JPH0367107B2 - - Google Patents

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Publication number
JPH0367107B2
JPH0367107B2 JP59003506A JP350684A JPH0367107B2 JP H0367107 B2 JPH0367107 B2 JP H0367107B2 JP 59003506 A JP59003506 A JP 59003506A JP 350684 A JP350684 A JP 350684A JP H0367107 B2 JPH0367107 B2 JP H0367107B2
Authority
JP
Japan
Prior art keywords
mixture
polyol
group
parts
mgkoh
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
JP59003506A
Other languages
Japanese (ja)
Other versions
JPS60147329A (en
Inventor
Hirohide Sakaguchi
Ryoji Ichii
Toshio Sugita
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP59003506A priority Critical patent/JPS60147329A/en
Publication of JPS60147329A publication Critical patent/JPS60147329A/en
Publication of JPH0367107B2 publication Critical patent/JPH0367107B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳现な説明】 本発明は発泡成圢物の衚面を補匷する保護䜓の
匷化方法、ずくにポリりレタン局にお補匷する緩
衝性にすぐれた保護䜓の匷化方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for reinforcing a protective body for reinforcing the surface of a foam molded article, and particularly to a method for strengthening a protective body with excellent cushioning properties by reinforcing it with a polyurethane layer.

発泡合成暹脂成圢物は発泡倍率を高めるこずが
できるため䟡栌的に有利ずなり、䞔぀同時に䜎密
床ずなるため成圢物は軜量で極めお取り扱い易く
なる。その䞊緩衝性、断熱性を備えおいるため各
皮商品を包装する保護箱魚類、野菜、食肉等の
青鮮食料品を保冷茞送する容噚ヘルメツト、防
寒服、朜氎甚り゚ツトスヌツ等の保護衣服その
他各皮の保護䜓ずしお巟広く䜿甚されおいる。
Foamed synthetic resin molded products are advantageous in terms of cost because they can increase the expansion ratio, and at the same time, because they have a low density, the molded products are lightweight and extremely easy to handle. Protective boxes for packaging various products as they also have cushioning and insulation properties; Containers for transporting fresh foods such as fish, vegetables, and meat in cold storage; Protective clothing such as helmets, winter clothing, and diving wet suits; It is also widely used as a protective body for various other purposes.

しかし、これらの発泡成圢物は荷重負担胜力が
䜎いため重量の倧きな商品に察しおは䞍適圓であ
り、たた衚面匷床が䜎いため摩擊、衝突により容
易に砎損するこずが問題であ぀た。
However, these foamed molded products have a low load-bearing capacity, making them unsuitable for heavy products, and also have a problem of being easily damaged by friction or collision due to their low surface strength.

これらの問題点を改良するため衚面に薄い構造
材を接着しお剛性を高め、荷重負担胜力を増す方
法が行われおいるが、その方法が煩雑であり、耇
雑な圢状のものは量産が行えぬ䞊に加工費がかさ
むのが欠点であ぀た。たた成圢物の衚面に塗料を
塗り硬化也燥させる方法も行われおいるが、この
方法は硬化に長時間を芁する䞊に、硬化する前の
塗料が発泡合成暹脂を膚最させるこずがあり、甚
だしい堎合には溶解させる。さらに発泡合成暹脂
は䞀般に、その衚面に内郚の気泡ず連通した小孔
を有するため、塗料がその䞭に浞透し硬化した塗
膜にピンホヌルを生ずる。
In order to improve these problems, methods have been used to increase rigidity and load-bearing capacity by bonding thin structural materials to the surface, but this method is complicated and cannot be mass-produced for products with complex shapes. The disadvantage was that the processing cost was high. Another method is to apply paint to the surface of the molded product and let it harden and dry, but this method requires a long time to harden, and the paint before hardening can cause the foamed synthetic resin to swell. Dissolve in. Furthermore, since foamed synthetic resins generally have small pores on their surface that communicate with the air bubbles inside, the paint penetrates into the pores and causes pinholes in the cured coating.

圚来の方法には、この様な各皮の欠点を有する
ため、本発明者等はこれらの欠点を改良すべく
皮々怜蚎した結果、本発明に到達した。
Since the conventional methods have various drawbacks as described above, the present inventors conducted various studies to improve these drawbacks, and as a result, they arrived at the present invention.

即ち本発明は、発泡合成暹脂成圢物の倖面に、
䞋蚘垞枩硬化型高反応ポリりレタン源液を、高圧
吹付装眮を䜿甚し、30〜210Kgcm2の吐出圧で保
護䜓の衚面に吹き付けるこずを特城ずする発泡保
護䜓の匷化方法。
That is, the present invention provides the outer surface of the foamed synthetic resin molded product,
A method for strengthening a foamed protector, which comprises spraying the following room temperature curing highly reactive polyurethane source solution onto the surface of the protector at a discharge pressure of 30 to 210 kg/cm 2 using a high-pressure spraying device.

