JPH01319521A - Catalyst composition for polymerizing polyurethane - Google Patents

Catalyst composition for polymerizing polyurethane

Info

Publication number
JPH01319521A
JPH01319521A JP15171388A JP15171388A JPH01319521A JP H01319521 A JPH01319521 A JP H01319521A JP 15171388 A JP15171388 A JP 15171388A JP 15171388 A JP15171388 A JP 15171388A JP H01319521 A JPH01319521 A JP H01319521A
Authority
JP
Japan
Prior art keywords
tertiary amine
catalyst
acid
ammonium salt
quaternary ammonium
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
JP15171388A
Other languages
Japanese (ja)
Other versions
JP2664936B2 (en
Inventor
Yasutoshi Isayama
諫山 康敏
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.)
Kao Corp
Original Assignee
Kao Corp
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 Kao Corp filed Critical Kao Corp
Priority to JP63151713A priority Critical patent/JP2664936B2/en
Publication of JPH01319521A publication Critical patent/JPH01319521A/en
Application granted granted Critical
Publication of JP2664936B2 publication Critical patent/JP2664936B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/16Catalysts
    • C08G18/18Catalysts containing secondary or tertiary amines or salts thereof
    • C08G18/1875Catalysts containing secondary or tertiary amines or salts thereof containing ammonium salts or mixtures of secondary of tertiary amines and acids

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)

Abstract

PURPOSE:To obtain the subject composition, useful for producing polyurethane, such as rigid foam, of electric refrigerators, etc., and capable of improving resin fluidity, etc., and curing in a short time by compounding an organic carboxylate of a tertiary amine with a specific amount of a quaternary ammonium salt compound. CONSTITUTION:The objective composition obtained by mixing (A) a tertiary amine (e.g., N-methylmorpholine) with, as necessary, a polar organic solvent, stirring the resultant mixture while cooling a container, adding and mixing an organic carboxylic acid (preferably formic, acetic acid, etc.) in an amount of 0.1-1.0 equiv. based on 1 equiv. N of the tertiary amine in divided several portions, cooling the resultant mixture and compounding (B) 5-50wt.% quaternary ammonium salt compound (obtained by reacting an acid in the presence of a tertiary amine and then reacting an alkylene oxide in an amount of >=1mol based on 1mol tertiary amine) so as to provide 100wt.% total amount of both components (A) and (B).

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は軟質、硬質、半硬質フオーム、あるいはエラス
トマー等のポリウレタン製造の際に用いる触媒に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a catalyst used in the production of polyurethanes such as soft, hard, semi-rigid foams or elastomers.

更に詳しくは電気冷蔵庫を中心とした硬質フオーム、自
動車内装材に使用される軟質、半硬質フオーム、あるい
は靴底、自動車バンパー等に代表されるエラストマーの
硬化速度を促進するウレタン製造用の触媒に関するもの
である。
More specifically, it relates to catalysts for the production of urethane that accelerate the curing speed of hard foams mainly used in electric refrigerators, soft and semi-rigid foams used in automobile interior materials, and elastomers such as shoe soles and automobile bumpers. It is.

〔従来の技術及び発明が解決しようとする課題〕ポリウ
レタン製造用の触媒としては従来錫系、鉄系等の有機金
属類と第3級アミンが用いられ、特に第3級アミンが好
んで使用されている。例えばN−メチルモルフォリン、
N−エチルモルフォリン、l・リエチレンジアミン、テ
トラメチルへキサメチレンジアミン、ペンクメチルジエ
チレントリアミン、トリメチルアミノエチルピペラジン
、ジメチルシクロヘキンルアミン、ビス−(ジメチルア
ミノエチル)エーテル等の化合物がポリウレタン製造用
触媒として用いられている。
[Prior art and problems to be solved by the invention] Conventionally, tin-based, iron-based, and other organic metals and tertiary amines have been used as catalysts for producing polyurethane, with tertiary amines being particularly preferred. ing. For example, N-methylmorpholine,
Compounds such as N-ethylmorpholine, l-lyethylenediamine, tetramethylhexamethylenediamine, pencmethyldiethylenetriamine, trimethylaminoethylpiperazine, dimethylcyclohexylamine, and bis-(dimethylaminoethyl)ether are used as catalysts for polyurethane production. It is being

