JPH0368023B2 - - Google Patents

Info

Publication number
JPH0368023B2
JPH0368023B2 JP59245365A JP24536584A JPH0368023B2 JP H0368023 B2 JPH0368023 B2 JP H0368023B2 JP 59245365 A JP59245365 A JP 59245365A JP 24536584 A JP24536584 A JP 24536584A JP H0368023 B2 JPH0368023 B2 JP H0368023B2
Authority
JP
Japan
Prior art keywords
diisocyanate
reaction
isocyanate
phosphite
catalyst
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 - Lifetime
Application number
JP59245365A
Other languages
Japanese (ja)
Other versions
JPS61129173A (en
Inventor
Shoichi Fujita
Koji Nasu
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.)
Takeda Pharmaceutical Co Ltd
Original Assignee
Takeda Chemical Industries 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 Takeda Chemical Industries Ltd filed Critical Takeda Chemical Industries Ltd
Priority to JP59245365A priority Critical patent/JPS61129173A/en
Publication of JPS61129173A publication Critical patent/JPS61129173A/en
Publication of JPH0368023B2 publication Critical patent/JPH0368023B2/ja
Granted legal-status Critical Current

Links

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

Landscapes

  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Polyurethanes Or Polyureas (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

 産業䞊の利甚分野 本発明は、たずえばポリりレタン塗料を補造す
る際の硬化剀ずしお有甚な、む゜シアヌレヌト環
ずむ゜シアナヌト基ずを有する化合物の補造法に
関する。さらに詳しくは、觊媒ずしおヒドロキシ
アルキル第四玚アンモニりム化合物を甚い、さら
に助觊媒ずしお有機亜リン酞゚ステルを䜵甚する
こずを特城ずするむ゜シアネヌト化合物からむ゜
シアヌレヌト環ずむ゜シアナヌト基ずを有する化
合物の補造法に関する。  埓来の技術 む゜シアヌレヌト環ずむ゜シアナヌト基ずを有
する化合物は、䞀般にむ゜シアネヌトトリマヌず
も呌ばれる通垞未端に個以䞊の反応性む゜シア
ナヌト基を有するず共に、分子内に耐候性、耐熱
性、耐薬品性などに優れるむ゜シアヌレヌト環を
有しおおり、さらに蒞気圧が䜎く取り扱いが容易
であるこずもあ぀お、たずえばポリりレタン塗料
などを補造する際の硬化剀ずしお、利甚されおい
る。このようなむ゜シアネヌトトリマヌは、通垞
有機ポリむ゜シアネヌトを原料ずし、これに觊媒
を䜜甚させお補造しおいる。このようなむ゜シア
ヌレヌト化の䜜甚のある觊媒ずしお、埓来から、
たずえば第䞉玚アミン、有機酞の金属塩、第䞉玚
ホスフむンをはじめずしお、数倚くの化合物が提
案され今日に至぀おいる。近時、脂肪族系の有機
ポリむ゜シアネヌトのむ゜シアヌレヌト化の觊媒
ずしおヒドロキシアルキル第四玚アンモニりム化
合物、特にヒドロキシアルキル第四玚アンモニり
ムヒドロキシドたずえば特開昭55−38380号公
報、特開昭54−119480号公報参照あるいはヒド
ロキシアルキル第四玚アンモニりムカルボキシレ
ヌトたずえば特開昭52−17484号公報、特開昭
55−143978号公報参照が有効であるこずが報告
されおいる。  発明が解決しようずする問題点 䞊蚘第四玚アンモニりム化合物觊媒は、比范的
小量䜿甚するだけで觊媒䜜甚を瀺すが、その䜜甚
は原料䞭に極く埮量存圚する䞍玔物の圱響を受け
易く、特に工業的に補造・販売されおいる有機ポ
リむ゜シアネヌトを原料ずする堎合には、䜜甚が
発珟しにくか぀たり、たた䞀旊䜜甚が発珟するず
む゜シアヌレヌト化の反応が急激に進行しお、反
応液がゲル化しおしたうなどの問題が残されおい
る。たた、䞀般に觊媒によるむ゜シアヌレヌト化
の反応では、生成物が着色し、濁りが発生するこ
ずが避けられない。これらの着色、濁りは、觊媒
の皮類、反応枩床によ぀お巊右されるが、觊媒の
䜿甚量によ぀おも倧きな圱響を受ける。䞊蚘第四
玚アンモニりム化合物は、埓来公知のむ゜シアヌ
レヌト化の觊媒に比べ、生成物の着色、濁りの点
で幟分改善されおはいるものの䟝然ずしお、これ
らの問題が解決されるたでに至぀おいない。 本発明者らは、む゜シアヌレヌト化の反応の制
埡が容易で、か぀反応生成物に着色、濁りの発生
しないむ゜シアヌレヌト化觊媒に぀いお鋭意怜蚎
したずころ、ヒドロキシアルキル第四玚アンモニ
りム化合物を觊媒ずしお甚い、この觊媒に、さら
に有機亜リン酞゚ステルを組合わせお䜿甚した堎
合、觊媒の䜿甚量が極めお少量であ぀おも匷い觊
媒掻性を瀺すこずを芋い出した。すなわち有機亜
リン酞゚ステルは、それ自䜓にはむ゜シアヌレヌ
ト化の觊媒䜜甚はないが、第四玚アンモニりムの
觊媒䜜甚を倧幅に増匷する、いわゆる助觊媒しお
の䜜甚のあるこずを芋い出した。本発明は、この
知芋に基づいおなされたものである。  問題点を解決するための手段 本発明はむ゜シアネヌト化合物を有機亜リン酞
゚ステルの存圚䞋にヒドロキシアルキル第四玚ア
ンモニりム化合物を觊媒ずしお反応させるこずを
特城ずするむ゜シアヌレヌト環ずむ゜シアナヌト
基ずを有する化合物の補造法である。 本発明においお觊媒ずしお䜿甚するヒドロキシ
アルキル第四玚アンモニりム化合物ずしおは、た
ずえばヒドロキシアルキル第四玚アンモニりムカ
ルボキシレヌト以䞋、カルボキシレヌト觊媒ず
略すこずもある。ずヒドロキシアルキル第四玚
アンモニりムヒドロキシド以䞋、ヒドロキシド
觊媒ず略すこずもある。ずを挙げるこずがでる。
これら化合物は、いずれも有機ポリむ゜シアネヌ
トのむ゜シアヌレヌト化の觊媒ずしお公知であ
り、これら公知の觊媒をそのたた䜿甚するこずが
できる。カルボキシレヌト觊媒は、ゞプロピレン
グリコヌルのごずき溶媒䞭で第䞉玚アミンずアル
キレンオキシドずを有機カルボン酞の存圚䞋に反
応させるこずにより埗られる。このようなものず
しお、たずえばトリメチル−−−ヒドロキシ
プロピルアンモニりム・−゚チルヘキサノ゚ヌ
ト、−ゞメチル−−ヒドロキシ゚チル−
−−ヒドロキシプロピルアンモニりム・ヘキ
サノ゚ヌト、トリメチル−−−ヒドロキシプ
ロピルアンモニりム・ヘキサデカノ゚ヌト、トリ
メチル−−−ヒドロキシプロピルアンモニり
ム・プニルカヌボネヌト、トリメチル−−
−ヒドロキシプロピルアンモニりム・フオヌメヌ
トなどを挙げるこずができるが、䜕らこれらに限
定されるものではない。たた、ヒドロキシ觊媒は
氎メタノヌル䞭で、第䞉玚アミンずアルキレン
オキシドずを反応させるこずにより埗られる。こ
のようなものずしお、たずえば−ヒドロキシ゚
チル−トリメチルアンモニりムヒドロキシド、
−ヒドロキシ゚チル−ドデシル−ゞメチルアンモ
ニりムヒドロキシド、−ヒドロキシ゚チル−ゞ
メチル−2′−ゞヒドロキシメチル−ブチルア
ンモニりムヒドロキシド、゚チレンオキシドず
−ゞアザビシクロ−−オクタン
のモノ付加物などを挙げるこずができるが、䜕ら
これらに限定されるものではない。 本発明で助觊媒ずしお䜿甚する有機亜リン酞゚
ステルずしおは、有機亜リン酞ゞ゚ステルず有機
亜リン酞トリ゚ステルずを挙げるこずができる。
これら化合物は分子䞭に
A. Industrial Application Field The present invention relates to a method for producing a compound having an isocyanurate ring and an isocyanate group, which is useful as a curing agent in producing polyurethane paints, for example. More specifically, a method for producing a compound having an isocyanurate ring and an isocyanate group from an isocyanate compound, which is characterized by using a hydroxyalkyl quaternary ammonium compound as a catalyst and an organic phosphite ester as a co-catalyst. Regarding. B. Prior Art A compound having an isocyanurate ring and an isocyanate group, which is also generally called an isocyanate trimer, usually has three or more reactive isocyanate groups at each end, and also has weather resistance, heat resistance, and chemical resistance in the molecule. It has an isocyanurate ring with excellent properties, and has a low vapor pressure and is easy to handle, so it is used as a curing agent in the production of polyurethane paints, for example. Such isocyanate trimers are usually manufactured by using organic polyisocyanate as a raw material and applying a catalyst to the organic polyisocyanate. Conventionally, as a catalyst that has the effect of isocyanurating,
For example, many compounds have been proposed to date, including tertiary amines, metal salts of organic acids, and tertiary phosphines. Recently, hydroxyalkyl quaternary ammonium compounds, especially hydroxyalkyl quaternary ammonium hydroxides (for example, JP-A-55-38380, JP-A-Sho 54- 119480) or hydroxyalkyl quaternary ammonium carboxylates (for example, JP-A-52-17484, JP-A-Sho
55-143978) is reported to be effective. C Problems to be Solved by the Invention The quaternary ammonium compound catalyst described above exhibits catalytic action even when used in a relatively small amount, but its action is easily affected by impurities present in extremely small amounts in the raw materials. In particular, when using industrially produced and sold organic polyisocyanates as raw materials, the effect may be difficult to develop, and once the effect occurs, the isocyanurate reaction proceeds rapidly and the reaction liquid Problems such as gelation remain. Further, in general, in the isocyanurate reaction using a catalyst, it is inevitable that the product becomes colored and cloudy. These coloring and turbidity depend on the type of catalyst and reaction temperature, but are also greatly affected by the amount of catalyst used. Although the above-mentioned quaternary ammonium compounds are somewhat improved in terms of coloring and turbidity of the product compared to conventionally known isocyanurate catalysts, these problems still remain to be solved. do not have. The present inventors have conducted intensive studies on isocyanurate catalysts that are easy to control the isocyanurate reaction and do not cause coloration or turbidity in the reaction product, and have found that using a hydroxyalkyl quaternary ammonium compound as a catalyst, It has been found that when this catalyst is further used in combination with an organic phosphite, strong catalytic activity is exhibited even when the amount of catalyst used is extremely small. In other words, it has been found that although organic phosphite itself does not have a catalytic effect on isocyanurate formation, it acts as a so-called co-catalyst, which significantly enhances the catalytic effect of quaternary ammonium. The present invention has been made based on this knowledge. D Means for Solving the Problems The present invention is characterized in that an isocyanurate ring and an isocyanate group are reacted by reacting an isocyanate compound in the presence of an organic phosphite using a hydroxyalkyl quaternary ammonium compound as a catalyst. This is a method for producing a compound having Examples of the hydroxyalkyl quaternary ammonium compounds used as catalysts in the present invention include hydroxyalkyl quaternary ammonium carboxylate (hereinafter sometimes abbreviated as carboxylate catalyst) and hydroxyalkyl quaternary ammonium hydroxide (hereinafter sometimes abbreviated as carboxylate catalyst). , sometimes abbreviated as hydroxide catalyst).
All of these compounds are known as catalysts for converting organic polyisocyanates into isocyanurates, and these known catalysts can be used as they are. Carboxylate catalysts are obtained by reacting a tertiary amine with an alkylene oxide in the presence of an organic carboxylic acid in a solvent such as dipropylene glycol. Examples of such substances include trimethyl-N-2-hydroxypropylammonium 2-ethylhexanoate, N,N-dimethyl-N-hydroxyethyl-
N-2-hydroxypropylammonium hexanoate, trimethyl-N-2-hydroxypropylammonium hexadecanoate, trimethyl-N-2-hydroxypropylammonium phenyl carbonate, trimethyl-N-2
Examples include, but are not limited to, -hydroxypropylammonium formate. Hydroxy catalysts can also be obtained by reacting tertiary amines and alkylene oxides in water/methanol. These include, for example, 2-hydroxyethyl-trimethylammonium hydroxide, 2-hydroxyethyl-trimethylammonium hydroxide,
-Hydroxyethyl-dodecyl-dimethylammonium hydroxide, 2-hydroxyethyl-dimethyl-2,2'-dihydroxymethyl-butylammonium hydroxide, monoadduct of ethylene oxide and 1,4-diazabicyclo-2,2,2-octane These examples include, but are not limited to these in any way. Examples of the organic phosphite used as a cocatalyst in the present invention include organic phosphite diester and organic phosphite triester.
These compounds are in the molecule

【匏】あるい は[formula] or teeth

【匏】ただし、酞玠原子の䞀方の手 は炭玠原子ず結合しおいるなる郚分構造を個
以䞊通垞個ないし個有しおいる。本発明
では有機亜リン酞トリ゚ステルを䜿甚するのが奜
たしく、このようなものずしお具䜓的には次のも
のを挙げるこずができる。 (i) −−3P〔ただし、は同䞀たたは異な
぀お炭玠数〜20のアルキルあるいは炭玠数
〜20のアルキルで眮換されおいおもよいアリヌ
ルアリヌルずしおは、たずえばプニルを
衚わす〕で瀺される化合物。このようなものず
しお、たずえばトリ゚チルホスフアむト、トリ
ブチルホスフアむト、トリス−゚チルヘキ
シルホスフアむト、トリデシルホスフアむ
ト、トリラりリルホスフアむト、トリストリ
デシルホスフアむト、トリステアリルホスフ
アむトトリプニルホスフアむト、トリス
ノニルプニルホスフアむト、トリス
−ゞ−−ブチルプニルホスフアむト
あるいはゞプニルデシルホスフアむト、ゞフ
゚ニルトリデシルホスフアむトなどのモノ
ホスフアむト類、 (ii) たずえばゞステアリル・ペンタ゚リスリチ
ル・ゞホスフアむトゞ・ドデシル・ペンタ゚
リスリトヌル・ゞホスフアむトゞノニルプ
ニル・ペンタ゚リスリトヌル・ゞホスフアむ
ト、テトラプニル・テトラ・トリデシル・ペ
ンタ゚リスリチル・テトラホスフアむト、テト
ラプニル・ゞプロピレングリコヌル・ゞホス
フアむト、トリペンタ゚リスリトヌル・トリホ
スフアむトなどの倚䟡アルコヌルから誘導され
たゞ・トリあるいはテトラホスフアむト類、お
よび (iii) たずえばゞ・アルキルC1-20・ビスプノ
ヌルA.ゞホスフアむト、4′−ブチリデン−
ビス−メチル−−−ブチルプニル−
ゞ・トリデシルホスフアむトなどのビスプ
ノヌル系化合物から誘導されたゞホスフアむト
類、および (iv) その他、たずえば氎添ビスプノヌルホス
フアむトポリマヌ分子量2400〜3000などの
ポリホスフアむト類。さらに有機亜リン酞ゞ゚
ステルずしおは、RO−2P〔ただし、
は前蚘ず同意矩〕を挙げるこずができ、この
ようなゞ゚ステルずしお、たずえばゞラりリル
ハむドロゲンホスフアむト、ゞプニルハむド
ロゲンホスフアむトなどがある。蚘号で瀺さ
れるアルキルは、たずえばクロルのようなハロ
ゲンで眮換されおいおもよく、このようなもの
ずしお、たずえばトリス−ゞクロロプ
ロピルホスフアむトがある。たた䞊蚘ホスフ
アむトの酞玠原子は硫黄原子で眮換されたもの
であ぀おもよく、このようなものずしお、たず
えばトリラりリルトリチオホスフアむトなどが
ある。 本発明の方法では、このような助觊媒を觊媒ず
組合わせお䜿甚し、觊媒自䜓の䜿甚量は、それ単
独で䜿甚する堎合の最も効果的な量よりも少ない
量を甚いればよい。たずえばカルボキシレヌト觊
媒の堎合には、原料む゜シアネヌト化合物に察し
お以䞋同じ0.002〜0.05重量奜たしくは
0.005〜0.018重量、たたヒドロキシド觊媒の
堎合には0.001〜0.05重量奜たしくは0.002〜
0.009重量の範囲で充分な觊媒掻性を瀺す。 たた助觊媒ずしお䜿甚する亜リン酞゚ステルの
䜿甚量は、觊媒のほが1/10〜10倍、奜たしくは等
量〜倍量である。この量よりも少ないず助觊媒
ずしおの䜜甚が充分でなく、たたこの量を越える
ず、反応により埗られた生成物を利甚した。最終
補品の物性に悪圱響を及がす恐れがある。 さらに本発明で原料ずしお䜿甚するこずのでき
るむ゜シアネヌト化合物ずしおは、埓来からむ゜
シアネヌトトリマヌの補造に利されおいるむ゜シ
アナヌト基を有する化合物を挙げるこずができ
る。 このような化合物ずしお、たずえば有機ポリむ
゜シアネヌトがある。有機ポリむ゜シアネヌトず
しおは、たずえばトリメチレンゞむ゜シアネヌ
ト、テトラメチレンゞむ゜シアネヌト、ヘキサメ
チレンゞむ゜シアネヌト、ペンタメチレンゞむ゜
シアネヌト、−プロピレンゞむ゜シアネヌ
ト、−ブチレンゞむ゜シアネヌト、
−ブチレンゞむ゜シアネヌト、−たた
は−トリメチルヘキサメチレンゞむ゜
シアネヌト、ドデカメチレンゞむ゜シアネヌト、
−ゞむ゜シアナヌトメチルカプロ゚ヌトな
どの脂肪族ゞむ゜シアネヌト、たずえば−
シクロペンタンゞむ゜シアネヌト、−シク
ロヘキサンゞむ゜シアネヌト、−シクロヘ
キサンゞむ゜シアネヌト、−む゜シアナヌトメ
チル−3.5−トリメチルシクロヘキシルむ゜
シアネヌト、4′−メチレンビスシクロヘキ
シルむ゜シアネヌト、メチル−−シクロ
ヘキサンゞむ゜シアネヌト、メチル−−シ
クロヘキサンゞむ゜シアネヌト、−ビス
む゜シアナヌトメチルシクロヘキサン、
−ビスむ゜シアナヌトメチルシクロヘキサ
ンなどのシクロアルキレン系ゞむ゜シアネヌト、
たずえば−プニレンゞむ゜シアネヌト、−
プニレンゞむ゜シアネヌト、4′−ゞプニ
ルゞむ゜シアネヌト、−ナフタレンゞむ゜
シアネヌト、4′−ゞプニルメタンゞむ゜シ
アネヌト、−たたは−トリレンゞむ
゜シアネヌト、4′−トルむゞンゞむ゜シアネ
ヌト、ゞアニシゞンむ゜シアネヌト、4′−ゞ
プニル゚ヌテルゞむ゜シアネヌトなどの芳銙族
ゞむ゜シアネヌト、たずえばωω′−ゞむ゜シ
アネヌト−−ゞメチルベンれン、ω
ω′−ゞむ゜シアネヌト−−ゞメチルベン
れン、ωω′−ゞむ゜シアネヌト−−ゞ
゚チルベンれン、−テトラメチルキシリレ
ンゞむ゜シアネヌト、−テトラメチルキシ
リレンゞむ゜シアネヌトなどの芳銙脂肪族ゞむ゜
シアネヌト、たずえばトリプニルメタン−
4′4″−トリむ゜シアネヌト、−トリ
む゜シアネヌトベンれン、−トリむ゜
シアネヌトシクロヘキサン、−トリむ
゜シアネヌトトル゚ン、ω−む゜シアネヌト゚チ
ル−−ゞむ゜シアネヌトカプロ゚ヌトなど
のトリむ゜シアネヌトなどがある。これら有機ポ
リむ゜シアネヌトのうち、脂肪族ゞむ゜シアネヌ
トおよびシクロアルキレン系ゞむ゜シアネヌトは
本発明で有利に甚いるこずのできる、む゜シアネ
ヌト化合物である。たた有機ポリむ゜シアネヌト
は皮以䞊の混合物たずえばヘキサメチレンゞ
む゜シアネヌトず−む゜シアナヌトメチル−
−トリメチルシクロヘキシルむ゜シア
ネヌトずの混合物で䜿甚しおもよい。さらに、
これら有機ポリむ゜シアネヌトに〜䟡のアル
コヌル、あるいは、たずえばポリ゚ステルポリオ
ヌル、ポリ゚ヌテルポリオヌルなどのポリオヌル
をNCOOHの倀がほが20〜30になるような割合
で反応させお埗られる未端にNCO基を有するり
レタンプレポリマヌを、本発明の原料ずしお䜿甚
するこずができる。䟡のアルコヌルずしおは、
たずえばメタノヌル、ブタノヌル、−゚チルヘ
キサノヌル、゚チレングリコヌルモノメチル゚ヌ
テルなど䟡のアルコヌルずしおは、たずえば
゚チレングリコヌル、−ブタンゞオヌル、
−ブタンゞオヌル、プロピレングリコヌ
ル、ネオペンチルグリコヌル、−ヘキサン
ゞオヌル、−゚チルヘキサンゞヌル、
−トリメチルペンタゞオヌルなど䟡のアル
コヌルずしおは、たずえばトリメチロヌルプロパ
ン、グリセリンなど䟡のアルコヌルずしお
は、たずえばペンタ゚リスリトヌルなどポリ゚
ステルポリオヌルずしおは、たずえばヒバリン酞
ネオペンチルグリコヌル゚ステルなどたたポリ
゚ヌテルポリオヌルずしおは、たずえばポリ゚チ
レングリコヌル、ポリプロピレングリコヌル、ポ
リテトラメチレン゚ヌテルグリコヌルなどを、そ
れぞれ挙げるこずができる。 本発明の方法では、このようなむ゜シアネヌト
化合物を原料ずし、これに觊媒ず助觊媒ずを添加
しおむ゜シアヌレヌト化の反応に付す。本発明の
む゜シアヌレヌト化の反応は、通垞30〜100℃、
奜たしくは40〜80℃で行なわれる。反応の進行は
NCO基含有量や粘床を枬定するこずにより远跡
するこずができきる。反応を所定量たで本発明
ではNCO基含有量が反応開始時のほが90〜50
に枛少するたで進行させたのち、反応を停止さ
せるために停止剀を加える。反応停止剀ずしお
は、酞性物質が甚いられる。酞性物質ずしおは、
たずえば塩酞、リン酞などの無機酞、たずえばベ
ンゟむルクロラむド、アセチルクロラむドなどの
有機酞クロラむドがある。これら停止剀は、䜿甚
した觊媒の量の1/2から倍重量皋床添加すれば
よい。本発明の方法は、無溶媒䞭でも進行する
が、必芁ならば、酢酞゚チル、酢酞ブチル、酢酞
セロ゜ルブアセテヌトなどの酢酞゚ステル類ある
いはリン酞トリメチル、リン酞トリ゚チルなどの
リン酞゚ステル類を溶媒にしお甚いおもよい。反
応終了埌、反応液には通垞は未反応む゜シアネヌ
トモノマヌが残存しおいるが、これは枛圧蒞留に
付しお留去するこずができる。溶媒に぀いおも同
様である。未反応む゜シアネヌトモノマヌの留去
には枛圧薄膜蒞留装眮を甚いるのがよい。この方
法により、未反応のむ゜シアネヌトモノマヌ含量
をほが重量以䞋、必芁に応じおほが重量
以䞋にするこずができる。 このようにしおむ゜シアヌレヌト環ずむ゜シア
ナヌト基ずを有する化合物が埗られる。この生成
物は、原料ずしお有機ゞむ゜シアネヌトを䜿甚し
た堎合、個の有機ゞむ゜シアネヌトが反応しお
生成した個のむ゜シアヌレヌト環ず個のむ゜
シアナヌト基ずを有する量䜓を䞻成分ずし、そ
の他量䜓個のむ゜シアヌレヌト環ず個の
む゜シアナヌト基ず量䜓個のむ゜シアヌ
レヌト環ず個のむ゜シアナヌト基ずを含有し
おいる。本発明の方法により䞉量䜓含量がほが40
〜70のもの液䜓クロマトグラフむヌによる分
析面積比を補造するこずができる。 本発明の方法では、原料玔床に拘わらずむ゜シ
アヌレヌト化の反応が安定に䞀定の速床で進行す
るため、反応をコントロヌルするこずが容易であ
り、む゜シアヌレヌト化の反応がある時点で急激
に進行しお反応液がゲル化するようなこずがな
い。たた、本発明の方法により補造されたむ゜シ
アヌレヌト環ずむ゜シアナヌト基ずを有する化合
物は、透明でか぀ほずんど着色しおいないため、
過や脱色凊理をするこずなく、そのたた硬化剀
などずしお䜿甚でき、商品䟡倀が極めお高い。す
なわち、本発明の目的物は、各皮りレタン甚ポリ
オヌル成分ず反応させお耐候性、耐熱性などの物
性に優れた塗料、接着剀、発泡䜓などを補造する
際の原料ずしお広く利甚するこずができ、極めお
有甚である。 以䞋、実斜䟋を挙げお本発明をさらに具䜓的に
説明する。 実斜䟋  ヘキサメチレンゞむ゜シアネヌト以䞋、
HDIず略す500をガラス補の四埄フラスコに
入れ、これを50℃に加枩したのち、トリメチル−
−−ヒドロキシプロピルアンモニりム・−
゚チルヘキサノ゚ヌト0.05、次いでテトラプ
ニルゞプロピレングリコヌルゞホスフアむト0.25
を加える。この混合物を撹拌䞋、60℃で時間
反応を続けるずNCO基含量は反応開始時の玄80
にたで枛少した。この時点で、ベンゟむルクロ
ラむド0.05を加えお反応を停止させた。埗られ
た反応液を薄膜蒞留装眮真空床0.7mgHg枩床
150℃にかけお未反応のHDIモノマヌを陀去
し、淡黄色透明の生成物を埗た。このものは
NCO基含有21.0、粘床25℃2300cps.色盞
APHA30であ぀た。このものの赀倖線吞収スペ
クトルに1680cm-1の吞収が認められたこずからむ
゜シアヌレヌト環を有するこずが確認された。 実斜䟋 〜 衚−および−に瀺す凊方および条件䞋
で実斜䟋ず同様にしおむ゜シアヌレヌト環ずむ
゜シアナヌト基ずを有する化合物を埗た。なお、
む゜シアヌレヌト化の反応は、ヘキサメチレンゞ
む゜シアネヌトHDIの堎合には、NCO基含
量がほが40、たた−む゜シアナヌトメチル−
−トリメチルシクロヘキシルむ゜シア
ネヌトIPDIの堎合にはNCO基含量がほが30
にな぀た時点で反応を停止させた。む゜シアヌ
レヌト化の反応液および蒞留によ぀お未反応モノ
マヌを留去しお埗られた生成物の物性を衚
および䞋欄に瀺した。
It has one or more (usually 1 to 4) partial structures of the formula: (wherein one hand of the oxygen atom is bonded to a carbon atom). In the present invention, it is preferable to use organic phosphorous acid triesters, and specific examples of such ones include the following. (i) (R-O) -3P [However, R is the same or different and is alkyl having 1 to 20 carbon atoms or 1 carbon number
-20 aryl optionally substituted with alkyl (aryl is, for example, phenyl). These include, for example, triethyl phosphite, tributyl phosphite, tris(2-ethylhexyl) phosphite, tridecyl phosphite, trilauryl phosphite, tris(tridecyl) phosphite, tristearyl phosphite; triphenyl phosphite, tris (nonylphenyl)phosphite, tris(2,
4-di-t-butylphenyl) phosphite;
or monophosphites such as diphenyldecyl phosphite and diphenyl (tridecyl) phosphite; (iii) di-tri or tetraphosphites derived from polyhydric alcohols such as tetra-tridecyl pentaerythrityl tetraphosphite, tetraphenyl dipropylene glycol diphosphite, tripentaerythritol triphosphite;・Alkyl (C 1-20 ) ・Bisphenol A. Diphosphite, 4,4'-butylidene-
bis(3-methyl-6-t-butylphenyl-