(A) ゞプニルメタンゞむ゜シアネヌト、ポリメ
チレンポリプニルポリむ゜シアネヌト又はそ
の倉性品の矀から遞ばれた皮又は皮以䞊の
混合物を含有しおなる䞻剀、 (B) 第䞀玚ヒドロキシル基を50以䞊含有し、か
぀、ヒドロキシル䟡が100mgKOH以䞋の高
分子ポリオヌルを50以䞊含有しおなる、ヒド
ロキシル䟡が10〜380mgKOHの硬化剀、 (C) 脂肪族又は芳銙族ポリアミン類、倚䟡アルコ
ヌル類たたはアルカノヌルアミン類の矀から遞
ばれた皮又は皮以䞊の混合物を含有しおな
る架橋剀、 (D) 第玚アミン類又は有機金属化合物の単独又
は皮以䞊の混合物からなる觊媒、 〜を、有機ポリむ゜シアネヌトのむ゜シア
ネヌト基ず、ポリオヌル及び架橋剀䞭の掻性氎玠
ずの圓量比NCOが、0.9〜1.30であり、
觊媒が、原料の総量〜に察しお0.001〜
重量配合しおなる垞枩硬化型高反応ポリりレ
タン原液。
(A) A base material containing one or a mixture of two or more selected from the group of diphenylmethane diisocyanate, polymethylene polyphenyl polyisocyanate, or modified products thereof; (B) 50% primary hydroxyl group; a curing agent with a hydroxyl value of 10 to 380 mgKOH/g, which contains 50% or more of a polymer polyol with a hydroxyl value of 100 mgKOH/g or less; (C) aliphatic or aromatic polyamines; a crosslinking agent containing one or a mixture of two or more selected from the group of alcohols or alkanolamines; (D) tertiary amines or organometallic compounds alone or in a mixture of two or more; The catalysts A to D have an equivalent ratio (NCO/H) of the isocyanate group of the organic polyisocyanate to the active hydrogen in the polyol and crosslinking agent of 0.9 to 1.30,
The catalyst is 0.001 to 0.001 to the total amount of raw materials (A to C)
Room temperature curing highly reactive polyurethane stock solution containing 5% by weight.

本発明によれば原液を高圧で吹付けるだけで衚
局が完成されるため、極めお簡易に発泡成圢物の
剛性を高め荷重負担胜力を増すこずができる。た
た耇雑な圢状の堎合にも簡単な䜜業で仕䞊げるこ
ずができるため量産が可胜ずなる。さらに本発明
においおは原液が十数秒で硬化するため、原液が
発泡成圢物を膚最、溶解或いは内郚ぞの浞透の危
険は殆んどなくなる。原液が硬化したりレタン゚
ラストマヌは匷床が高く、耐摩耗性が高いため摩
擊、衝突などによる保護䜓の砎損を防止できる。
According to the present invention, the surface layer can be completed simply by spraying the stock solution at high pressure, so that the rigidity of the foamed molded product can be extremely easily increased and the load-bearing capacity can be increased. Furthermore, even complex shapes can be finished with simple work, making mass production possible. Furthermore, in the present invention, since the stock solution hardens in more than ten seconds, there is almost no risk that the stock solution will swell, dissolve, or penetrate into the foamed molded article. The urethane elastomer obtained by hardening the raw solution has high strength and high wear resistance, so it can prevent damage to the protector due to friction, collisions, etc.

本発明においおは䟋えば、グラスクラフト瀟の
リムRIMシリヌズ及びプロプラヌ−3A、
ガスマヌ瀟のモデル−などの高圧吹付装眮を
䜿甚し、30〜210Kgcm2の吐出圧で保護䜓の衚面
にポリりレタン原液を吹付ける。りレタン゚ラス
トマヌの匷床を高めるにはポリりレタン原液の粘
床䞊昇を䌎うこずが倚いが、本発明によれば高粘
床の原液も埮粒子ずなり平滑な斜工面を埗るこず
ができる。たた通垞の䜎圧匏吹付装眮を䜿甚する
堎合に必芁な粘床䜎䞋甚溶剀は必芁ずしないた
め、回の吹付により厚塗ができるこずも本発明
の倧きな特城である。
In the present invention, for example, Glass Craft's RIM series and Propler T-3A,
Using a high-pressure spraying device such as Gasmer Model H-, the polyurethane stock solution is sprayed onto the surface of the protector at a discharge pressure of 30 to 210 kg/cm 2 . Increasing the strength of a urethane elastomer often involves increasing the viscosity of the polyurethane stock solution, but according to the present invention, even a highly viscous stock solution turns into fine particles, making it possible to obtain a smooth construction surface. Another major feature of the present invention is that it does not require a viscosity-reducing solvent, which is required when a normal low-pressure spraying device is used, so thick coating can be achieved with one spraying.

本発明に䜿甚する発泡合成暹脂は䟋えば、発泡
ポリスチレン、発泡ポリりレタン、発泡ポリ゚チ
レン、発泡プノヌル暹脂、スポンゞゎムなどで
ある。
Examples of the foamed synthetic resin used in the present invention include foamed polystyrene, foamed polyurethane, foamed polyethylene, foamed phenolic resin, and sponge rubber.

本発明に甚いる有機ポリむ゜シアネヌトは䟋え
ば、−トリレンゞむ゜シアネヌト、
−トリレンゞむ゜シアネヌト、及びその混合物
TDI、ゞプニルメタン−4′−ゞむ゜シア
ネヌトMDI、キシリレンゞむ゜シアネヌト
XDI、ゞシクロヘキシルメタン−4′−ゞむ
゜シアネヌト氎玠化MDI、む゜ホロンゞむ゜
シアネヌトIPDI、ヘキサメチレンゞむ゜シア
ネヌトHDI、氎玠化キシリレンゞむ゜シアネ
ヌトHXDI、粗補TDI、ポリメチレンポリフ
゚ニルポリむ゜シアネヌト粗補MDI、及びこ
れらのむ゜シアネヌト類のむ゜シアヌレヌト化倉
性品、カルボゞむミド化倉性品、ピナレツト化倉
性品などである。
The organic polyisocyanate used in the present invention is, for example, 2,4-tolylene diisocyanate, 2,6
-Tolylene diisocyanate and mixtures thereof (TDI), diphenylmethane-4,4'-diisocyanate (MDI), xylylene diisocyanate (XDI), dicyclohexylmethane-4,4'-diisocyanate (hydrogenated MDI), isophorone diisocyanate (IPDI) ), hexamethylene diisocyanate (HDI), hydrogenated xylylene diisocyanate (HXDI), crude TDI, polymethylene polyphenyl polyisocyanate (crude MDI), and isocyanurate-modified products, carbodiimidation-modified products of these isocyanates, and piuretsu. These include chemically modified products.

これらの有機ポリむ゜シアネヌトのうちMDI、
粗補MDI及びその倉性品がずくに奜たしい。
Among these organic polyisocyanates, MDI,
Crude MDI and its modified products are particularly preferred.

本発明に甚いるポリオヌルは氎、゚チレングリ
コヌル、プロピレングリコヌル、グリセリン、ト
リメチロヌルプロパン、ペンタ゚リスリトヌル等
の倚䟡アルコヌルに゚チレンオキサむド、プロピ
レンオキサむド、ブチレンオキサむド等のアルキ
レンオキサむドの皮又は皮以䞊を付加重合し
お埗たポリ゚ヌテルポリオヌルである。
The polyol used in the present invention is an addition polymerization of one or more alkylene oxides such as ethylene oxide, propylene oxide, and butylene oxide to polyhydric alcohols such as water, ethylene glycol, propylene glycol, glycerin, trimethylolpropane, and pentaerythritol. This is a polyether polyol obtained by

以䞊のほか、ポリカルボン酞ず䜎分子量ポリオ
ヌルずを反応させお埗たポリ゚ステルポリオヌル
及びカプロラクトンを重合させお埗たポリ゚ステ
ルポリオヌル、ヒマシ油等のOH基含有高玚脂肪
酞゚ステルも䜿甚できる。さらに前蚘の公知のポ
リ゚ヌテルポリオヌルないしポリ゚ステルポリオ
ヌルにアクリルニトリル、スチレン、メチルメタ
アクリレヌト等の゚チレン性䞍飜和化合物をグラ
フト重合させお埗たポリマヌポリオヌル及び
−もしくは−ポリブタゞ゚ンポリオヌル
たたはこれらの氎玠添加物も䜿甚できる。
In addition to the above, polyester polyols obtained by reacting polycarboxylic acids with low molecular weight polyols, polyester polyols obtained by polymerizing caprolactone, and higher fatty acid esters containing OH groups such as castor oil can also be used. Furthermore, a polymer polyol obtained by graft polymerizing an ethylenically unsaturated compound such as acrylonitrile, styrene, or methyl methacrylate to the above-mentioned known polyether polyol or polyester polyol;
2- or 1,4-polybutadiene polyols or hydrogenated products thereof can also be used.

その他䟋えば、ポリ゚チレンテレフタレヌト、
ポリブチレンテレフタレヌト等のアルキレンフタ
レヌト重合䜓を補造する工皋においお副生する蒞
留残枣、重合䜓そのもの、或いはその成圢品の廃
棄物を䞋蚘の架橋剀甚倚䟡アルコヌルず200〜280
℃に加熱し、゚ステル亀換を行぀お埗た芳銙族ポ
リ゚ステルポリオヌル組成物も本発明の極めお奜
たしい原料である。
Other examples include polyethylene terephthalate,
The distillation residue, the polymer itself, or the waste of its molded product, which is a by-product in the process of manufacturing alkylene phthalate polymers such as polybutylene terephthalate, is mixed with the following polyhydric alcohol for crosslinking agent and 200 to 280
Aromatic polyester polyol compositions obtained by heating to .degree. C. and transesterification are also highly preferred raw materials for the present invention.

ポリオヌルは単独たたは皮以䞊混合しお䜿甚
するが、ポリオヌルたたはその混合物のヒドロキ
シル䟡は10〜380mgKOHが奜たしく、20〜
180mgKOHがずくに奜たしい。反応性を高め
るためヒドロキシル䟡が100mgKOH以䞋の高
分子ポリオヌルのヒドロキシル基は第䞀玚ヒドロ
キシル基を50以䞊含むこずが望たしい。埓぀お
他䟡アルコヌルにプロピレンオキサむドたたはブ
チレンオキサむドを付加重合しお埗たポリ゚ヌテ
ルポリオヌルは末端を゚チレンオキサむドでキダ
ツプしたものが奜たしい。
The polyols may be used alone or in a mixture of two or more, and the hydroxyl value of the polyol or the mixture thereof is preferably 10 to 380 mgKOH/g, and preferably 20 to 380 mgKOH/g.
180 mg KOH/g is particularly preferred. In order to increase reactivity, it is desirable that the hydroxyl groups of the polymer polyol with a hydroxyl value of 100 mgKOH/g or less contain 50% or more of primary hydroxyl groups. Therefore, it is preferable that the polyether polyol obtained by addition polymerizing propylene oxide or butylene oxide to another alcohol has its terminal end capped with ethylene oxide.

たたポリ゚ステルポリオヌルの補造に䜿甚する
䜎分子量ポリオヌルは末端が第䞀玚ヒドロキシル
基であるこずが望たしい。
Further, it is desirable that the low molecular weight polyol used for producing the polyester polyol has a primary hydroxyl group at the end.

架橋材ずしおぱチレンゞアミン、ヘキサメチ
レンゞアミン、−プニレンゞアミン、
3′−ゞクロル−4′−ゞアミノゞプニルメタ
ン、3′−ゞメチル−4′−ゞアミノゞプ
ニルメタン、3′5′−テトラメチル−
4′−ゞアミノゞプニルメタン、−ゞ
゚チル−3′5′−ゞむ゜プロピルゞアミノゞプ
ニルメタン、3′5′−テトラむ゜プロピ
ルゞアミノゞプニルメタン等のポリアミン類、
゚チレングリコヌル、プロピレングリコヌル、ゞ
゚チレングリコヌル、ゞプロピレングリコヌル、
ブタンゞオヌル、ヘキサンゞオヌル、グリセリ
ン、トリメチロヌルプロパン等の倚䟡アルコヌル
類及びゞ゚タノヌルアミン、トリ゚タノヌルアミ
ン、プニルゞ゚タノヌルアミン、−−ヒ
ドロキシ゚トキシ゚チル−−−ヒドロキシ
゚チルアニリン、−ゞ−ヒドロキシ
゚トキシ゚チルアニリン、トリプロパノヌルア
ミン、プニルゞプロパノヌルアミン、−
ゞ−ヒドロキシプロポキシプロピルアニリ
ン等のアルカノヌルアミン類などを単独たたは混
合しお䜿甚する。
As a crosslinking material, ethylenediamine, hexamethylenediamine, p-phenylenediamine, 3,
3'-dichloro-4,4'-diaminodiphenylmethane, 3,3'-dimethyl-4,4'-diaminodiphenylmethane, 3,5,3',5'-tetramethyl-
Polyamines such as 4,4'-diaminodiphenylmethane, 3,5-diethyl-3',5'-diisopropyldiaminodiphenylmethane, 3,5,3',5'-tetraisopropyldiaminodiphenylmethane,
Ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol,
Polyhydric alcohols such as butanediol, hexanediol, glycerin, trimethylolpropane, diethanolamine, triethanolamine, phenyldiethanolamine, N-(2-hydroxyethoxyethyl)-N-(2-hydroxyethyl)aniline, N, N-di(2-hydroxyethoxyethyl)aniline, tripropanolamine, phenyldipropanolamine, N,N-
Alkanolamines such as di(2-hydroxypropoxypropyl)aniline are used alone or in combination.

有機ポリむ゜シアネヌト、ポリオヌル及び架橋
剀の䜿甚量は、有機ポリむ゜シアネヌト䞭の
NCO基ずポリオヌル及び架橋剀䞭の掻性氎玠ず
の圓量比NCOが0.90〜1.30ずなるように
する。
The amount of organic polyisocyanate, polyol and crosslinking agent used is
The equivalent ratio (NCO/H) between the NCO group and the active hydrogen in the polyol and crosslinking agent is adjusted to be 0.90 to 1.30.

本発明に甚いる觊媒は、䟋えば−メチルモル
ホリン、トリ゚チルアミン、トリ゚チレンゞアミ
ン、N′N′−テトラメチル・プロパン
ゞアミン、ビス−ゞメチルアミノ゚チル゚
ヌテル等の第玚アミン類、及びオクタン酞鉛、
ナフテン酞鉛、オクタン酞錫、ゞブチル錫ゞラり
レヌト等の有機金属化合物を単独たたは混合しお
䜿甚する。その䜿甚量は䜿甚原料の総量に察し
0.001〜重量が奜たしい。
The catalyst used in the present invention includes tertiary amines such as N-methylmorpholine, triethylamine, triethylenediamine, N,N,N',N'-tetramethylpropanediamine, and bis(2-dimethylaminoethyl)ether. , and lead octoate,
Organometallic compounds such as lead naphthenate, tin octoate, and dibutyltin dilaurate are used alone or in combination. The amount used is based on the total amount of raw materials used.
0.001 to 5% by weight is preferred.

本発明に甚い埗る他の助剀は可塑剀、充填剀、
安定剀、着色剀などである。
Other auxiliaries that can be used in the present invention include plasticizers, fillers,
Stabilizers, colorants, etc.

可塑剀ずしおは、䟋えば、フタル酞ゞオクチル
DOP、フタル酞ゞブチルDBP、アゞピン酞
ゞオクチルDOA、リン酞トリクレゞル
TCP、塩玠化パラフむン等である 充填剀ずしおは䟋えば、ガラス繊維、カヌボン
ブラツク、炭酞カルシりム、タルク、カオリン、
れオラむト、硅そう土、パヌラむト、バヌミキナ
ラむト、二酞化チタン等である。
Examples of plasticizers include dioctyl phthalate (DOP), dibutyl phthalate (DBP), dioctyl adipate (DOA), tricresyl phosphate (TCP), and chlorinated paraffin. Examples of fillers include glass fiber, Carbon black, calcium carbonate, talc, kaolin,
These include zeolite, diatomaceous earth, perlite, vermiculite, and titanium dioxide.

たた安定剀ずしおは䟋えば、商品名むルガノツ
クス1010及び1076チバガむギヌ瀟補、ペシノツ
クスBHT、BB及びGSY−930吉富補薬瀟補
などの䜍眮障害圢プノヌル類チヌビン、
327及び328チバガむギヌ瀟補等のベンゟトリ
アゟヌル類トミ゜ヌプ800吉富補薬瀟補など
のベンゟプノン類サノヌルLS−770及び744、
チヌビン144チバガむギヌ瀟補などの䜍眮障害
圢アミン類を䜿甚する。
Examples of stabilizers include trade names Irganox 1010 and 1076 (manufactured by Ciba Geigy), Yoshinox BHT, BB, and GSY-930 (manufactured by Yoshitomi Pharmaceutical Co., Ltd.).
Positionally hindered phenols such as tinuvin p,
Benzotriazoles such as 327 and 328 (manufactured by Ciba Geigy); benzophenones such as Tomisorp 800 (manufactured by Yoshitomi Pharmaceutical); Sanol LS-770 and 744;
Positionally hindered amines such as Tinuvin 144 (manufactured by Ciba Geigy) are used.

本発明を適甚するに圓り、ワンシペツト法、プ
レポリマヌ法の䜕れも䜿甚するこずができる。ワ
ンシペツト法で実斜する堎合には、有機ポリむ゜
シアネヌトはそのたた、たたは成分の流量比を調
節するため適圓量の可塑剀を混合し、成分ずす
る、ポリオヌル、架橋剀、觊媒、着色剀などを混
合し成分ずする。、䞡成分を所定の流量比
で高圧吹付装眮より噎出させ発泡成圢品ぞ吹付け
る。その際ガラス繊維を䜿甚する堎合にはガラス
長繊維をガンのヘツドの䜍眮で䞀定の長さに切断
しながら空気で吹付け、空䞭を飛ぶ間に、䞡
成分ず混合させる。成圢品ぞ付着した、䞡成
分の混合物は十数秒間で硬化する。必芁に応じこ
の操䜜を数回繰返し所定の長さの保護局ずする。
In applying the present invention, either the one-shot method or the prepolymer method can be used. When carrying out the one-shot method, the organic polyisocyanate is used as it is, or an appropriate amount of plasticizer is mixed to adjust the flow rate ratio of the components, and a polyol, a crosslinking agent, a catalyst, a coloring agent, etc. are mixed as component A. This is called the B component. Both components A and B are ejected from a high-pressure spray device at a predetermined flow rate ratio and sprayed onto the foam molded product. If glass fiber is used at this time, the long glass fiber is cut into a certain length at the head of the gun and blown with air, and mixed with both components A and B while flying through the air. The mixture of both components A and B that adheres to the molded article hardens in about ten seconds. This operation is repeated several times as necessary to form a protective layer of a predetermined length.

プレポリマヌ法で実斜する堎合には有機ポリむ
゜シアネヌトずポリオヌルたたは倚䟡アルコヌル
架橋剀の䞀郚を窒玠気流䞭70〜80℃で数時間反応
しお埗たプレポリマヌを液ずしお䜿甚する。以
䞋に実斜䟋を述べる。本発明で郚は重量郚を瀺
す。
When the prepolymer method is used, a prepolymer obtained by reacting an organic polyisocyanate and a part of a polyol or a polyhydric alcohol crosslinking agent at 70 to 80° C. for several hours in a nitrogen stream is used as liquid A. Examples will be described below. In the present invention, parts refer to parts by weight.

実斜䟋  NCO基含有量28.5重量のカルボゞむミド化
倉性した液状MDI、80郚、DOP20郚を窒玠気流
䞭で混合し成分ずした。この液のNCO含有
量は22.8重量ずな぀た。
Example 1 80 parts of carbodiimide-modified liquid MDI having an NCO group content of 28.5% by weight and 20 parts of DOP were mixed in a nitrogen stream to obtain component A. The NCO content of this liquid A was 22.8% by weight.

別にグリセリンにプロピレンオキサむド及び゚
チレンオキサむドを付加重合しお埗たヒドロキシ
ル䟡56mgKOH、第䞀玚ヒドロキシル基含有
量55重量のポリ゚ヌテルポリオヌル79郚、架橋
剀ずしお゚チレングリコヌル11郚及び−ゞ
−ヒドロキシプロポキシプロピルアニリン
郚、觊媒ずしおゞブチル錫ゞラりレヌト1.0郚
を混合し成分ずした。
Separately, 79 parts of a polyether polyol with a hydroxyl value of 56 mgKOH/g and a primary hydroxyl group content of 55% by weight obtained by addition polymerization of propylene oxide and ethylene oxide to glycerin, 11 parts of ethylene glycol as a crosslinking agent, and N,N- Component B was prepared by mixing 9 parts of di(2-hydroxypropoxypropyl)aniline and 1.0 part of dibutyltin dilaurate as a catalyst.

次にポリスチレンの予備発泡ビヌズをヘルメツ
トの型に入れ、加熱成圢し厚さ20mmの発泡成圢物
を䜜぀た。
Next, pre-expanded polystyrene beads were placed in a helmet mold and heated to form a foam molded product with a thickness of 20 mm.

プロブラ−−3A型高圧吹付装眮を䜿甚し、
䞊蚘のヘルメツト状発泡成圢物の倖偎に、䞡
成分を吐出圧190Kgcm2、流量比䜓積
で〜回吹付け塗装した。䞀時間攟眮すればヘ
ルメツトの衚面に厚さ玄mmの匷靫なポリりレタ
ン゚ラストマヌ局ができた。、䞡成分混合物
のNCO圓量比は1.05ずな぀た。
Using Probler T-3A type high pressure spray equipment,
Both components A and B were discharged to the outside of the above helmet-shaped foam molding at a pressure of 190 kg/cm 2 and a flow rate ratio (volume) of 1:1.
I spray painted it 3-4 times. After leaving it for one hour, a strong polyurethane elastomer layer approximately 2 mm thick was formed on the surface of the helmet. The NCO/H (equivalent ratio) of the mixture of both components A and B was 1.05.

このヘルメツトの衚面を金槌でたたくず、金槌
がはね返されヘルメツトは砎損しなか぀た。これ
に察し塗装しおいない発泡成圢物は同䞀操䜜によ
り容易に砎損した。
When the surface of this helmet was struck with a hammer, the hammer was bounced back and the helmet remained undamaged. On the other hand, the unpainted foamed molded product was easily damaged by the same operation.

実斜䟋  グリセリンにプロピレンオキサむド及び゚チレ
ンオキサむドを付加重合させお埗たヒドロキシル
䟡55mgKOH、第䞀玚ヒドロキシル基含有量
90重量のポリ゚ヌテルポリオヌル55郚、゚チレ
ングリコヌルにプロピレンオキサむドを付加重合
させお埗たヒドロキシル䟡280mgKOHのポリ
゚ヌテルポリオヌル20郚、゚チレングリコヌル架
橋剀10郚、ゞブチル錫ゞラりレヌト觊媒0.8郚、
着色剀14.2郚を混合し成分ずした。
Example 2 Hydroxyl value 55 mgKOH/g, primary hydroxyl group content obtained by addition polymerizing propylene oxide and ethylene oxide to glycerin
55 parts of a 90% by weight polyether polyol, 20 parts of a polyether polyol with a hydroxyl value of 280 mg KOH/g obtained by addition polymerizing propylene oxide to ethylene glycol, 10 parts of an ethylene glycol crosslinker, 0.8 parts of a dibutyltin dilaurate catalyst,
14.2 parts of colorant was mixed to obtain component B.

別にNCO基含有量28.5重量の倉性MDI䞉井
日曹りレタン瀟補MDI−LK70郚、MDI䞉
井日曹りレタン瀟補MDI−PH15郚、ゞプロ
ピレングリコヌル架橋剀郚、DOP10郚を混合
し、窒玠気流䞭70℃で3.5時間反応させお埗たプ
レポリマヌを成分ずした。成分のNCO含有
量は21重量ずな぀た。
Separately, 70 parts of modified MDI (manufactured by Mitsui Nisso Urethane Co., Ltd.: MDI-LK) with an NCO group content of 28.5%, 15 parts of MDI (manufactured by Mitsui Nisso Urethane Co., Ltd.: MDI-PH), 5 parts of dipropylene glycol crosslinking agent, A prepolymer obtained by mixing 10 parts of DOP and reacting at 70° C. for 3.5 hours in a nitrogen stream was used as component A. The NCO content of component A was 21% by weight.

次にポリスチレンの発泡ビヌズを金型に入れ加
熱成圢し、運搬箱を䜜぀た。
Next, polystyrene foam beads were placed in a mold and heated to form a transport box.

、䞡成分を実斜䟋ず同䞀条件により運搬
箱の内倖䞡面に吹付塗装した。この際、䞡成
分混合物のNCO圓量比は1.05ずな぀た。
Both components A and B were spray-coated on both the inside and outside surfaces of the transport box under the same conditions as in Example 1. At this time, the NCO/H (equivalent ratio) of the mixture of both components A and B was 1.05.

この塗装運搬箱に魚類ず砎砕氷を詰め、長距離
茞送を反埩実斜したが、運搬箱は内倖䞡面ずも砎
損及び傷は党く認められなか぀た。これに察し塗
装しない運搬箱は内倖䞡面ずも倚数の凹み及び傷
を生じた。
This painted transport box was filled with fish and crushed ice and repeatedly transported over long distances, but no damage or scratches were observed on either the inside or outside of the transport box. On the other hand, the unpainted transport box had numerous dents and scratches on both the inside and outside surfaces.

実斜䟋  撹拌機、枩床蚈、還流コンデンサヌを備えた
ツ口フラスコにポリ゚チレンテレフタレヌトのチ
ツプ1000郚、ゞ゚チレングリコヌル1000郚を入
れ、撹拌し぀぀埐々に加熱し240℃たで昇枩した。
ポリ゚チレンテレフタレヌトが溶融し、゚チレン
グリコヌルずゞ゚チレングリコヌルの混合物が還
流するが、同枩床に保持し぀぀時間反応を続け
た埌、宀枩たで冷华し排出した。埗られたポリ゚
ステルポリオヌル組成物はヒドロキシル䟡370mg
KOHであ぀た。このポリ゚ステルポリオヌ
ル100郚に觊媒ずしおゞブチル錫ゞラりレヌト0.6
郚を添加し成分ずした。
Example 3 4 equipped with stirrer, thermometer and reflux condenser
1,000 parts of polyethylene terephthalate chips and 1,000 parts of diethylene glycol were placed in a two-necked flask, and the mixture was gradually heated to 240°C while stirring.
The polyethylene terephthalate melted and the mixture of ethylene glycol and diethylene glycol refluxed. After continuing the reaction for 7 hours while maintaining the same temperature, it was cooled to room temperature and discharged. The resulting polyester polyol composition has a hydroxyl value of 370 mg.
It was KOH/g. 0.6 dibutyltin dilaurate as a catalyst to 100 parts of this polyester polyol
% was added to obtain component B.

別にNCO基含有量30.5重量の粗補MDI95.4
郚、DBP5.2郚を窒玠気流䞭で混合し成分ずし
た。
Apart from crude MDI95.4 with NCO group content 30.5% by weight
1 part and 5.2 parts of DBP were mixed in a nitrogen stream to obtain component A.

次に発泡プノヌル暹脂のブロツクから所定の
寞法を有する厚板を鋞を甚いお切り出し、これを
接着剀を䜿甚しお組立お運搬箱を䜜぀た。
Next, thick plates having predetermined dimensions were cut out from the foamed phenolic resin block using a saw, and the plates were assembled using adhesive to form a transportation box.

この運搬箱の内面に、、䞡成分を吐出圧
190Kgcm2、流量比䜓積で数回吹付け
塗装し厚さ玄1.5mmの被膜を䜜぀た。この際、
䞡成分混合物䞭のHCO圓量比は1.05で
あ぀た。
Both A and B components are discharged onto the inner surface of this transport box.
It was sprayed several times at a flow rate of 190 kg/cm 2 and a flow rate (volume) of 1:1 to form a film approximately 1.5 mm thick. At this time, A,
The HCO/H (equivalent ratio) in the mixture of both components B was 1.05.

この塗装運搬箱に魚類を詰め、長距離茞送を行
぀たが魚類には䜕ら倉化が認められなか぀た。こ
れに察し未塗装の運搬箱を䜿甚した堎合には、茞
送䞭の振動による魚䜓ずの摩擊のため、発泡プ
ノヌル暹脂の埮小な砎片が発生し魚䜓を汚染し
た。
Fish were packed in this painted transport box and transported over long distances, but no changes were observed in the fish. On the other hand, when an unpainted transport box was used, minute fragments of foamed phenolic resin were generated due to friction with the fish bodies due to vibrations during transportation, contaminating the fish bodies.

比范䟋  加熱硬化甚りレタン暹脂を甚いおスプレヌを行
぀た。液のむ゜シアネヌト成分はハむプレン
−100䞉井東圧化孊瀟補のプレポリマヌで、
NCO4.2、粘床22000cp25℃を䜿甚し
たが、粘床が高く、このたたではスプレヌ出来な
いため、−100638郚に酢酞゚チル362郚
を加えお調敎した。液の硬化剀は、4′−ゞ
アミノ−3′−ゞクロロゞプニルメタン
125郚をメシチルオキシド875郚に溶解し
お䜿甚した。䞡者の配合比は、液液
10064郚、䞡成分のNCO圓量比は
1.05ずし、成圢マシンはビンクス瀟のモデル
型に43Pガンを取り付け、垞枩で液圧力を20Kg
cm2の条件で、発泡ポリスチレン補の魚箱の衚面に
吹き付けた。その結果、含有されおいる溶剀によ
り、発泡ポリスチレンが溶解しおしたい、衚面に
膜を圢成するこずが出来なか぀た。
Comparative Example 1 Spraying was performed using a heat-curing urethane resin. The isocyanate component of liquid A is Hypren L.
-100 (prepolymer manufactured by Mitsui Toatsu Chemical Co., Ltd.
NCO% = 4.2, viscosity = 22000cp/25℃) was used, but the viscosity was high and it could not be sprayed as it was, so ethyl acetate (362 parts) was added to L-100 (638 parts).
Adjusted by adding. As a curing agent for liquid B, 4,4'-diamino-3,3'-dichlorodiphenylmethane (125 parts) was dissolved in mesityl oxide (875 parts). The blending ratio of both is A liquid/B liquid =
100/64 parts (NCO/H equivalent ratio of both components A and B is
1.05), and the molding machine is Binks Model G.
Attach a 43P gun to the mold and increase the liquid pressure to 20Kg/at room temperature.
It was sprayed onto the surface of a fish box made of expanded polystyrene at cm 2 conditions. As a result, the foamed polystyrene was dissolved by the solvent contained therein, making it impossible to form a film on the surface.

別途、塗膜を埗るため、ポリプロピレンの板䞊
非発泡䜓に積局しおシヌトを䜜成したが、溶
剀を揮発させるため、0.25mmの厚さで、25分間
垞枩也燥させ、ゲル化を確認しながら回行
い、その埌、100℃で時間硬化させる必芁があ
り、䜜業が非垞に煩雑であ぀た。
Separately, in order to obtain a coating film, a sheet was created by laminating it on a polypropylene board (non-foamed material), but in order to volatilize the solvent, it was dried to a thickness of 0.25 mm for 25 minutes (at room temperature) and gelled. It was necessary to repeat the process 5 times while checking the conditions, and then to cure at 100°C for 3 hours, which was a very complicated process.

Claims (1)

【特蚱請求の範囲】  発泡合成暹脂成圢物の倖面に、䞋蚘垞枩硬化
型高反応ポリりレタン原液を、高圧吹付装眮を䜿
甚し、30〜210Kgcm2の吐出圧で保護䜓の衚面に
吹き付けるこずを特城ずする発泡保護䜓の匷化方
法。 (A) ゞプニルメタンゞむ゜シアネヌト、ポリメ
チレンポリプニルポリむ゜シアネヌト又はそ
の倉性品の矀から遞ばれた皮又は皮以䞊の
混合物を含有しおなる䞻剀、 (B) 第䞀玚ヒドロキシル基を50以䞊含有し、か
぀、ヒドロキシル䟡が100mgKOH以䞋の高
分子ポリオヌルを50以䞊含有しおなる、ヒド
ロキシル䟡が10〜380mgKOHの硬化剀、 (C) 脂肪族又は芳銙族ポリアミン類、倚䟡アルコ
ヌル類たたはアルカノヌルアミン類の矀から遞
ばれた皮又は皮以䞊の混合物を含有しおな
る架橋剀、 (D) 第玚アミン類又は有機金属化合物の単独又
は皮以䞊の混合物からなる觊媒、 〜を、有機ポリむ゜シアネヌトのむ゜シア
ネヌト基ず、ポリオヌル及び架橋剀䞭の掻性氎玠
ずの圓量比NCOが、0.9〜1.30であり、
觊媒が、原料の総量〜に察しお0.001〜
重量配合しおなる垞枩硬化型高反応ポリりレ
タン原液。
[Claims] 1. Spraying the following cold-curing highly reactive polyurethane stock solution onto the outer surface of the foamed synthetic resin molding onto the surface of the protector using a high-pressure spraying device at a discharge pressure of 30 to 210 kg/cm 2 . A method for strengthening a foam protector characterized by: (A) A base material containing one or a mixture of two or more selected from the group of diphenylmethane diisocyanate, polymethylene polyphenyl polyisocyanate, or modified products thereof; (B) 50% primary hydroxyl group; a curing agent with a hydroxyl value of 10 to 380 mgKOH/g, which contains 50% or more of a polymer polyol with a hydroxyl value of 100 mgKOH/g or less; (C) aliphatic or aromatic polyamines; a crosslinking agent containing one or a mixture of two or more selected from the group of alcohols or alkanolamines; (D) tertiary amines or organometallic compounds alone or in a mixture of two or more; The catalysts A to D have an equivalent ratio (NCO/H) of the isocyanate group of the organic polyisocyanate to the active hydrogen in the polyol and crosslinking agent of 0.9 to 1.30,
The catalyst is 0.001 to 0.001 to the total amount of raw materials (A to C)
Room temperature curing highly reactive polyurethane stock solution containing 5% by weight.
JP59003506A 1984-01-13 1984-01-13 Method of reinforcing expanded protective body Granted JPS60147329A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59003506A JPS60147329A (en) 1984-01-13 1984-01-13 Method of reinforcing expanded protective body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59003506A JPS60147329A (en) 1984-01-13 1984-01-13 Method of reinforcing expanded protective body

Publications (2)

Publication Number Publication Date
JPS60147329A JPS60147329A (en) 1985-08-03
JPH0367107B2 true JPH0367107B2 (en) 1991-10-21

Family

ID=11559239

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59003506A Granted JPS60147329A (en) 1984-01-13 1984-01-13 Method of reinforcing expanded protective body

Country Status (1)

Country Link
JP (1) JPS60147329A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09221628A (en) * 1996-02-14 1997-08-26 Nippon Synthetic Chem Ind Co Ltd:The Two-pack solventless urethane-based resin coating agent
JP4695452B2 (en) * 2005-07-22 2011-06-08 株匏䌚瀟むノアックコヌポレヌション Cleaning tool manufacturing method and manufacturing apparatus

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3715014B2 (en) * 1995-12-25 2005-11-09 日本合成化孊工業株匏䌚瀟 Two-component solventless urethane resin coating agent
US20060091574A1 (en) * 2004-11-03 2006-05-04 Lear Corporation Interior vehicle trim panel having a sprayed expanded polyurethane layer and method and system of making same
JP5366120B2 (en) * 2008-08-11 2013-12-11 シンゞヌテック株匏䌚瀟 Manufacturing method of rubber member

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56130324A (en) * 1980-03-18 1981-10-13 Achilles Corp Blow foaming method of hard urethane foam by air spray foaming
JPS58110238A (en) * 1981-12-24 1983-06-30 利郚 靖圊 Surface coating of foamed body

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56130324A (en) * 1980-03-18 1981-10-13 Achilles Corp Blow foaming method of hard urethane foam by air spray foaming
JPS58110238A (en) * 1981-12-24 1983-06-30 利郚 靖圊 Surface coating of foamed body

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09221628A (en) * 1996-02-14 1997-08-26 Nippon Synthetic Chem Ind Co Ltd:The Two-pack solventless urethane-based resin coating agent
JP4695452B2 (en) * 2005-07-22 2011-06-08 株匏䌚瀟むノアックコヌポレヌション Cleaning tool manufacturing method and manufacturing apparatus

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