JPH0670103B2 - Method for producing polyisocyanate compound - Google Patents
Method for producing polyisocyanate compoundInfo
- Publication number
- JPH0670103B2 JPH0670103B2 JP63285743A JP28574388A JPH0670103B2 JP H0670103 B2 JPH0670103 B2 JP H0670103B2 JP 63285743 A JP63285743 A JP 63285743A JP 28574388 A JP28574388 A JP 28574388A JP H0670103 B2 JPH0670103 B2 JP H0670103B2
- Authority
- JP
- Japan
- Prior art keywords
- polyisocyanate compound
- reaction
- compound
- weight
- polyisocyanate
- 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.)
- Expired - Fee Related
Links
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- Compositions Of Macromolecular Compounds (AREA)
- Polyurethanes Or Polyureas (AREA)
- Paints Or Removers (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Macromonomer-Based Addition Polymer (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ポリイソシアネート化合物の製造方法に関す
る、 更に詳しくは、ポリイソシアネートとビニルポリマーと
からなるもので、特に塗料用として適したポリイソシア
ネート化合物の製造方法に関するものである。TECHNICAL FIELD The present invention relates to a method for producing a polyisocyanate compound, more specifically, a polyisocyanate compound composed of a polyisocyanate and a vinyl polymer, which is particularly suitable for paints. The present invention relates to a manufacturing method of.
ポリウレタン系塗料は、用途によって初期乾燥性が遅い
ため、その改良が要望され色々検討されてきた。例え
ば、ポリイソシアネート化合物に触媒を添加する方法
は、乾燥性を改良することは出来るが、貯蔵安定性が低
下し実用的ではない。また、ポリイソシアネート化合物
中にイソシアヌレート基を導入する方法は広く用いられ
ているが、初期乾燥性の改良については十分ではなかっ
た。Since the initial drying property of the polyurethane-based paint is slow depending on the application, improvement has been demanded and various studies have been made. For example, the method of adding a catalyst to the polyisocyanate compound can improve the drying property, but is not practical because the storage stability is lowered. Further, a method of introducing an isocyanurate group into a polyisocyanate compound is widely used, but improvement in initial drying property is not sufficient.
本発明者は、初期乾燥性を改良するために有機ポリイソ
シアネートについて種々検討した結果、有機ポリイソシ
アネートと1分子中に水酸基および不飽和基を有する化
合物との反応生成物にビニルモノマーを重合させて得ら
れるポリイソシアネート化合物の製造方法が優れた初期
乾燥性を有することを見出し、本発明に至った。The present inventor has conducted various studies on organic polyisocyanates in order to improve the initial drying property. As a result, a vinyl monomer is polymerized into a reaction product of the organic polyisocyanate and a compound having a hydroxyl group and an unsaturated group in one molecule. The inventors have found that the method for producing the obtained polyisocyanate compound has excellent initial drying property, and have reached the present invention.
即ち本発明は、 有機ポリイソシアネートと1分子中に水酸基及び不飽和
基を有する化合物とをNCO基/活性水素当量比3/1〜20/1
で、60℃〜150℃で1時間〜6時間反応させて得た反応
生成物(A)100重量部に対してビニールモノマー
(B)を10重量部〜200重量部を60℃〜150℃で30分間〜
5時間重合させることを特徴とするポリイソシアネート
化合物の製造方法である。本発明によるポリイソシアネ
ート化合物は、初期乾燥性を改良するほか、他成分、例
えばアクリルポリオール類との相溶性が良く、貯蔵安定
性も優れているという特徴がある。That is, in the present invention, an organic polyisocyanate and a compound having a hydroxyl group and an unsaturated group in one molecule are used in an NCO group / active hydrogen equivalent ratio of 3/1 to 20/1.
Then, 10 parts by weight to 200 parts by weight of the vinyl monomer (B) is added to 100 parts by weight of the reaction product (A) obtained by reacting at 60 ° C. to 150 ° C. for 1 to 6 hours at 60 ° C. to 150 ° C. in 30 minutes~
A method for producing a polyisocyanate compound, which comprises polymerizing for 5 hours. The polyisocyanate compound according to the present invention is characterized in that it has improved initial drying properties, good compatibility with other components such as acrylic polyols, and excellent storage stability.
