuric acid ester |
| DE19782839084 DE2839084C2 (en) | 1977-09-12 | 1978-09-08 | Process for the preparation of tri-(allyl isocyanurate) |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10962877A JPS5835515B2 (en) | 1977-09-12 | 1977-09-12 | Production method of isocyanuric acid ester |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5444689A JPS5444689A (en) | 1979-04-09 |
| JPS5835515B2 true JPS5835515B2 (en) | 1983-08-03 |
Family
ID=14515093
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10962877A Expired JPS5835515B2 (en) | 1977-09-12 | 1977-09-12 | Production method of isocyanuric acid ester |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5835515B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014240393A (en) * | 2014-07-14 | 2014-12-25 | 日本化成株式会社 | Triallyl isocyanurate |
| JP2015134820A (en) * | 2015-04-16 | 2015-07-27 | 日本化成株式会社 | Triallyl isocyanurate |
| EP2899184A1 (en) | 2009-05-25 | 2015-07-29 | Nippon Kasei Chemical Co., Ltd. | Use of triallyl isocyanurate |
| JP2015166462A (en) * | 2015-04-16 | 2015-09-24 | 日本化成株式会社 | Crosslinking agent and sealant |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6128272B2 (en) * | 2016-09-08 | 2017-05-17 | 日本化成株式会社 | Crosslinker and sealant |
| WO2021020325A1 (en) * | 2019-07-30 | 2021-02-04 | マツモトファインケミカル株式会社 | Silicon isocyanate compound-containing composition and production method therefor |
-
1977
- 1977-09-12 JP JP10962877A patent/JPS5835515B2/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2899184A1 (en) | 2009-05-25 | 2015-07-29 | Nippon Kasei Chemical Co., Ltd. | Use of triallyl isocyanurate |
| JP2014240393A (en) * | 2014-07-14 | 2014-12-25 | 日本化成株式会社 | Triallyl isocyanurate |
| JP2015134820A (en) * | 2015-04-16 | 2015-07-27 | 日本化成株式会社 | Triallyl isocyanurate |
| JP2015166462A (en) * | 2015-04-16 | 2015-09-24 | 日本化成株式会社 | Crosslinking agent and sealant |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5444689A (en) | 1979-04-09 |
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