近年、ポリウレタン製造時におけるウレタン触媒への要
求が高度化してきている。例えば製品の大型化そして形
状の複雑化に対し少ない樹脂量で且つ、フオームの型内
流動性を高めるため低粘度状態での充填を行える触媒、
更に生産性を向上させる為脱型時間を短くする硬化性の
高い触媒ンステムである。
In recent years, demands on urethane catalysts during polyurethane production have become more sophisticated. For example, a catalyst that can be filled in a low viscosity state to increase the fluidity of the foam in the mold and with a small amount of resin as the product becomes larger and has a more complex shape.
Furthermore, it is a highly curable catalyst system that shortens demolding time to improve productivity.

しかし通常、樹脂流動性、充填性を向上させるため初期
樹脂化活性を低下させる触媒を単独で用いると後期樹脂
化活性も同時に低下させ脱型時間の延長を引き起こして
しまう。一方、後期樹脂化活性を向上させる触媒を単独
で用いると初期樹脂化活性も同時に高くなり樹脂流動性
が悪くなる。
However, normally, when a catalyst that lowers the initial resin forming activity is used alone in order to improve resin fluidity and filling property, the latter stage resin forming activity is also reduced at the same time, resulting in an extension of demolding time. On the other hand, if a catalyst that improves the late-stage resinization activity is used alone, the initial resinization activity also increases, resulting in poor resin fluidity.

このような問題点を解決するため初期活性が低く反応の
進行とともに活性の増大する、いわゆる遅延性触媒が考
えられている。
In order to solve these problems, so-called retarded catalysts, which have low initial activity and increase in activity as the reaction progresses, have been considered.

このような初期流動性と後期の硬化性を同時に満足させ
る事を目的とした触媒としては特開昭54−13069
7号公報、特公昭57−56491号公報に記載されて
いるように第3級アミンの有機カルボン酸塩が知られて
いる。
As a catalyst intended to simultaneously satisfy such initial fluidity and late curing properties, Japanese Patent Application Laid-Open No. 54-13069
Organic carboxylic acid salts of tertiary amines are known as described in Japanese Patent Publication No. 7 and Japanese Patent Publication No. 57-56491.

第3級アミンの有機カルボン酸塩はポリウレタンフォー
ム形成反応の初期においては第3級アミンが有機カルボ
ン酸でブロックされているため本来の活性を示さないが
、次第に上昇する反応熱により分解され、また有機カル
ボン酸がインシアネートと反応し触媒として有効な第3
級アミンを生成するため本来の触媒活性が発現される。
Organic carboxylic acid salts of tertiary amines do not exhibit their original activity at the beginning of the polyurethane foam forming reaction because the tertiary amines are blocked by organic carboxylic acids, but they are decomposed by the heat of reaction that gradually increases, and An organic carboxylic acid reacts with incyanate to form a third compound that is effective as a catalyst.
The original catalytic activity is expressed to produce a class amine.

このような性質を持つ第3級アミンの有機カルボン酸塩
触媒としては例えばトリエチレンジアミン、ビス−(ジ
メチルアミノエチル)エーテルやN、 N、 N、 N
、 N−ペンタメチルジエチレントリアミンなどの通常
の3級アミンとギ酸、酢酸、2−エチルヘキサン酸など
の有機カルボン酸の塩が知られている。
Examples of tertiary amine organic carboxylate catalysts having such properties include triethylene diamine, bis-(dimethylaminoethyl) ether, N, N, N, N, etc.
, Salts of ordinary tertiary amines such as N-pentamethyldiethylenetriamine and organic carboxylic acids such as formic acid, acetic acid, and 2-ethylhexanoic acid are known.

しかしながら、これら第3級アミンの有機カルボン酸塩
触媒は初期反応の遅延性により流動性の向上は顕著に現
れるが硬化性の向上による脱型時間の短縮には効果が小
さかった。そこで、より効果の大きな触媒、すなわち、
インシアネートとポリオールの反応において初期の樹脂
化活性を遅延させることで樹脂流動性、充填性を向上さ
せ、更に後期の樹脂化活性を促進し最終の硬化時間をよ
り短くする触媒システムが望まれていた。
However, although these tertiary amine organic carboxylate catalysts significantly improve fluidity due to the retardation of the initial reaction, they have little effect on shortening demolding time due to improved curability. Therefore, a more effective catalyst, namely,
There is a need for a catalyst system that improves resin fluidity and filling properties by delaying the initial resinization activity in the reaction between incyanate and polyol, and further promotes the late resinization activity to shorten the final curing time. Ta.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者らは前記の2つの性能を同時に向上する触媒を
鋭意検討した結果、第3級アミンの有機カルボン酸塩触
媒に第4級アンモニウム塩化合物を特定の比率で複合化
することで初期流動性を損なわずに硬化性が向上し大幅
な脱型時間の短縮が可能となることを見出し、本発明に
到達した。
The present inventors have intensively investigated a catalyst that improves the above two performances at the same time. As a result, the initial flow rate was improved by compounding a quaternary ammonium salt compound with a tertiary amine organic carboxylate catalyst at a specific ratio. The inventors have discovered that the curing properties can be improved without impairing the properties and the demolding time can be significantly shortened, and the present invention has been achieved.

即ち、本発明は第3級アミン化合物の炭素数1〜8の有
機カルボン酸の塩に対し、第4級アンモニウム塩化合物
を、両者の和を100重量%として5〜50重量%複合
してなるポリウレタン重合用触媒組成物を提供するもの
である。
That is, the present invention is a compound in which 5 to 50% by weight of a quaternary ammonium salt compound is combined with a salt of an organic carboxylic acid having 1 to 8 carbon atoms of a tertiary amine compound, with the sum of both being 100% by weight. A catalyst composition for polyurethane polymerization is provided.

本発明の触媒において、第4級アンモニウム塩の添加中
が5重量%未渦の場合その効果がほとんど見られず、5
0重量%を越えた場合樹脂表面のボロつきいわゆるフラ
イアビリティ−が多くなり面材との接着等に支障が出て
くる。好ましくは30〜45重量%である。
In the catalyst of the present invention, when 5% by weight of the quaternary ammonium salt is added without vortexing, almost no effect is observed;
If it exceeds 0% by weight, the resin surface will become loose, so-called flyability, and adhesion to the surface material will be hindered. Preferably it is 30 to 45% by weight.

すなわち本発明の触媒は第3級アミンの有機カルボン酸
塩に第4級アンモニウム塩化合物を複合してなる初期遅
延性と後期硬化性を同時に向上させるポリウレタン重合
用触媒である。
That is, the catalyst of the present invention is a polyurethane polymerization catalyst that simultaneously improves initial retardation and late curing properties, which is made by combining an organic carboxylate of a tertiary amine with a quaternary ammonium salt compound.

本発明で使用する第3級アミンの有機カルボン酸塩及び
、第4級アンモニウム塩化合物に用いる第3級アミンと
しては例えば、N−メチルモルフォリン、N−エチルモ
ルフォリン、トリエチレンジアミン、N、N、N、N−
テトラメチル−1,3−プロピレンジアミン、N、 N
、 N、 N−テトラメチルへキサメチレンジアミン、
N、N、N、N、L−ペンタメチルジエチレントリアミ
ン、ビス−(2−ジメチルアミノエチル)エーテノペ 
N、N−ジメチルエタノールアミン、N、N−ジメチル
ベンジルアミン、N、N、N−)IJメチルアミノエチ
ルピペラジン、N、N、N−ト’Jス(3−ジメチルア
ミノプロピル)へキサヒドロ−Sトリアジン等の化合物
が例示される。
Examples of the tertiary amine used in the organic carboxylate of a tertiary amine and the quaternary ammonium salt compound used in the present invention include N-methylmorpholine, N-ethylmorpholine, triethylenediamine, N,N , N, N-
Tetramethyl-1,3-propylenediamine, N, N
, N, N-tetramethylhexamethylenediamine,
N,N,N,N,L-pentamethyldiethylenetriamine, bis-(2-dimethylaminoethyl)ethenope
N,N-dimethylethanolamine, N,N-dimethylbenzylamine, N,N,N-)IJ methylaminoethylpiperazine, N,N,N-to'Js(3-dimethylaminopropyl)hexahydro-S Examples include compounds such as triazine.

本発明で使用する第3級アミンの有機力ルボン酸塩製造
の際に用いる炭素数1〜8の有機カルボン酸はギ酸、酢
酸、プロピオン酸、醋酸、カプリル酸、2−エチルへキ
サン酸、カプロン酸、ピルビン酸、安息香酸などが用い
られるが、ギ酸、酢酸、プロピオン酸が特に好ましく用
いられ、その添加量は該3級アミンの窒素1モル当量に
対し01から1.0モル当量が用いられる。
The organic carboxylic acids having 1 to 8 carbon atoms used in the production of organic carboxylic acid salts of tertiary amines used in the present invention are formic acid, acetic acid, propionic acid, acetic acid, caprylic acid, 2-ethylhexanoic acid, caprone. Acids such as pyruvic acid and benzoic acid are used, but formic acid, acetic acid, and propionic acid are particularly preferably used, and the amount added is from 0.1 to 1.0 molar equivalent per 1 molar equivalent of nitrogen of the tertiary amine. .

本発明で用いる第4級アンモニウム塩化合物は、該3級
アミンの存在下に無機酸でも有機酸でもよいが、酸を作
用させた後該3級アミン1モル当たり1モル以上、好ま
しくは1ないし3モルのアルキレンオキサイドを反応さ
せて製造されるものである。
The quaternary ammonium salt compound used in the present invention may be an inorganic acid or an organic acid in the presence of the tertiary amine; It is produced by reacting 3 moles of alkylene oxide.

アルキレンオキサイドの種類としてはエチレンオキサイ
ド、プロピレンオキザイド、ブチレンオキサイド、イソ
ブチレンオキサイドなどが好ましく使用される。
As the alkylene oxide, ethylene oxide, propylene oxide, butylene oxide, isobutylene oxide, etc. are preferably used.

本発明の触媒の製造に当たっては、第3級アミンを、必
要に際してはグリコール系に代表される極性有機溶剤を
混合した後、容器を冷却しながら撹拌し、数回に分けて
所定量の有機カルボン酸を添加、混合する。冷却後第4
級アンモニウム塩化合物を所定量添加、混合すればよい
In producing the catalyst of the present invention, the tertiary amine is mixed with a polar organic solvent, such as a glycol-based solvent, if necessary, and then stirred while cooling the container. Add acid and mix. 4th after cooling
What is necessary is to add and mix a predetermined amount of a class ammonium salt compound.

このようにして製造された本発明の複合触媒は通常使用
されるポリオールを100Bとした時05から5.0部
使用され、また共触媒として通常の3級アミンや有機錫
化合物と併用することも出来る。
The composite catalyst of the present invention produced in this way is used in an amount of 0.5 to 5.0 parts when the commonly used polyol is 100B, and can also be used in combination with a common tertiary amine or an organic tin compound as a cocatalyst. I can do it.

本発明の新規触媒を用いてポリウレタンを製造する際に
は、必要に応じて添加剤として、CFCl3やCH2C
l2等の発泡剤、有機ポリシロキサン等の界面活性剤、
ハロゲン化アルキル化合物、ハロゲン化リン化合物等の
難燃剤、その他の添加剤を用いることができる。
When producing polyurethane using the novel catalyst of the present invention, additives such as CFCl3 and CH2C may be used as necessary.
Foaming agents such as l2, surfactants such as organic polysiloxane,
Flame retardants such as halogenated alkyl compounds and halogenated phosphorus compounds, and other additives can be used.

これらの添加剤の種類及び添加量については、通常使用
される種類及び範囲において充分使用できる。
The types and amounts of these additives can be sufficiently used within the types and ranges commonly used.

〔実施例〕〔Example〕

以下に実施例及び比較例を示して本発明を具体的に説明
するが、本発明はこれら実施例のみに限定されるもので
はない。
EXAMPLES The present invention will be specifically explained below with reference to Examples and Comparative Examples, but the present invention is not limited only to these Examples.

ポリウレタン製造のための原料の混合割合を表−1に示
す配合とし、通常の手順に従ってウレタン発泡を実施し
た。即ち、20℃に保ったポリオール、水、界面活性剤
、触媒、発泡剤、ポリイソシアネートを混合、撹拌し、
紙製カップに注ぎ込みウレタンフオームを形成させた(
紙製カップの上部は解放状態)。
The mixing ratio of raw materials for polyurethane production was as shown in Table 1, and urethane foaming was carried out according to the usual procedure. That is, polyol, water, surfactant, catalyst, blowing agent, and polyisocyanate kept at 20°C are mixed and stirred,
Pour it into a paper cup to form a urethane foam (
The top of the paper cup is open).

今回フライアビリティ−の評価はASTM C42l−
61に準じた。・・・図−1 充填性の評価には40℃に温調した逆り字型発泡パネル
を用いてその成形品の長さにより判断した。・・・表3 又、硬化性の評価においては動的粘弾性の測定(ハイブ
ロン法)を用いて樹脂中心部の硬化挙動を連続追跡して
評価した。・・・図−2尚、図−2中のDFは樹脂硬度
の指標となる値である。
This time, the flyability evaluation was ASTM C42l-
61. ...Figure 1 Fillability was evaluated based on the length of the molded product using an inverted-shaped foam panel whose temperature was controlled at 40°C. ...Table 3 In addition, in the evaluation of curability, the curing behavior of the resin center was continuously tracked and evaluated using dynamic viscoelasticity measurement (Hybron method). ...Figure 2 Note that DF in Figure 2 is a value that is an index of resin hardness.

表   −1 実施例I II、 N、 l’l″J’J”−ペンタメチルジエチ
レントリアミン1モルを2−エチルへキサン酸1モルで
中和した後プロピレンオキザイドを1モル付加させ4級
アンモニウム塩化合物とした。一方、トリエチレンジア
ミンを2倍量のジプロピレングリコールに溶解した後ギ
酸をトリエチレンジアミンと当モル添加し撹拌、冷却後
、前記の4級アンモニウム塩化合物とギ酸塩の比が4/
6となるよう複合化した。
Table-1 Example I II, N, l'l''J'J''-1 mol of pentamethyldiethylenetriamine was neutralized with 1 mol of 2-ethylhexanoic acid, and then 1 mol of propylene oxide was added to form a quaternary ammonium salt. It was made into a compound. On the other hand, after dissolving triethylenediamine in twice the amount of dipropylene glycol, formic acid was added in the same molar amount as triethylenediamine, and after stirring and cooling, the ratio of the quaternary ammonium salt compound to formate was 4/4.
It was combined to become 6.

この触媒を用いて前記の処方にもとづき発泡を行った。Using this catalyst, foaming was carried out based on the above recipe.

結果は、表−3、図−1、図−2に示す。The results are shown in Table 3, Figures 1 and 2.

実施例2 実施例1において4級アンモニウム塩化合物とギ酸塩の
比を1/9とし同様の操作を行った。
Example 2 The same operation as in Example 1 was carried out except that the ratio of the quaternary ammonium salt compound to the formate was changed to 1/9.

結果は表−3、図−1に示す。The results are shown in Table 3 and Figure 1.

実施例3 実施例1においてギ酸を2−エチルヘキザン酸に変え、
同様の操作を行った。
Example 3 In Example 1, formic acid was changed to 2-ethylhexanoic acid,
A similar operation was performed.

結果は表−3、図=2に示す。The results are shown in Table 3 and Figure 2.

実施例4 実施例1においてギ酸を2倍モル添加し、同様の操作を
行った。
Example 4 The same operation as in Example 1 was performed except that twice the mole of formic acid was added.

結果は表−3に示す。The results are shown in Table-3.

実施例5 実施例1において4級アンモニウム塩化合物のプロピレ
ンオキサイドをエチレンオキザイドに変え、同様の操作
を行った。
Example 5 The same operation as in Example 1 was performed except that the propylene oxide of the quaternary ammonium salt compound was changed to ethylene oxide.