本発明に用いられる有機ポリイソシアネートは、ポリウ
レタン塗料用に使われているイソシアネート類はすべて
使用することが出来る。例えば、トリレンジイソシアネ
ートとトリメチロールプロパンのアダクト体、トリレン
ジイソシアネートの三量体、ヘキサメチレンジイソシア
ネートとトリメチロールプロパンのアダクト体、ヘキサ
メチレンジイソシアネートの三量体、ポリイソシアネー
トとポリオールによるNCO基末端プレポリマーなどがあ
る。As the organic polyisocyanate used in the present invention, all the isocyanates used for polyurethane coatings can be used. For example, an adduct of tolylene diisocyanate and trimethylol propane, a trimer of tolylene diisocyanate, an adduct of hexamethylene diisocyanate and trimethylol propane, a trimer of hexamethylene diisocyanate, an NCO group-terminated prepolymer with polyisocyanate and a polyol. and so on.
本発明に用いられる1分子中に水酸基及び不飽和基を有
する化合物(以下水酸基含有不飽和化合物と略す)は、
例えば、2−ヒドロキシエチルメタアクリレート、アリ
ルアルコール、オレイルアルコール、エチレングリコー
ルマレエートなどである。これらは1分子中に1個以上
の水酸基と1個以上の不飽和基を有する化合物である。The compound having a hydroxyl group and an unsaturated group in one molecule used in the present invention (hereinafter abbreviated as a hydroxyl group-containing unsaturated compound) is
For example, 2-hydroxyethyl methacrylate, allyl alcohol, oleyl alcohol, ethylene glycol maleate and the like. These are compounds having one or more hydroxyl groups and one or more unsaturated groups in one molecule.
本発明の有機ポリイソシアネートと水酸基含有不飽和化
合物との反応は、NCO基/活性水素当量比3/1〜20/1で、
反応温度30〜120℃、反応時間1〜6時間の条件で行う
ことができる。当量比は、両者の分子量、官能基数など
によって選択することができる。この場合、当量比が3/
1未満では、塗膜にした場合強靭性が不十分となり好ま
しくない。また、20/1を越えると、得られたポリイソシ
アネート化合物中のビニルポリマーが分離する可能性が
大きくなるので好ましくない。The reaction between the organic polyisocyanate of the present invention and the hydroxyl group-containing unsaturated compound is carried out at an NCO group / active hydrogen equivalent ratio of 3/1 to 20/1,
The reaction can be performed under the conditions of a reaction temperature of 30 to 120 ° C. and a reaction time of 1 to 6 hours. The equivalence ratio can be selected according to the molecular weight of the both and the number of functional groups. In this case, the equivalence ratio is 3 /
If it is less than 1, the toughness is insufficient when formed into a coating film, which is not preferable. On the other hand, when it exceeds 20/1, the vinyl polymer in the obtained polyisocyanate compound is more likely to be separated, which is not preferable.
本発明に用いられるビニルモノマーは、例えばメチルメ
タアクリレート、メチルアクリレート、ブチルメタアク
リレート、アクリロニトリル、スチレン、無水マレイン
酸、N−ビニル−2−ピロリドンなどである。これらは
単独で、あるいは2種以上の混合物で使用することがで
きる。The vinyl monomer used in the present invention is, for example, methyl methacrylate, methyl acrylate, butyl methacrylate, acrylonitrile, styrene, maleic anhydride, N-vinyl-2-pyrrolidone or the like. These can be used alone or as a mixture of two or more kinds.