(iv) other polyphosphites, such as hydrogenated bisphenol A phosphite polymers (molecular weight 2400-3000). Furthermore, as the organic phosphite diester, (RO) -2P (o)H [however,
R has the same meaning as defined above], and examples of such diesters include dilauryl hydrogen phosphite and diphenyl hydrogen phosphite. Alkyl of the symbol R may be substituted with halogen, such as chloro, for example tris(2,3-dichloropropyl)phosphite. Further, the oxygen atom of the above-mentioned phosphite may be substituted with a sulfur atom, such as trilauryl trithiophosphite. In the process of the present invention, such a cocatalyst is used in combination with a catalyst, and the catalyst itself may be used in an amount less than the most effective amount when used alone. For example, in the case of a carboxylate catalyst, 0.002 to 0.05% by weight (preferably
0.005-0.018% by weight), and in the case of hydroxide catalysts 0.001-0.05% by weight (preferably 0.002-0.018% by weight)
0.009% by weight) shows sufficient catalytic activity. The amount of phosphite used as a cocatalyst is approximately 1/10 to 10 times the amount of the catalyst, preferably equivalent to 6 times the amount of the catalyst. If the amount is less than this amount, the action as a promoter will not be sufficient, and if it exceeds this amount, the product obtained by the reaction will be utilized. It may adversely affect the physical properties of the final product. Further, as the isocyanate compound that can be used as a raw material in the present invention, there can be mentioned a compound having an isocyanate group that has been conventionally used in the production of an isocyanate trimer. Examples of such compounds include organic polyisocyanates. Examples of the organic polyisocyanate include trimethylene diisocyanate, tetramethylene diisocyanate, hexamethylene diisocyanate, pentamethylene diisocyanate, 1,2-propylene diisocyanate, 2,3-butylene diisocyanate, 1,3
-butylene diisocyanate, 2,4,4- or 2,2,4-trimethylhexamethylene diisocyanate, dodecamethylene diisocyanate,
Aliphatic diisocyanates such as 2,6-diisocyanate methyl caproate, e.g. 1,3-
Cyclopentane diisocyanate, 1,4-cyclohexane diisocyanate, 1,3-cyclohexane diisocyanate, 3-isocyanatomethyl-3.5,5-trimethylcyclohexyl isocyanate, 4,4'-methylenebis(cyclohexyl isocyanate), methyl-2,4-cyclohexane Diisocyanate, methyl-2,6-cyclohexane diisocyanate, 1,4-bis(isocyanatomethyl)cyclohexane, 1,
Cycloalkylene diisocyanates such as 3-bis(isocyanatomethyl)cyclohexane,
For example, m-phenylene diisocyanate, p-
Phenylene diisocyanate, 4,4'-diphenyl diisocyanate, 1,5-naphthalene diisocyanate, 4,4'-diphenylmethane diisocyanate, 2,4- or 2,6-tolylene diisocyanate, 4,4'-toluidine diisocyanate , dianisidine isocyanate, aromatic diisocyanates such as 4,4'-diphenyl ether diisocyanate, e.g. ω,ω'-diisocyanate-1,3-dimethylbenzene, ω,
Aroaliphatic diisocyanates such as ω'-diisocyanate-1,4-dimethylbenzene, ω,ω'-diisocyanate-1,4-diethylbenzene, 1,3-tetramethylxylylene diisocyanate, 1,4-tetramethylxylylene diisocyanate, etc. , for example triphenylmethane-4,
4',4''-triisocyanate, 1,3,5-triisocyanatebenzene, 1,3,5-triisocyanatecyclohexane, 2,4,6-triisocyanatetoluene, ω-isocyanateethyl-2,6-diisocyanate triisocyanates such as proate. Among these organic polyisocyanates, aliphatic diisocyanates and cycloalkylene diisocyanates are isocyanate compounds that can be advantageously used in the present invention. mixtures (e.g. hexamethylene diisocyanate and 3-isocyanatomethyl-
It may also be used in a mixture with 3,5,5-trimethylcyclohexyl isocyanate). moreover,
These organic polyisocyanates are reacted with mono- to tetrahydric alcohols or polyols such as polyester polyols and polyether polyols at a ratio such that the NCO/OH value is approximately 20-30. Urethane prepolymers having groups can be used as raw materials in the present invention. As a monohydric alcohol,
For example, methanol, butanol, 2-ethylhexanol, ethylene glycol monomethyl ether, etc.; examples of dihydric alcohols include ethylene glycol, 1,3-butanediol,
1,4-butanediol, propylene glycol, neopentyl glycol, 1,6-hexanediol, 2-ethylhexanediol, 2,2,
4-trimethylpentadiol and the like; trihydric alcohols such as trimethylolpropane and glycerin; tetrahydric alcohols such as pentaerythritol; polyester polyols such as neopentyl hivalate glycol ester; Examples of the ether polyol include polyethylene glycol, polypropylene glycol, polytetramethylene ether glycol, and the like. In the method of the present invention, such an isocyanate compound is used as a raw material, a catalyst and a cocatalyst are added thereto, and the compound is subjected to an isocyanurate reaction. The isocyanurate reaction of the present invention is usually carried out at 30 to 100°C.
Preferably it is carried out at 40-80°C. The progress of the reaction is
It can be tracked by measuring the NCO group content and viscosity. The reaction is carried out to a predetermined amount (in the present invention, the NCO group content is approximately 90 to 50% of that at the start of the reaction).
After allowing the reaction to proceed (until the reaction decreases to ), a terminating agent is added to stop the reaction. An acidic substance is used as the reaction terminator. As acidic substances,
Examples include inorganic acids such as hydrochloric acid and phosphoric acid, and organic acid chlorides such as benzoyl chloride and acetyl chloride. These terminators may be added in an amount of about 1/2 to twice the weight of the catalyst used. Although the method of the present invention proceeds without a solvent, if necessary, acetate esters such as ethyl acetate, butyl acetate, and cellosolve acetate, or phosphate esters such as trimethyl phosphate and triethyl phosphate may be used as a solvent. It's okay. After the reaction is completed, unreacted isocyanate monomer usually remains in the reaction solution, but this can be distilled off under reduced pressure. The same applies to solvents. A vacuum thin film distillation apparatus is preferably used to distill off unreacted isocyanate monomers. By this method, the unreacted isocyanate monomer content can be reduced to approximately 3% by weight or less, and if necessary approximately 1% by weight.
It can be: In this way, a compound having an isocyanurate ring and an isocyanate group is obtained. When an organic diisocyanate is used as a raw material, the main component of this product is a trimer having one isocyanurate ring and three isocyanate groups produced by the reaction of three organic diisocyanates, and other It contains a pentamer (2 isocyanurate rings and 4 isocyanate groups) and a heptamer (3 isocyanurate rings and 5 isocyanate groups). The method of the invention reduces the trimer content to approximately 40
~70% (analysis by liquid chromatography; area ratio) can be produced. In the method of the present invention, the isocyanurate reaction progresses stably at a constant rate regardless of the purity of the raw materials, so the reaction is easy to control, and the isocyanurate reaction progresses rapidly at a certain point. The reaction solution will not gel. Furthermore, since the compound having an isocyanurate ring and an isocyanate group produced by the method of the present invention is transparent and has almost no color,
It can be used as a hardening agent without any filtration or decolorization, and has extremely high commercial value. That is, the object of the present invention can be widely used as a raw material for producing paints, adhesives, foams, etc. with excellent physical properties such as weather resistance and heat resistance by reacting with various polyol components for urethane. , extremely useful. Hereinafter, the present invention will be explained in more detail with reference to Examples. Example 1 Hexamethylene diisocyanate (hereinafter referred to as
HDI (abbreviated as HDI) was placed in a four-diameter glass flask, heated to 50°C, and then trimethyl-
N-2-hydroxypropylammonium 2-
0.05 g of ethylhexanoate, then 0.25 g of tetraphenyl dipropylene glycol diphosphite
Add g. When this mixture was allowed to react at 60°C for 3 hours with stirring, the NCO group content was approximately 80% at the start of the reaction.
%. At this point, 0.05 g of benzoyl chloride was added to stop the reaction. The obtained reaction solution was heated to a thin film distillation device (vacuum degree 0.7 mgHg; temperature
(150°C) to remove unreacted HDI monomer, and a pale yellow transparent product was obtained. This thing is
NCO group content 21.0%, viscosity (25℃) 2300cps.Hue
It was APHA30. Since absorption at 1680 cm -1 was observed in the infrared absorption spectrum of this product, it was confirmed that it had an isocyanurate ring. Examples 2 to 9 Compounds having an isocyanurate ring and an isocyanate group were obtained in the same manner as in Example 1 using the formulations and conditions shown in Tables-a and -b. In addition,
The isocyanuration reaction is carried out in the case of hexamethylene diisocyanate (HDI), with an NCO group content of approximately 40%, and 3-isocyanatomethyl-
In the case of 3,5,5-trimethylcyclohexyl isocyanate (IPDI), the NCO group content is approximately 30
%, the reaction was stopped. The physical properties of the isocyanurate reaction solution and the product obtained by distilling off unreacted monomers are shown in Table (a).
and b) shown in the bottom column.

【衚】【table】

【衚】 留に付し未反応モノマヌを陀去した。
実斜䟋 10 ヘキサメチレンゞむ゜シアネヌトHDI500
および゚チレングリコヌル10をガラス補の
埄フラスコに入れ、窒玠気流䞋75℃で時間りレ
タン化反応を行ない末端にNCO基を有するりレ
タンプレポリマヌを含む反応液を埗た。この反応
液を50℃に冷华し、これにトリメチル−−−
ヒドロキシプロピルアンモニりム・−゚チルヘ
キサノ゚ヌト0.05およびテトラプニルゞプロ
ピレングリコヌルゞホスフアむト0.25加え60℃
でむ゜シアヌレヌト化反応を行぀た。この反応液
のNCO基含量がほが40にな぀た時点玄時
間でベンゟむルクロラむド0.05を加えお反応
を停止させた。反応液䞭の未反応のHDIモノマ
ヌを薄膜蒞留装眮を甚いお留去し、淡黄色透明液
䜓を埗た。このものはNCO基含有量20.0、粘
床25℃2500cps色盞APHA30であ぀た。たた
赀線吞収スペクトルに1680cm-1の吞収が認められ
たこずからむ゜シアヌレヌト環を有するこずが確
認された。 実斜䟋 11〜16 衚に瀺す凊方および条件䞋で実斜䟋10ず同様
にしおむ゜シアヌレヌト環ずむ゜シアナヌト基ず
を有する化合物を埗た。なお、む゜シアヌレヌト
化反応は、ヘキサメチレンゞむ゜シアネヌト原料
HDIの堎合にはNCO基含量がほが40、たた
−む゜シアナヌトメチル−−トリメ
チルシクロヘキシルむ゜シアネヌトIPDI原
料の堎合にはNCO基含量がほが30にな぀た時
点で反応を停止させた。 む゜シアヌレヌト化の反応液および蒞留によ぀
お未反応モノマヌを留去しお埗られた生成物の物
性を衚䞋欄に瀺した。
[Table] Unreacted monomers were removed by distillation.
Example 10 Hexamethylene diisocyanate (HDI) 500
g and 10 g of ethylene glycol in a glass container
The mixture was placed in a diameter flask and subjected to urethanization reaction at 75°C for 2 hours under a nitrogen stream to obtain a reaction solution containing a urethane prepolymer having an NCO group at the end. This reaction solution was cooled to 50°C, and trimethyl-N-2-
Add 0.05 g of hydroxypropylammonium 2-ethylhexanoate and 0.25 g of tetraphenyldipropylene glycol diphosphite at 60°C.
The isocyanurate reaction was carried out. When the NCO group content of this reaction solution reached approximately 40% (about 3 hours), 0.05 g of benzoyl chloride was added to stop the reaction. The unreacted HDI monomer in the reaction solution was distilled off using a thin film distillation apparatus to obtain a pale yellow transparent liquid. This product had an NCO group content of 20.0%, a viscosity (25°C) of 2500 cps, and a hue of APHA30. In addition, absorption at 1680 cm -1 was observed in the red line absorption spectrum, which confirmed that it had an isocyanurate ring. Examples 11 to 16 Compounds having an isocyanurate ring and an isocyanate group were obtained in the same manner as in Example 10 using the formulation and conditions shown in the table. The isocyanurate reaction is performed when the NCO group content is approximately 40% in the case of hexamethylene diisocyanate raw material (HDI), and in the case of 3-isocyanatomethyl-3,5,5-trimethylcyclohexyl isocyanate (IPDI) raw material. The reaction was stopped when the NCO group content reached approximately 30%. The physical properties of the isocyanurate reaction solution and the product obtained by distilling off unreacted monomers are shown in the lower column of the table.

【衚】【table】

Claims (1)

【特蚱請求の範囲】[Claims]  む゜シアネヌト化合物を有機亜リン酞゚ステ
ルの存圚䞋にヒドロキシアルキル第四玚アンモニ
りム化合物を觊媒ずしお反応させるこずを特城ず
するむ゜シアヌレヌト環ずむ゜シアナヌト基ずを
有する化合物の補造法。
1. A method for producing a compound having an isocyanurate ring and an isocyanate group, which comprises reacting an isocyanate compound in the presence of an organic phosphite using a hydroxyalkyl quaternary ammonium compound as a catalyst.
JP59245365A 1984-11-19 1984-11-19 Production of compound having isocyanurate ring and isocyanate group Granted JPS61129173A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59245365A JPS61129173A (en) 1984-11-19 1984-11-19 Production of compound having isocyanurate ring and isocyanate group

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59245365A JPS61129173A (en) 1984-11-19 1984-11-19 Production of compound having isocyanurate ring and isocyanate group

Publications (2)

Publication Number Publication Date
JPS61129173A JPS61129173A (en) 1986-06-17
JPH0368023B2 true JPH0368023B2 (en) 1991-10-25

Family

ID=17132577

Family Applications (1)

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

Country Link
JP (1) JPS61129173A (en)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2770329B2 (en) * 1988-07-22 1998-07-02 倧日本むンキ化孊工業株匏䌚瀟 Method for producing polyisocyanate
US5086175A (en) * 1988-12-28 1992-02-04 Takeda Chemical Industries, Ltd. Polyisocyanates, their production and uses
JPH0320322A (en) * 1989-06-16 1991-01-29 Nippon Polyurethane Ind Co Ltd Modified polymethylenepolyphenyl polyisocyanate, resin composition having good storage stability, and production of polyisocyanurate foam by using them
US5102918A (en) * 1989-05-16 1992-04-07 Nippon Polyurethane Industry Co., Ltd. Process for producing modified organic polyisocyanate
DE3928503A1 (en) * 1989-08-29 1991-03-07 Bayer Ag METHOD FOR PRODUCING SOLUTIONS OF POLYISOCYANATES CONTAINING ISOCYANURATE GROUPS IN LACQUER SOLVENTS AND THE USE THEREOF
US5208334A (en) * 1991-07-22 1993-05-04 Miles Inc. Process for the production of polyisocyanates containing allophanate and isocyanurate groups
US5235018A (en) * 1991-07-22 1993-08-10 Miles Inc. Polyisocyanates containing allophanate and isocyanurate groups, a process for their production and their use in two-component coating compositions
DE19828935A1 (en) * 1998-06-29 1999-12-30 Basf Ag High viscosity polyisocyanate composition useful as a surface coating
JP5356300B2 (en) * 2010-03-30 2013-12-04 旭化成ケミカルズ株匏䌚瀟 Allophanate group-containing blocked polyisocyanate
EP3486230A1 (en) 2011-03-09 2019-05-22 Mitsui Chemicals, Inc. Pentamethylenediisocyanate, method for producing pentamethylenediisocyanate, polyisocyanate composition, polyurethane resin, and polyurea resin
JP6434825B2 (en) * 2014-03-04 2018-12-05 䞉井化孊株匏䌚瀟 Method for producing polyisocyanurate composition
WO2015133494A1 (en) * 2014-03-04 2015-09-11 䞉井化孊株匏䌚瀟 Isocyanurate composition
KR102202351B1 (en) 2016-02-19 2021-01-12 믞쓰읎 가가쿠 가부시킀가읎샀 Two-component curing type solvent-free laminate adhesive and cured resin

Also Published As

Publication number Publication date
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