結果は表−3、図−2に示す。The results are shown in Table 3 and Figure 2.

比較例1 触媒としてN、 N、 N、 N、 N−ペンタメチル
ジエチレントリアミンを用いて前記処方に従い発泡を行
った。
Comparative Example 1 Foaming was carried out according to the above recipe using N, N, N, N, N-pentamethyldiethylenetriamine as a catalyst.

結果は表−3及び図−2に示す。The results are shown in Table 3 and Figure 2.

比較例2 触媒としてトリエチレンジアミンを用い−ご前記処方に
従い発泡を行った。
Comparative Example 2 Foaming was carried out according to the above recipe using triethylenediamine as a catalyst.

結果は表−3及び図−2に示す。The results are shown in Table 3 and Figure 2.

比較例3 実施例1においてギ酸塩触媒のみを用いて発泡を行った
Comparative Example 3 Foaming was carried out in Example 1 using only the formate catalyst.

結果は表−3及び図−1に示す。The results are shown in Table 3 and Figure 1.

比較例4 実施例1において4級アンモニウム塩化合物のみを用い
て発泡を行った。
Comparative Example 4 Foaming was carried out in Example 1 using only the quaternary ammonium salt compound.

結果は表−3及び図−1に示す。The results are shown in Table 3 and Figure 1.

比較例5 実施例1において用いた4級アンモニウム塩化合物とギ
酸塩触媒の比が7/3となるよう複合化したものを触媒
として用いて、発泡を行った。
Comparative Example 5 Foaming was carried out using a composite of the quaternary ammonium salt compound and formate catalyst used in Example 1 in a ratio of 7/3 as a catalyst.

結果は表−3及び図−1に示す。The results are shown in Table 3 and Figure 1.

表−2に上記の実施例、比較例の触媒の配合をまとめて
示す。
Table 2 summarizes the catalyst formulations of the above Examples and Comparative Examples.

表中ゲルタイムとは、ポリウレタンフォーム表面上に鋭
利な物体を接触させ、つついて離した場合、ポリウレタ
ンフォームから糸を引くまでに充分に高分子量化が進行
するのに要した時間を指す。
In the table, gel time refers to the time required for the polymerization to sufficiently proceed before a string is pulled from the polyurethane foam when a sharp object is brought into contact with the surface of the polyurethane foam and then removed.

表−2触媒配合例 GTニゲルタイム・・・55秒に設定 TBDA : トリエチレンジアミン P)、IDBTA :ペンタメチルジエチレントリーr
ミンFA:ギ酸 εH八 2−エチルヘキカン酸 Po:プロピレンオキザイド E口;エチレンオキザイド 表−3充填性の評価 〔発明の効果〕 本発明の複合系触媒は発泡時における充填性を向上し、
且つ硬化性を促進することが出来る。
Table-2 Catalyst blending example GT Nigel time...set to 55 seconds TBDA: triethylenediamine P), IDBTA: pentamethyldiethylene trir
Min FA: formic acid εH8 2-ethylhexanoic acid Po: propylene oxide
In addition, curability can be promoted.

例えば表−3において比較例3の充填性が優れているこ
とが明らかであるが、これに4級塩を複合した実施例1
においてもその充填性は同様に優れている。また図−2
より、その硬化挙動を評価すると3級アミン単体として
最高の硬化性を示す比較例2に対し比較例3は劣らない
ことがわかる。これに4級塩を複合することで実施例1
のように更に硬化性で上回ることが初めて定量的にわか
った。
For example, in Table 3, it is clear that Comparative Example 3 has excellent filling properties, but Example 1 in which a quaternary salt was combined with Comparative Example 3
The filling properties are also excellent. Also Figure-2
Therefore, when the curing behavior is evaluated, it can be seen that Comparative Example 3 is not inferior to Comparative Example 2, which exhibits the highest curability as a single tertiary amine. By combining this with quaternary salt, Example 1
For the first time, it has been quantitatively shown that the curability is even higher than that of the previous one.

以上より本発明の触媒の効果は明らかである。From the above, the effects of the catalyst of the present invention are clear.

又、4級塩触媒を使うことによるフライアビリティ−の
評価は図−1より約50%を上限として複合化すること
が望ましい。
Also, when evaluating the fryability by using a quaternary salt catalyst, it is desirable to combine the fryability with an upper limit of about 50% as shown in Figure 1.

【図面の簡単な説明】[Brief explanation of the drawing]

図−1はフライアビリティ−と触媒中の4級塩の割合の
関係を示すグラフ、図−2は触媒の硬化挙動を示すグラ
フである。
Figure 1 is a graph showing the relationship between flyability and the proportion of quaternary salt in the catalyst, and Figure 2 is a graph showing the curing behavior of the catalyst.

Claims (1)

【特許請求の範囲】 1 第3級アミン化合物の炭素数1〜8の有機カルボン
酸の塩に対し、第4級アンモニウム塩化合物を、両者の
和を100重量%として5〜50重量%複合してなるポ
リウレタン重合用触媒組成物。 2 第3級アミン化合物の有機カルボン酸の塩が、第3
級アミン化合物の窒素当量に対し、0.1から1.0当
量の一塩基性有機カルボン酸を使用して製造されるもの
である請求項1記載のポリウレタン重合用触媒組成物。
[Scope of Claims] 1. 5 to 50% by weight of a quaternary ammonium salt compound is combined with a salt of an organic carboxylic acid having 1 to 8 carbon atoms of a tertiary amine compound, with the sum of both being 100% by weight. A catalyst composition for polyurethane polymerization. 2 A salt of an organic carboxylic acid of a tertiary amine compound is
2. The catalyst composition for polyurethane polymerization according to claim 1, which is produced using 0.1 to 1.0 equivalent of the monobasic organic carboxylic acid relative to the nitrogen equivalent of the primary amine compound.
JP63151713A 1988-06-20 1988-06-20 Catalyst composition for polyurethane polymerization Expired - Lifetime JP2664936B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63151713A JP2664936B2 (en) 1988-06-20 1988-06-20 Catalyst composition for polyurethane polymerization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63151713A JP2664936B2 (en) 1988-06-20 1988-06-20 Catalyst composition for polyurethane polymerization

Publications (2)

Publication Number Publication Date
JPH01319521A true JPH01319521A (en) 1989-12-25
JP2664936B2 JP2664936B2 (en) 1997-10-22

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ID=15524649

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2664936B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996012748A1 (en) * 1994-10-21 1996-05-02 Sanyo Chemical Industries Ltd. Curable composition
JP2002069417A (en) * 2000-08-24 2002-03-08 Nippon Polyurethane Ind Co Ltd Adhesive composition for hot press molded article of lignocellulosic material, and hot press molded article using the same and its manufacturing method
JP2007186711A (en) * 2007-03-12 2007-07-26 Tosoh Corp Amine catalyst for producing polyurethane and polyisocyanurate
JP2014091827A (en) * 2012-11-07 2014-05-19 San Apro Kk Catalyst composition for manufacturing polyurethane resin and method for manufacturing rigid polyurethane foam or rigid polyisocyanurate foam

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996012748A1 (en) * 1994-10-21 1996-05-02 Sanyo Chemical Industries Ltd. Curable composition
US5854360A (en) * 1994-10-21 1998-12-29 Sanyo Chemical Industries Ltd. Curable composition
JP2002069417A (en) * 2000-08-24 2002-03-08 Nippon Polyurethane Ind Co Ltd Adhesive composition for hot press molded article of lignocellulosic material, and hot press molded article using the same and its manufacturing method
JP2007186711A (en) * 2007-03-12 2007-07-26 Tosoh Corp Amine catalyst for producing polyurethane and polyisocyanurate
JP4687668B2 (en) * 2007-03-12 2011-05-25 東ソー株式会社 Amine catalysts for the production of polyurethanes and polyisocyanurates
JP2014091827A (en) * 2012-11-07 2014-05-19 San Apro Kk Catalyst composition for manufacturing polyurethane resin and method for manufacturing rigid polyurethane foam or rigid polyisocyanurate foam

Also Published As

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