本発明の有機ポリイソシアネートと水酸基含有不飽和化
合物の反応生成物(A)とビニルモノマー(B)の配合
比率は、(A)100重量部に対し、(B)10〜200重量部
である。これらAとBの重合は、通常のビニル重合の反
応と同様に行なうことが出来る。重合に際して、一般に
使われる溶媒を使用することが出来る。溶媒としては、
例えば酢酸ブチル、トルエン、キシレンなどを用いるこ
とが出来る。この反応条件は、反応温度60〜150℃で反
応時間30分〜5時間で行うことができる。この場合、反
応生成物(A)100重量部に対してビニルモノマーが10
重量部未満の場合、ポリイソシアネート組成物中に占め
るビニルポリマーの割合がすくなくて、塗膜の初期乾燥
性を改良することが出来ない。また、ビニルモノマーが
200重量部を超えると、ポリイソシアネート化合物の粘
度が高くなり、作業性を悪化させたり、また、塗膜中の
ポリウレタンの占める割合が低くなり、ポリウレタンの
もつ特徴が発揮されなくなるので好ましくない。The blending ratio of the reaction product (A) of the organic polyisocyanate of the present invention and the hydroxyl group-containing unsaturated compound and the vinyl monomer (B) is 10 to 200 parts by weight of (B) with respect to 100 parts by weight of (A). The polymerization of these A and B can be carried out in the same manner as the ordinary vinyl polymerization reaction. In the polymerization, commonly used solvents can be used. As a solvent,
For example, butyl acetate, toluene, xylene and the like can be used. This reaction condition can be carried out at a reaction temperature of 60 to 150 ° C. and a reaction time of 30 minutes to 5 hours. In this case, 10 parts by weight of the reaction product (A) was used to add 10 parts of vinyl monomer.
When the amount is less than the amount by weight, the proportion of the vinyl polymer in the polyisocyanate composition is too small to improve the initial drying property of the coating film. Also, vinyl monomer
If it exceeds 200 parts by weight, the viscosity of the polyisocyanate compound becomes high, the workability is deteriorated, and the proportion of polyurethane in the coating film becomes low, so that the characteristics of polyurethane are not exhibited, which is not preferable.
本発明のポリイソシアネート化合物の製造方法は、ポリ
イソシアネート化合物と水酸基含有不飽和化合物による
ウレタン化反応を行ない、その後、ビニルモノマーを添
加して重合を行なう方法が好ましい。別の方法として
は、有機ポリイソシアネートと水酸基含有不飽和化合物
の混合物にビニルモノマーを添加して、ウレタン化反応
とビニル重合を同時に行なうことも出来る。また、水酸
基含有不飽和化合物にビニルモノマーを添加しビニル重
合を先に行ない、後から有機ポリイソシアネートを添加
してウレタン化反応を行なうことも出来る。本発明のポ
リイソシアネート化合物には、通常使われている全ての
添加剤を混合することが出来る。例えば、酸化防止剤、
紫外線吸収剤、顔料、充填剤、可塑剤、防黴剤、改質剤
などである。The method for producing the polyisocyanate compound of the present invention is preferably a method in which the polyisocyanate compound and a hydroxyl group-containing unsaturated compound are subjected to a urethanization reaction, and then a vinyl monomer is added to carry out polymerization. As another method, a vinyl monomer may be added to a mixture of an organic polyisocyanate and a hydroxyl group-containing unsaturated compound to carry out the urethanization reaction and the vinyl polymerization at the same time. It is also possible to add a vinyl monomer to the hydroxyl group-containing unsaturated compound to carry out vinyl polymerization first, and then add an organic polyisocyanate to carry out the urethanization reaction. All the commonly used additives can be mixed with the polyisocyanate compound of the present invention. For example, antioxidants,
Examples include UV absorbers, pigments, fillers, plasticizers, antifungal agents, and modifiers.
本発明の樹脂は、塗料用だけでなく、接着剤、インキバ
インダーなどに使用することもできる。The resin of the present invention can be used not only for paints but also for adhesives, ink binders and the like.
次に本発明について実施例により、更に詳しく説明す
る。尚、実施例における「部」及び「%」は断りのない
限り「重量部」及び「重量%」を表わす。Next, the present invention will be described in more detail with reference to examples. In the examples, "parts" and "%" represent "parts by weight" and "% by weight" unless otherwise specified.
