JPH05170748A - Production of polyisocyanate containing isocyanurate group - Google Patents

Production of polyisocyanate containing isocyanurate group

Info

Publication number
JPH05170748A
JPH05170748A JP3340910A JP34091091A JPH05170748A JP H05170748 A JPH05170748 A JP H05170748A JP 3340910 A JP3340910 A JP 3340910A JP 34091091 A JP34091091 A JP 34091091A JP H05170748 A JPH05170748 A JP H05170748A
Authority
JP
Japan
Prior art keywords
reaction
diisocyanate
phosphate
polyisocyanate
isocyanate
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.)
Granted
Application number
JP3340910A
Other languages
Japanese (ja)
Other versions
JP3111103B2 (en
Inventor
Yukiya Saho
幸也 佐保
Junichi Oguma
淳一 小熊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP03340910A priority Critical patent/JP3111103B2/en
Publication of JPH05170748A publication Critical patent/JPH05170748A/en
Application granted granted Critical
Publication of JP3111103B2 publication Critical patent/JP3111103B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Abstract

PURPOSE:To obtain the subject compound which generates no floating matter and causes no turbidness on dilution with a solvent by effecting trimerization reaction of a diisocyanate monomer and an isocyanate compound and terminating the reaction with a poisoned catalyst. CONSTITUTION:In the presence of a tertiary amine or a quaternary ammonium salt such as tetramethylammonium caprate, trimerization reaction is carried out between a diisocyanate monomer and a part of the isocyanate group in at least one isocyanate compound selected from the preliminarily urethanized product from a diisocyanate monomer and mono- to trifunctional alcohol. Then, an acidic phosphoric acid ester containing alkoxy groups is used as a catalytic poison to stop the reaction and obtain the subject compound. The polyisocyanate having an isocyanurate ring in the molecule has excellent resistance to weather, heat, chemicals and so forth and is useful as a starting substance for coating, adhesive, elastomer, artificial leather, foam or the like.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、イソシアヌレート基含
有ポリイソシアネートの製法に関する、さらに詳しく
は、溶剤溶解性の良好なイソシアヌレート環を有するポ
リイソシアネートの製法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a process for producing an isocyanurate group-containing polyisocyanate, and more particularly to a process for producing a polyisocyanate having an isocyanurate ring having good solvent solubility.

【0002】[0002]

【従来の技術】分子内にイソシアヌレート環を有するポ
リイソシアネートは、耐候性、耐熱性、耐薬品性などに
優れ、塗料、接着剤、エラストマー、人工皮革、フォー
ムなどのポリウレタンの原料として利用される。製法と
しては触媒の存在下に、単量体ジイソシアネートを三量
化し、塩酸、燐酸、硫酸、ジクロロ酢酸、トリクロロ酢
酸、ベンソイルクロライド、アセチルクロライド、ベン
ゼンスルホン酸等の酸性物質により反応を停止する方法
が知られている。(例えば、特開平3ー93825号、
特開平2ー258771号、特開平2ー107337
号、特開平2ー11554号、特開平2ー3682号、
特開平2ー250872号、特開平2ー32068号、
特開平2ー6454号、特開平1ー297420号、特
開平1ー149821号、特開昭63ー57577号、
特開昭61ー129173号、特開昭61ー11137
1号、特開昭60ー181114号公報)。
2. Description of the Related Art Polyisocyanates having an isocyanurate ring in the molecule have excellent weather resistance, heat resistance and chemical resistance and are used as raw materials for polyurethanes such as paints, adhesives, elastomers, artificial leather and foams. .. As a production method, a method in which monomer diisocyanate is trimerized in the presence of a catalyst and the reaction is stopped by an acidic substance such as hydrochloric acid, phosphoric acid, sulfuric acid, dichloroacetic acid, trichloroacetic acid, benzoyl chloride, acetyl chloride or benzenesulfonic acid. It has been known. (For example, JP-A-3-93825,
JP-A-2-258771, JP-A-2-107337
No. 2, Japanese Patent Application Laid-Open No. 2-11554, Japanese Patent Application Laid-Open No. 2-3682,
JP-A-2-250872, JP-A-2-32068,
JP-A No. 2-6454, JP-A No. 1-297420, JP-A No. 1-149821, and JP-A No. 63-57577,
JP 61-129173 A, JP 61-11137 A
No. 1, JP-A-60-181114).

【0003】ところが、従来の触媒被毒物質には浮遊物
が触媒被毒物質添加時に発生したり、製品が着色すると
いった欠点がある。リン酸、ジクロロ酢酸を用いた場合
には添加時に浮遊物が生じ、ろ過工程が必要となり、ベ
ンゼンスルホン酸を用いた場合には製品が着色する。さ
らに、近年、プラスチックレンズ等の光学材料の原料に
も利用されるようになり、溶剤で希釈した際の濁りが問
題となっている。特開平2−6480号公報では、リン
酸ジブチル等のアルキル基、アリール基、アリールアル
キル基含有酸性リン酸エステルを触媒被毒物質に使うこ
とが提唱されているが、浮遊物の発生については効果が
認められるものの、製品を溶剤で希釈した場合の濁りに
ついては十分な解決策とはなっていない。さらに、特開
平2ー42068号公報には溶剤希釈時に濁りの発生し
ない製法として、ケイ酸塩を添加し触媒を吸着する製法
が提唱されているが、触媒を吸着したケイ酸塩をろ過す
る必要がある。
However, the conventional catalyst poisoning substances have drawbacks such that suspended matter is generated when the catalyst poisoning substance is added and the product is colored. When phosphoric acid or dichloroacetic acid is used, a floating substance is generated at the time of addition and a filtration step is required, and when benzenesulfonic acid is used, the product is colored. Further, in recent years, it has also been used as a raw material for optical materials such as plastic lenses, and turbidity when diluted with a solvent has become a problem. Japanese Patent Application Laid-Open No. 2-6480 proposes to use an acidic phosphoric acid ester containing an alkyl group, an aryl group, or an arylalkyl group, such as dibutyl phosphate, as a catalyst poisoning substance, but it is effective in generating suspended matter. However, it is not a sufficient solution for turbidity when the product is diluted with a solvent. Further, Japanese Patent Application Laid-Open No. 2-42068 proposes a manufacturing method in which a silicate is added to adsorb a catalyst as a manufacturing method in which turbidity does not occur when a solvent is diluted, but it is necessary to filter the silicate adsorbing the catalyst. There is.

【0004】[0004]

【発明が解決しようとする課題】本発明の課題は、浮遊
物の発生がなく、溶剤で希釈時に濁りの発生しないイソ
シアヌレート環を有するポリイソシアネートを提供する
ことを目的とするものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a polyisocyanate having an isocyanurate ring that does not generate suspended solids and does not cause turbidity when diluted with a solvent.

【0005】[0005]

【課題を解決するための手段】本発明者等は、鋭意研究
検討を重ねた結果、アルコキシ基含有酸性燐酸エステル
を触媒被毒物質として用いることにより、前記課題を解
決する方法を見出し本発明に至った。即ち本発明は、第
三級アミンまたは第四級アンモニウム塩の存在下に、単
量体ジイソシアネート、及び、単量体ジイソシアネート
と1〜3官能性のアルコールとの予備ウレタン化反応物
から選ばれた、少なくとも1種のイソシアネート化合物
のイソシアネート基の一部の三量化反応を行い、触媒被
毒物質により反応を停止することからなる、イソシアヌ
レート基含有ポリイソシアネートの製法において、アル
コキシ基含有酸性燐酸エステルを触媒被毒物質として使
用することを特徴とする、イソシアヌレート基含有ポリ
イソシアネートの製法である。
As a result of intensive studies and studies, the present inventors have found a method for solving the above problems by using an alkoxy group-containing acidic phosphoric acid ester as a catalyst poisoning substance, and found the present invention. I arrived. That is, the present invention is selected from a monomer diisocyanate and a pre-urethanization reaction product of the monomer diisocyanate and a 1 to 3 functional alcohol in the presence of a tertiary amine or a quaternary ammonium salt. In a process for producing an isocyanurate group-containing polyisocyanate, which comprises performing a trimerization reaction of a part of an isocyanate group of at least one isocyanate compound and stopping the reaction by a catalyst poisoning substance, an alkoxy group-containing acidic phosphate ester A method for producing an isocyanurate group-containing polyisocyanate, which is characterized in that it is used as a catalyst poisoning substance.

【0006】本発明に用いるイソシアネート化合物は、
脂肪族イソシアネート、芳香族イソシアネート等の単量
体ジイソシアネート、および、これら単量体ジイソシア
ネートと1〜3官能性のアルコールとの予備ウレタン化
反応物である。脂肪族ジイソシアネートの例は、ヘキサ
メチレンジイソシアネート(HDI)、イソホロンジイ
ソシアネート(IPDI)、ジシクロヘキシルメタンジ
イソシアネート(水添MDI)、水添キシリレンジイソ
シアネート(水添XDI)及び2,4,4(または2,
2,4)ートリメチルヘキサメチレンジイソシアネート
(TMDI)である。芳香族ジイソシアネートの例は、
トリレンジイソシアネート(TDI)、ジフェニルメタ
ンジイソシアネート(MDI)、トルイジンジイソシア
ネート(TODI)、キシリレンジイソシアネート(X
DI)及びナフタレンジイソシアネート(NDI)であ
る。
The isocyanate compound used in the present invention is
It is a monomer diisocyanate such as an aliphatic isocyanate and an aromatic isocyanate, and a pre-urethanization reaction product of these monomer diisocyanates and a 1 to 3 functional alcohol. Examples of aliphatic diisocyanates are hexamethylene diisocyanate (HDI), isophorone diisocyanate (IPDI), dicyclohexylmethane diisocyanate (hydrogenated MDI), hydrogenated xylylene diisocyanate (hydrogenated XDI) and 2,4,4 (or 2,
2,4) -trimethylhexamethylene diisocyanate (TMDI). Examples of aromatic diisocyanates are:
Tolylene diisocyanate (TDI), diphenylmethane diisocyanate (MDI), toluidine diisocyanate (TODI), xylylene diisocyanate (X
DI) and naphthalene diisocyanate (NDI).

【0007】これら単量体ジイソシアネートは、最終製
品の使用目的に応じ任意に選択されるが、特に非黄変性
が要求される場合には脂肪族ジイソシアネートが好まし
い。1〜3官能性のアルコールとしては、例えば、メタ
ノール、エタノール、イソプロパノール等の低級脂肪族
一価アルコールのほか、エチレングリコール、プリピレ
ングリコール、ブタンジオール、グリセリン、1,2,
6ーヘキサントリオール等の低級脂肪族多価アルコー
ル、及び分子量約200〜10000のポリエステルポ
リオール、ポリエーテルポリオール等である。
These monomeric diisocyanates are arbitrarily selected according to the intended use of the final product, but aliphatic diisocyanates are preferred especially when non-yellowing is required. Examples of the monofunctional to trifunctional alcohols include lower aliphatic monohydric alcohols such as methanol, ethanol and isopropanol, as well as ethylene glycol, prepylene glycol, butanediol, glycerin, 1, 2,
Examples include lower aliphatic polyhydric alcohols such as 6-hexanetriol, polyester polyols and polyether polyols having a molecular weight of about 200 to 10,000.

【0008】三量化反応を行うイソシアネート化合物
は、前記例示の少なくとも二種以上のイソシアネート化
合物からなる混合物であっても良い。三量化反応で触媒
として用いる第三級アミン、第四級アンモニウム塩は公
知のいずれのものであってもよい。第三級アミンの例
は、ジアルキルアミノアルキルフェノール、トリアルキ
ルアミン、テトラアルキルアルキレンジアミンである。
第四アンモニウム塩の例は、テトラメチルアンモニウム
ヒドロキシド、トリメチルー2ーヒドロキシエチルアン
モニウムヒドロキシド、テトラメチルアンモニウム・カ
プリエートである。触媒濃度は、使用する触媒の種類及
び反応温度により異なるが、通常、単量体ジイソシアネ
ートに対して、10ppm 〜1%の範囲から選択される。
The isocyanate compound for the trimerization reaction may be a mixture of at least two kinds of the above-exemplified isocyanate compounds. Any known tertiary amine or quaternary ammonium salt may be used as a catalyst in the trimerization reaction. Examples of tertiary amines are dialkylaminoalkylphenols, trialkylamines, tetraalkylalkylenediamines.
Examples of quaternary ammonium salts are tetramethylammonium hydroxide, trimethyl-2-hydroxyethylammonium hydroxide, tetramethylammonium capryate. The catalyst concentration varies depending on the type of catalyst used and the reaction temperature, but is usually selected from the range of 10 ppm to 1% with respect to the monomer diisocyanate.

【0009】触媒については,例えば、特開平3ー93
825号、特開平2ー250872号、特開平2ー32
068号、特開平2ー6454号、特開平1ー2974
20号、特開平ー149821号、特開昭63ー575
77号、特開昭61ー129173号、特開昭61ー1
11371号、特開昭60ー181114号公報などに
記載されている。
Regarding the catalyst, for example, JP-A-3-93
825, JP-A-2-250872, JP-A-2-32
068, JP-A No. 2-6454, and JP-A No. 1-2974.
No. 20, JP-A-149821, JP-A-63-575.
77, JP 61-129173 A, JP 61-1 A.
11371, JP-A-60-181114, etc.

【0010】触媒被毒物質としては、アルコキシ基含有
酸性燐酸エステルを用いる。アルコキシ基含有酸性燐酸
エステルは、化1に示す化合物である。
An alkoxy group-containing acidic phosphoric acid ester is used as the catalyst poisoning substance. The alkoxy group-containing acidic phosphoric acid ester is the compound shown in Chemical formula 1.

【0011】[0011]

【化1】 [Chemical 1]

【0012】アルコキシ基含有酸性燐酸エステルの例
は、メトキシメチルホスフェート、ジメトキシメチルホ
スフェート、エトキシメチルホスフェート、ジエトキシ
メチルホスフェート、プロポキシメチルホスフェート、
ジプロポキシメチルホスフェート、ブトキシメチルホス
フェート、ジブトキシメチルホスフェート、ブトキシエ
チルホスフェート、ジブトキシエチルホスフェートであ
る。
Examples of the alkoxy group-containing acidic phosphoric acid ester include methoxymethyl phosphate, dimethoxymethyl phosphate, ethoxymethyl phosphate, diethoxymethyl phosphate, propoxymethyl phosphate,
These are dipropoxymethyl phosphate, butoxymethyl phosphate, dibutoxymethyl phosphate, butoxyethyl phosphate, dibutoxyethyl phosphate.

【0013】触媒被毒物質の使用量は、触媒1当量あた
り、好ましくは、0.4〜10当量さらに好ましくは
0.6〜5当量である。反応は、溶剤を用いても、用い
なくてもよい。溶剤を用いる際には当然、イソシアネー
ト基に対して反応活性を持たない溶剤を選択すべきであ
る。反応温度は、通常20〜160℃、好ましくは40
〜120℃の範囲から選ばれる。
The amount of the catalyst poisoning substance used is preferably 0.4 to 10 equivalents, more preferably 0.6 to 5 equivalents, per equivalent of the catalyst. The reaction may or may not use a solvent. When using a solvent, it is of course necessary to select a solvent having no reaction activity with respect to isocyanate groups. The reaction temperature is usually 20 to 160 ° C., preferably 40.
It is selected from the range of 120 ° C.

【0014】反応の進行は、反応液のNCO%測定、赤
外分光測定、屈折率測定等で追跡することができる。イ
ソシヌレートへの転化反応が進み過ぎると、三量化と共
に五量化、七量化が部分的に生じ生成物の粘度が上昇す
るため、反応は、イソシアネート化合物の転化率が5〜
70%、好ましくは10〜60%に達するまで行うのが
好ましい。
The progress of the reaction can be traced by NCO% measurement of the reaction solution, infrared spectroscopy measurement, refractive index measurement and the like. If the conversion reaction to isocyanurate proceeds too much, pentamerization and heptamerization partially occur together with trimerization to increase the viscosity of the product.
It is preferable to carry out until it reaches 70%, preferably 10 to 60%.

【0015】反応を停止した後、過剰の単量体ジイソシ
アネートおよび溶剤を除去して製品を得る。この単量体
ジイソシアネートおよび溶剤の除去は、例えば、薄膜蒸
留法や溶剤抽出法により行われる。
After stopping the reaction, excess monomeric diisocyanate and solvent are removed to obtain a product. The removal of the monomer diisocyanate and the solvent is performed by, for example, a thin film distillation method or a solvent extraction method.

【0016】[0016]

【実施例】以下に実施例を挙げて本発明をさらに具体的
に説明する。しかし、本発明はこれらに制限されるもの
でない。なお、実施例における評価は以下に示す方法で
行った。 浮遊物の有無:目視により観察 溶剤希釈時の濁り:酢酸エチルに固形分30%になるよ
うに希釈後、紫外可視分光光度計(島津製作所、UV−
160にて酢酸エチルをリファレンスとする波長550
nm、測光長20mmでの吸光度を測定。
EXAMPLES The present invention will be described in more detail with reference to the following examples. However, the present invention is not limited to these. The evaluation in the examples was carried out by the method described below. Presence or absence of suspended matter: Visual observation Turbidity when diluted with solvent: Ultraviolet-visible spectrophotometer (Shimadzu Corporation, UV-
Wavelength 550 with ethyl acetate as reference at 160
Measure the absorbance at nm and photometric length of 20 mm.

【0017】[0017]

【実施例1】温度計、撹はん機、窒素シール管を備えた
ガラス製四つ口フラスコに、単量体ジイソシアネートと
してヘキサメチレンジイソシアネート1000gを仕込
み、フラスコ内の空気を窒素で置換し、撹はんしながら
60℃に加熱した。三量化触媒として、テトラメチルア
ンモニウム・カプリエート0.2gを分割して加えた。
60℃で反応を続け、反応液の屈折率測定により、ヘキ
サメチレンジイソシアメートの転化率が20%になった
時点で、ジブトキシエチルホスフェートを0.5g添加
して反応を停止した。この反応液より、流下式薄膜蒸留
装置を用いて、未反応のヘキサメチレンジイソシアネー
トを除去回収した。
Example 1 A glass four-necked flask equipped with a thermometer, a stirrer, and a nitrogen seal tube was charged with 1000 g of hexamethylene diisocyanate as a monomeric diisocyanate, the air in the flask was replaced with nitrogen, and the mixture was stirred. Heated to 60 ° C. with stirring. As a trimerization catalyst, 0.2 g of tetramethylammonium capryate was added in portions.
The reaction was continued at 60 ° C., and when the conversion of hexamethylene diisocyanate reached 20% by measuring the refractive index of the reaction solution, 0.5 g of dibutoxyethyl phosphate was added to stop the reaction. Unreacted hexamethylene diisocyanate was removed and recovered from this reaction solution using a falling film distillation apparatus.

【0018】[0018]

【実施例2】ジブトキシエチルホスフェートに代えてモ
ノブトキシエチルホスフェートを使う以外は、実施例1
と同様にして行った。
Example 2 Example 1 except that monobutoxyethyl phosphate is used instead of dibutoxyethyl phosphate.
I went in the same way.

【0019】[0019]

【実施例3】温度計、撹はん機、窒素シール管を備えた
ガラス製四つ口フラスコに、単量体ジイソシアネートと
してトリレンジイソシアネート1000g、ブタンジオ
ール50gを仕込み、フラスコ内の空気を窒素で置換
し、撹はんしながら反応させた。酢酸ブチル1000g
に溶解した後、三量化触媒として、テトラメチルエチレ
ンジアミン5gを加え、反応液のNCO含量が8%にな
ったところでプロポキシエチルホスフェート3.0gを
加え、反応を停止した。
Example 3 A glass four-necked flask equipped with a thermometer, a stirrer, and a nitrogen seal tube was charged with 1000 g of tolylene diisocyanate as monomer diisocyanate and 50 g of butanediol, and the air in the flask was filled with nitrogen. After substitution, the reaction was carried out with stirring. Butyl acetate 1000g
Then, 5 g of tetramethylethylenediamine was added as a trimerization catalyst, and when the NCO content of the reaction solution reached 8%, 3.0 g of propoxyethyl phosphate was added to stop the reaction.

【0020】この反応液より、流下式薄膜蒸留装置を用
いて、未反応のトリレンジイソシアネート及び酢酸ブチ
ルを除去回収した。
From the reaction solution, unreacted tolylene diisocyanate and butyl acetate were removed and recovered using a falling film distillation apparatus.

【0021】[0021]

【比較例1】ジブトキシエチルホスフェートに代えて、
りん酸を0.3g使用する以外は、実施例1と同様にし
て行った。
Comparative Example 1 Instead of dibutoxyethyl phosphate,
Example 1 was repeated except that 0.3 g of phosphoric acid was used.

【0022】[0022]

【比較例2】ジブトキシエチルホスフェートに代えて、
ジブチルホスフェートを0.4g使用する以外は、実施
例1と同様にして行った。
Comparative Example 2 Instead of dibutoxyethyl phosphate,
Example 1 was repeated except that 0.4 g of dibutyl phosphate was used.

【0023】[0023]

【比較例3】ジブトキシエチルホスフェートに代えて、
ジプロピルホスフェートを0.3g使用する以外は、実
施例1と同様にして行った。
Comparative Example 3 Instead of dibutoxyethyl phosphate,
Example 1 was repeated except that 0.3 g of dipropyl phosphate was used.

【0024】[0024]

【比較例4】ジブトキシエチルホスフェートに代えて、
トリブトキシエチルホスフェートを1.0g使用する以
外は、実施例1と同様にして行ったが、反応が停止しな
かった。以上の例で得られたポリイソシアネートの測定
結果を表1に示す。
Comparative Example 4 Instead of dibutoxyethyl phosphate,
Example 1 was repeated except that 1.0 g of tributoxyethyl phosphate was used, but the reaction did not stop. Table 1 shows the measurement results of the polyisocyanate obtained in the above examples.

【0025】[0025]

【表1】 [Table 1]

【0026】[0026]

【発明の効果】浮遊物の発生がなく、溶剤で希釈時にも
にごりの発生しないイソシアヌレート環を有するポリイ
ソシアネートを製造することができる。
EFFECT OF THE INVENTION It is possible to produce a polyisocyanate having an isocyanurate ring which does not generate floating substances and does not cause turbidity even when diluted with a solvent.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】第三級アミンまたは第四級アンモニウム塩
の存在下に、単量体ジイソシアネート、及び、単量体ジ
イソシアネートと1〜3官能性のアルコールとの予備ウ
レタン化反応物から選ばれた、少なくとも1種のイソシ
アネート化合物のイソシアネート基の一部の三量化反応
を行い、触媒被毒物質により反応を停止することからな
る、イソシアヌレート基含有ポリイソシアネートの製法
において、アルコキシ基含有酸性燐酸エステルを触媒被
毒物質として使用することを特徴とする、イソシアヌレ
ート基含有ポリイソシアネートの製法。
1. A monomer diisocyanate in the presence of a tertiary amine or a quaternary ammonium salt, and a pre-urethanization reaction product of the monomer diisocyanate and a 1-3 functional alcohol. In a process for producing an isocyanurate group-containing polyisocyanate, which comprises performing a trimerization reaction of a part of an isocyanate group of at least one isocyanate compound and stopping the reaction by a catalyst poisoning substance, an alkoxy group-containing acidic phosphate ester A method for producing a polyisocyanate containing an isocyanurate group, which is used as a catalyst poisoning substance.
JP03340910A 1991-12-24 1991-12-24 Process for producing isocyanurate group-containing polyisocyanate Expired - Lifetime JP3111103B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03340910A JP3111103B2 (en) 1991-12-24 1991-12-24 Process for producing isocyanurate group-containing polyisocyanate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03340910A JP3111103B2 (en) 1991-12-24 1991-12-24 Process for producing isocyanurate group-containing polyisocyanate

Publications (2)

Publication Number Publication Date
JPH05170748A true JPH05170748A (en) 1993-07-09
JP3111103B2 JP3111103B2 (en) 2000-11-20

Family

ID=18341435

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03340910A Expired - Lifetime JP3111103B2 (en) 1991-12-24 1991-12-24 Process for producing isocyanurate group-containing polyisocyanate

Country Status (1)

Country Link
JP (1) JP3111103B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999010354A1 (en) * 1997-08-26 1999-03-04 Daihachi Chemical Industry Co., Ltd. Phosphoric ester compounds and process for producing the same, copper phosphoric ester compounds and process for producing the same, near infrared absorber, and near infrared absorbent acrylic resin composition
WO2007034883A1 (en) * 2005-09-22 2007-03-29 Asahi Kasei Chemicals Corporation Polyisocyanate composition and coating composition containing the same
JP2016008300A (en) * 2014-06-26 2016-01-18 東ソー株式会社 Polyisocyanurate-modified isocyanate composition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999010354A1 (en) * 1997-08-26 1999-03-04 Daihachi Chemical Industry Co., Ltd. Phosphoric ester compounds and process for producing the same, copper phosphoric ester compounds and process for producing the same, near infrared absorber, and near infrared absorbent acrylic resin composition
US6410613B1 (en) 1997-08-26 2002-06-25 Kureha Kagaku Kogyo Kabushiki Kaisha Phosphate compound and preparation process thereof, phosphate copper compound and preparation process thereof, near infrared ray absorber, and near infrared ray-absorbing acrylic resin composition
WO2007034883A1 (en) * 2005-09-22 2007-03-29 Asahi Kasei Chemicals Corporation Polyisocyanate composition and coating composition containing the same
US8952120B2 (en) 2005-09-22 2015-02-10 Asahi Kasei Chemicals Corporation Polyisocyanate composition and coating composition containing the same
JP2016008300A (en) * 2014-06-26 2016-01-18 東ソー株式会社 Polyisocyanurate-modified isocyanate composition

Also Published As

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