実施例 1. 撹拌機、冷却器、滴化ロート、温度計をつけた500mlの
四っ口フラスコに、ヘキサメチレンジイソシアネートの
三量体(日本ポリウレタン工業製、コロネートEH)NCO
含量21.3%、111.7g、2−ハイドロキシエチルメタアク
リレート1.4g、酢酸ブチル59.8gを計りとり、窒素ガス
を流しながら加熱混合する。80℃で1時間反応させて反
応生成物(A)を得た。これにビニルモノマー(B)成
分としてメチルメタアクリレート26.5gとパーキュアO
(日本油脂製、脂肪族系過酸化物触媒、ジメチルフタレ
ート50%溶液)0.6gの混合物を90℃で15分かけて滴下す
る。滴下終了後110℃で1時間30分加熱して反応終了と
した。このポリイソシアネート化合物は、NCO含量12.0
%、不揮発分69.4%、粘度3100cP/25℃であった。この
ポリイソシアネート樹脂4.6gアクリデックA−801(大
日本インキ工業製のアクリルポリオール、水酸基価50mg
KOH/g、不揮発分50g)13.5g、および酢酸ブチル1.8gを
ビーカーに計りとり、混合して塗料配合液をえた。この
配合液を25℃の雰囲気中でガラス板上に70μmの厚さで
塗布した。指触媒乾燥時間を測定した結果12分であっ
た。Example 1. In a 500 ml four-necked flask equipped with a stirrer, a condenser, a dropping funnel, and a thermometer, hexamethylene diisocyanate trimer (Nippon Polyurethane Industry Co., Ltd., Coronate EH) NCO
The content of 21.3%, 111.7 g, 1.4 g of 2-hydroxyethyl methacrylate and 59.8 g of butyl acetate are weighed and mixed by heating while flowing nitrogen gas. Reaction was carried out at 80 ° C. for 1 hour to obtain a reaction product (A). To this, 26.5 g of methyl methacrylate and Percure O as vinyl monomer (B) components
(Nippon Oil and Fats Co., Ltd., aliphatic peroxide catalyst, dimethyl phthalate 50% solution) A mixture of 0.6 g is added dropwise at 90 ° C. over 15 minutes. After completion of dropping, the reaction was completed by heating at 110 ° C. for 1 hour and 30 minutes. This polyisocyanate compound has an NCO content of 12.0.
%, Nonvolatile content 69.4%, viscosity 3100 cP / 25 ° C. 4.6 g of this polyisocyanate resin Acrydec A-801 (acrylic polyol manufactured by Dainippon Ink and Chemicals, hydroxyl value 50 mg
KOH / g, non-volatile content 50 g) 13.5 g, and butyl acetate 1.8 g were weighed in a beaker and mixed to obtain a coating composition liquid. This compounded solution was applied on a glass plate in an atmosphere of 25 ° C. to a thickness of 70 μm. As a result of measuring the finger catalyst drying time, it was 12 minutes.
比較例 1. ヘキサメチレンジイソシアネートの三量体(実施例.1と
同じ)を用いて塗料配合液を調整した。アクリデックA
−801 14.4g、コロネートEH2.8gおよび酢酸ブチル2.8g
をビーカーに計りとり混合した。この配合液を25℃の雰
囲気中でガラス板上に70μmの厚さで塗布した。指触乾
燥時間を測定した結果、16分であった。Comparative Example 1. A coating solution was prepared using a trimer of hexamethylene diisocyanate (same as in Example 1). Acrydeck A
-801 14.4g, Coronate EH 2.8g and Butyl acetate 2.8g
Were weighed into a beaker and mixed. This compounded solution was applied on a glass plate in an atmosphere of 25 ° C. to a thickness of 70 μm. As a result of measuring the touch dry time, it was 16 minutes.
実施例 2. 実施例1.と同じ装置を付けたフラスコに、ヘキサメチレ
ンジイソシアネートの三量体(実施例.1と同じ)111.7
g、2−ハイドロキシエチルメタアクリレート1.4g、酢
酸ブチル59.8gを計りとり、窒素ガスを流しながら加熱
混合する。80℃で1時間反応させて反応生成物(A)を
得た。これにスチレン26.5gとパーキュアO0.6gの混合物
を90℃で15分かけて滴下する。滴下終了後110℃1時間3
0分加熱して反応終了とした。反応生成物を200メッシュ
金網を用いてろ過して、NCO含有12.1%、不揮発分68.9
%、粘度1700cP/25℃のポリイソシアネート化合物を得
た。このポリイソシアネート化合物4.6g、アクリデック
A−801 13.5gおよび酢酸ブチル1.8gをビーカーに計り
とり、混合して塗料配合液をえた。この配合液を25℃の
雰囲気中でガラス板上に7μmの厚さで塗布し、指触乾
燥時間を測定した結果、13分であった。Example 2. In a flask equipped with the same equipment as in Example 1, hexamethylene diisocyanate trimer (same as Example 1) 111.7
g, 1.4 g of 2-hydroxyethyl methacrylate and 59.8 g of butyl acetate are weighed and mixed by heating while flowing a nitrogen gas. Reaction was carried out at 80 ° C. for 1 hour to obtain a reaction product (A). To this, a mixture of 26.5 g of styrene and 0.6 g of Percure O was added dropwise at 90 ° C over 15 minutes. 110 ° C for 1 hour after completion of dropping 3
The reaction was completed by heating for 0 minutes. The reaction product was filtered using a 200-mesh wire net, NCO content 12.1%, non-volatile content 68.9
%, A polyisocyanate compound having a viscosity of 1700 cP / 25 ° C. was obtained. 4.6 g of this polyisocyanate compound, 13.5 g of Acrydec A-801 and 1.8 g of butyl acetate were weighed in a beaker and mixed to obtain a coating composition liquid. This compounded solution was applied onto a glass plate at a thickness of 7 μm in an atmosphere of 25 ° C., and the touch-drying time was measured, and the result was 13 minutes.
実施例 3. 実施例.1と同じ装置を付けたフラスコに、トリレンジイ
ソシアネートのトリメチロールプロパンアダクト体(日
本ポリウレタン工業製、コロネートL)NCO含量13.0
%、119.7g、2−ハイドロキシエチルメタクリレート1.
5g、酢酸ブチル49.8gを計りとり、窒素ガスを流しなが
ら加熱混合する。60℃で1時間30分反応させて反応生成
物(A)を得た。これにメチルメタアクリレート28.4g
とバーキュアO0.6gの混合物を80℃で30分かけて滴下す
る。滴下終了後90℃1時間加熱して反応終了とした。こ
のポリイソシアネート化合物はNCO含量8.0%、不揮発分
55.8%、粘度45cP/25℃であった。このポリイソシアネ
ート化合物6.7g、アクリデックA−801 13.5gをビーカ
ーに計りとり、混合して塗料配合液をえた。この配合液
を25℃の雰囲気中でガラス板上に70μmの厚さで塗布
し、指触乾燥時間を測定した結果、6分であった。Example 3. A trimethylolpropane adduct of tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., Coronate L) with an NCO content of 13.0 was placed in a flask equipped with the same equipment as in Example 1.
%, 119.7 g, 2-hydroxyethyl methacrylate 1.
Weigh 5 g and 49.8 g of butyl acetate, and mix with heating while flowing nitrogen gas. The reaction product (A) was obtained by reacting at 60 ° C. for 1 hour and 30 minutes. 28.4g of methyl methacrylate
And 0.6 g of Vercure O are added dropwise at 80 ° C. over 30 minutes. After completion of the dropping, the reaction was completed by heating at 90 ° C. for 1 hour. This polyisocyanate compound has an NCO content of 8.0% and a nonvolatile content.
The viscosity was 55.8% and the viscosity was 45 cP / 25 ° C. 6.7 g of this polyisocyanate compound and 13.5 g of Acrydeck A-801 were weighed in a beaker and mixed to obtain a coating composition liquid. This compounded solution was applied onto a glass plate at a thickness of 70 μm in an atmosphere of 25 ° C., and the touch-drying time was measured, and the result was 6 minutes.
比較例 2. トリレンジイソシアネートのトリメチロールプロパンア
ダクト体(実施例.3と同じ)を用いて塗料配合液を調整
した。アクリデックA−801 13.6g、コロネートL4.3g
および酢酸ブチル2.1gをビーカーに計りとり混合した。
この配合液を25℃の雰囲気中てガラス板上に70μmの厚
さで塗布し、指触乾燥時間を測定した結果10分であっ
た。Comparative Example 2. A trimethylolpropane adduct of tolylene diisocyanate (same as in Example 3) was used to prepare a coating composition liquid. Acrydec A-801 13.6g, Coronate L4.3g
And 2.1 g of butyl acetate were weighed in a beaker and mixed.
This compounded solution was applied onto a glass plate at a thickness of 70 μm in an atmosphere of 25 ° C., and the touch-drying time was measured, and it was 10 minutes.
本発明のポリイソシアネート化合物は、湿気硬化型塗
料、2液混合型塗料用などの原料として使用すると初期
乾燥性を改良すことができ、色々な分野の塗料に用いる
ことが出来る。例えば、木工用塗料、プラスチック用塗
料、金属用塗料などに使用することが出来る。The polyisocyanate compound of the present invention can improve the initial drying property when used as a raw material for a moisture-curable coating material, a two-component mixed coating material, etc., and can be used for coating materials in various fields. For example, it can be used as a paint for woodwork, a paint for plastics, a paint for metals, and the like.
Claims (1)
基及び不飽和基を有する化合物とをNCO基/活性水素当
量比3/1〜20/1で、60℃〜150℃で1時間〜6時間反応さ
せて得た反応生成物(A)100重量部に対してビニール
モノマー(B)を10重量部〜200重量部を60℃〜150℃で
30分間〜5時間重合させることを特徴とするポシイソシ
アネート化合物の製造方法。1. An organic polyisocyanate and a compound having a hydroxyl group and an unsaturated group in one molecule at an NCO group / active hydrogen equivalent ratio of 3/1 to 20/1 at 60 ° C. to 150 ° C. for 1 hour to 6 hours. 100 parts by weight of the reaction product (A) obtained by the reaction, 10 parts by weight to 200 parts by weight of the vinyl monomer (B) at 60 ° C to 150 ° C
A method for producing a poisocyanate compound, comprising polymerizing for 30 minutes to 5 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63285743A JPH0670103B2 (en) | 1988-11-14 | 1988-11-14 | Method for producing polyisocyanate compound |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63285743A JPH0670103B2 (en) | 1988-11-14 | 1988-11-14 | Method for producing polyisocyanate compound |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02133418A JPH02133418A (en) | 1990-05-22 |
| JPH0670103B2 true JPH0670103B2 (en) | 1994-09-07 |
Family
ID=17695475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63285743A Expired - Fee Related JPH0670103B2 (en) | 1988-11-14 | 1988-11-14 | Method for producing polyisocyanate compound |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0670103B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101432291B1 (en) * | 2005-11-10 | 2014-08-21 | 바이엘 머티리얼사이언스 아게 | A hydrophilic polyisocyanate mixture |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102004056849A1 (en) * | 2004-11-25 | 2006-06-08 | Bayer Materialscience Ag | New polyisocyanate mixtures, a process for their preparation and their use as hardener component in polyurethane coatings |
| JP6067235B2 (en) * | 2012-03-06 | 2017-01-25 | 第一工業製薬株式会社 | Urethane (meth) acrylate and curable resin composition containing the same |
| JP7331505B2 (en) * | 2019-07-04 | 2023-08-23 | 三菱ケミカル株式会社 | Adhesive layer, adhesive sheet and laminate |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6043364A (en) * | 1983-08-22 | 1985-03-07 | 丹平製薬株式会社 | Nutrient food |
| JPS6125749A (en) * | 1984-07-13 | 1986-02-04 | Yamazaki Mazak Corp | Determination of machining sequence in machining center |
-
1988
- 1988-11-14 JP JP63285743A patent/JPH0670103B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101432291B1 (en) * | 2005-11-10 | 2014-08-21 | 바이엘 머티리얼사이언스 아게 | A hydrophilic polyisocyanate mixture |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02133418A (en) | 1990-05-22 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |