JPS6149328B2 - - Google Patents
Info
- Publication number
- JPS6149328B2 JPS6149328B2 JP57151894A JP15189482A JPS6149328B2 JP S6149328 B2 JPS6149328 B2 JP S6149328B2 JP 57151894 A JP57151894 A JP 57151894A JP 15189482 A JP15189482 A JP 15189482A JP S6149328 B2 JPS6149328 B2 JP S6149328B2
- Authority
- JP
- Japan
- Prior art keywords
- mixture
- melamine
- polymethylene polyphenyl
- polyphenyl isocyanate
- heat
- 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
Links
Landscapes
- Polyurethanes Or Polyureas (AREA)
Description
本発明はポリメチレンポリフエニルイソシアネ
ートとメラミン及び/又はグアナミンとの反応を
利用した耐熱性熱硬化性樹脂の製造方法に関する
ものである。
従来より、有機ポリイソシアネートと2以上の
活性水素を有する化合物とが付加重合するという
ことは知られており、広く高分子化合物の製造に
利用されている。即ち、例えば、有機ポリイソシ
アネートは多価アルコール類と反応してポリウレ
タンを生じ、ポリアミンと反応してポリ尿素を生
ずる等、この二種類の化合物の反応は種々に組合
わされてポリウレタンの総称に包含される有用な
高分子物質群を形成する。
更に、まれではあるが、有機ポリイソシアネー
トと多価有機との反応によつて生ずるアミド結合
が、上記ポリウレタン類の改質のために利用され
る場合もある。
一方、アミノトリアジン類も遊離アミノ基に活
性水素を持つ化合物であるが、これまで有機ポリ
イソシアネートとアミノトリアジン類との反応に
より高分子物質が製造された例は少ない。
本発明の発明者らは、上述した事情を背景とし
て新たな耐熱性熱硬化性樹脂の製造方法を提供す
るための研究を重ねた結果、アミノトリアジン類
をポリメチレンポリフエニルイソシアネートと共
に加熱すると、一旦固化し、これを更に加熱して
硬化させれば極めて硬質で不溶不融の縮合物を生
成することを知得して本発明を完成させたもの
で、本発明の製造方法は、ポリメチレンポリフエ
ニルイソシアネートとメラミン及び/又はグアナ
ミンを加熱下に反応させることを特徴とするもの
である。
次に本発明について詳細に説明する。
まずポリメチレンポリフエニルイソシアネート
とメラミン及び/又はグアナミンとを常温におい
て充分混合する。
この混合は適当な混合分散機、例えばボールミ
ル、サンドミル、ホモジナイザー等を用いるが、
可能な限りメラミン及び/又はグアナミンをポリ
メチレンポリフエニルイソシアネートに微粒子と
して均一に分散させる必要がある。混合に際して
の両者の比率は広範囲に変えることができ、イソ
シアネート基1グラム当量に対しメラミン及び/
又はグアナミンは遊離アミノ基で0.5乃至5グラ
ム当量の範囲で選択可能で、これをイソシアネー
ト基に対する遊離アミノ基の当量比指数をγとす
れば、γ=0.5〜5となり、γ<0.5では得られる
耐熱性熱硬化性樹脂の収率が低過ぎ、γ>5では
該樹脂の強度が低下する。アミノトリアジンはそ
れぞれ単独で用いても、二種以上の混合物であつ
ても良い。
得られた分散混合物は常温でかなり安定であ
り、例えばポリメチレンポリフエニルイソシアネ
ートにメラミンを充分微細に分散した混合物はス
ラリー状で数週間にわたつて固液分離を生じない
等、常温付近ではほとんど反応しない。又、ポリ
メチレンポリフエニルイソシアネートと置換アミ
ノトリアジンの分散混合物も数日間から数週間安
定であるが、ポリメチレンポリフエニルイソシア
ネートとベンゾグアナミンとの分散混合物は、数
日間は液状を保つが徐々に粘度が上昇し、2週間
後には極めて粘稠となる。
次に前記スラリー状の分散混合物を加熱し反応
させるのであるが、加熱温度やその態様により、
得られる樹脂は若干相違した性質を示す。
即ち、前記スラリー状混合物を適当な型に注入
し加熱器中で加熱すると、混合物の粘度は温度の
上昇とともに減少するが、一定の温度に達すると
急速に粘度が上昇し硬化して樹脂が得られるので
あり、この硬化するに至る温度は分散混合物の成
分種類によつて異なり、例えばポリメチレンポリ
フエニルイソシアネートとメラミンとの混合物は
125℃乃至135℃であり、ポリメチレンポリフエニ
ルイソシアネートとベンゾグアナミンとの混合物
は40℃乃至50℃から徐々に粘度が上昇し、80℃で
硬化するが、これらより低い温度であつても加熱
時間を長くすれば硬化させることができる。
上記温度により得られた樹脂は褐色で、顕微鏡
下ではもはやアミノトリアジンの結晶は認められ
ず、従つてポリフエニルイソシアネートとメラミ
ン及び/又はベンゾグアナミンとの低分子重合物
と思われ、金属物で表面を強くこすつても傷の付
かない程度の硬度と、直接火炎にさらしても軟化
溶融しない程度の耐熱性とを有している。尚、こ
の樹脂を急速に冷却すると非常にもろいワツクス
状を呈するが、通常のワツクスと異なり加熱下に
溶融することはない。
又、上記のようにして得られた耐熱性熱硬化性
樹脂を180℃乃至250℃の温度で数分間乃至数十時
間キユアーしたり、前記スラリー状混合物を直接
180℃乃至250℃の温度に加熱することにより、極
めて硬質の樹脂を得ることができ、このようにし
て得られた樹脂は熱的に非常に安定で、空気中
200℃乃至250℃の温度では樹脂層に薄い炭化膜を
形成するが、数十時間にわたつて実質的な熱分解
は認められず、直接火炎に接しても着火性がなく
燃焼もしない。
更に前記温度により得られた樹脂を300℃以上
に加熱したり、前記スラリー状混合物をこの温度
に加熱したりすると、わずかに軟化して主として
水分と思われるガスを放出しつつ若干発泡し、再
び硬化して黄色を呈し、非常に優れた耐熱性を示
す樹脂が得られる。350℃で2時間処理した当該
樹脂は第2図に示すように、300℃乃至350℃及至
350℃に至るまで毎分5℃の昇温速度での熱重量
分析においてほとんど重量減少を示さないもので
ある。
而して、本発明により得られる樹脂は如何なる
加熱温度による場合もすべての溶媒に対し不溶で
あり、典型的な熱硬化性樹脂ということができ、
所望の形状の型内に注型したり、加熱装置を通し
て閉鎖型内に注入固化したり、又、連続板状に固
化せしめることが可能で、加熱工程は常圧下で行
なつても加圧下で行なつても良いが、加圧下で行
なえば緻密な構造のものが得やすい。
又、この樹脂にガラス繊維、石綿のような繊維
状強化材や酸化チタン、炭酸カルシウム、クレ
イ、タルク、シリカ粉末等の無機充填材、ポリフ
ワ化炭素樹脂粉末、アミノ樹脂縮合物粉末、木粉
等の有機充填材を配合することにより、その性質
を好しいものに変えることができる。ただし、こ
れらの強化材は少なくとも150℃以上の耐熱性を
有するものが望ましい。
更に、ポリメチレンポリフエニルイソシアネー
トとメラミン及び/又はベンゾグアナミンの混合
物に発泡剤を加えて加熱すれば、前記樹脂による
発泡体を製造することもできる。例えば、混合物
にアゾビスイソプチロニトリル、ジニトロソペン
タメチレンテトラミンや炭酸水素ナトリウムのよ
うに発泡剤を配合しておき加熱して発泡させ、次
いでこれを加熱キユアーすることによりほとんど
不燃の発泡体が得られる如くである。又、有機ポ
リイソシアネートに対し反応当量以下の水を配合
して加熱することにより発泡せしめ、次いでこれ
を加熱キユアーしてもよく、いずれの方法による
も、本発明により得られた発泡体は耐熱性で難燃
乃至不燃性を有し、直接炎に接してもほとんど発
煙しない。
このようにして得られた耐熱性熱硬化性樹脂は
硬質の耐熱、耐炎性材料として極めて有用であ
り、この優れた特性を利用して、耐熱性、難燃性
の建築材料や断熱材として、又、ブレーキライニ
ングやクラツチフエーシング等の摩擦材として用
いることができ、更に、シエルモード用硅砂のバ
インダーとしても、木材フレークと混合してパー
テイクルボードを製造するのに用いても好適であ
る。
以下、実施例により本発明を具体的に説明す
る。
実施例 1
ポリメチレンポリフエニルイソシアネート1120
グラム(8グラム当量)とメラミン340グラム
(8グラム当量)とを磁製ポツトミルに仕込み、
磁製ボール2000グラムとともに18時間粉砕分散
し、褐色のスラリー状混合物1を得た。粘度は
680cpsであつた。
このスラリー状混合物1を165℃に調節した平
滑な金型上に少量滴下すると、30秒後にワツクス
状固形物となり、120秒後には金属ヘラで表面を
強くこすつても傷のつかない程度に硬化し、この
ものをバーナーの炎にさらしても軟化溶融の現象
はみられなかつた。
実施例 2
ポリメチレンポリフエニルイソシアネート1120
グラム(8グラム当量)とメラミン605グラム
(14.2グラム当量)とを磁製ポツトミルに仕込
み、磁製ボール2200グラムとともに18時間粉砕分
散し、褐色のスラリー状混合物2を得た。粘度は
1500cpsであつた。
このスラリー状混合物2を165℃に調節した平
滑な金型上に少量滴下すると、20秒後にワツクス
状固形物となり、60秒後には金属ヘラで表面を強
くこすつても傷のつかない程度に硬化し、このも
のをバーナーの炎にさらしても軟化溶融の現象は
みられなかつた。
実施例 3
ポリメチレンポリフエニルイソシアネート1120
g(8グラム当量)とベンゾグアナミン748g
(8グラム当量)とを磁製ポツトミルに仕込み、
磁製ボール2000gとともに18時間粉砕分散し、褐
色のスラリー状混合物3を得た。粘度は800cps
であつた。このスラリー状混合物3を165℃に調
節した平滑な金型上に少量滴下すると、60秒後に
ワツクス状固形物となり、180秒後には金属ヘラ
で表面を強くこすつても傷のつかない程度に硬化
し、このものをバーナーの炎にさらしても軟化溶
融の現象はみられなかつた。
実施例 4
ポリメチレンポリフエニルイソシアネート1120
g(8グラム当量)とメラミン170g(4グラム
当量)とベンゾグアナミン374g(4グラム当
量)とを磁製ポツトミルに仕込み、磁製ボール
2000gとともに18時間粉砕分散し、褐色のスラリ
ー状混合物4を得た。粘度は720cpsであつた。
このスラリー状混合物4を165℃に調節した平滑
な金型上に少量滴下すると、50秒後にワツクス状
固形物となり、180秒後には金属ヘラで表面を強
くこすつても傷のつかない程度に硬化し、このも
のをバーナの炎にさらしても軟化溶融の現象はみ
られなかつた。
上記実施例1及び実施例2に於けるスラリー状
混合物1,2を20℃及び40℃の温度においた場合
の粘度変化は第1図に示す通りである。
実施例 5
実施例1,2,3及び4に於けるスラリー状混
合物1,2,3,4を、165℃に温度調節された
乾燥機中で予め加熱された金型中に流し込み、同
時に蓋をして、そのまま乾燥機中で1時間加熱を
続け、板状成型品を得た。このものの物性は表1
に示す通りである。
The present invention relates to a method for producing a heat-resistant thermosetting resin using a reaction between polymethylene polyphenyl isocyanate and melamine and/or guanamine. BACKGROUND ART Conventionally, it has been known that an organic polyisocyanate undergoes addition polymerization with a compound having two or more active hydrogens, and is widely used in the production of polymer compounds. That is, for example, organic polyisocyanate reacts with polyhydric alcohols to produce polyurethane, and reacts with polyamine to produce polyurea, and the reactions of these two types of compounds are combined in various ways and are included in the general term polyurethane. Forms a group of useful polymeric substances. Furthermore, although rare, amide bonds produced by the reaction between organic polyisocyanates and polyvalent organic compounds are sometimes used to modify the polyurethanes mentioned above. On the other hand, aminotriazines are also compounds having an active hydrogen in a free amino group, but there have been few examples of producing polymeric substances by reacting organic polyisocyanates with aminotriazines. The inventors of the present invention have repeatedly conducted research to provide a new method for producing heat-resistant thermosetting resins against the background of the above-mentioned circumstances. The present invention was completed based on the knowledge that an extremely hard, insoluble and infusible condensate can be produced by solidifying and further heating and curing the condensate. This method is characterized by reacting enyl isocyanate with melamine and/or guanamine under heating. Next, the present invention will be explained in detail. First, polymethylene polyphenyl isocyanate and melamine and/or guanamine are thoroughly mixed at room temperature. This mixing uses a suitable mixing/dispersing machine such as a ball mill, sand mill, homogenizer, etc.
It is necessary to disperse melamine and/or guanamine as fine particles as uniformly as possible in the polymethylene polyphenyl isocyanate. The ratio of the two during mixing can vary within a wide range; melamine and/or
Alternatively, guanamine can be selected in the range of 0.5 to 5 gram equivalents of free amino groups, and if the equivalent ratio index of free amino groups to isocyanate groups is γ, then γ = 0.5 to 5, and when γ < 0.5, it is obtained. The yield of the heat-resistant thermosetting resin is too low, and when γ>5, the strength of the resin decreases. Aminotriazines may be used alone or in a mixture of two or more. The resulting dispersion mixture is quite stable at room temperature; for example, a mixture of sufficiently finely dispersed melamine in polymethylene polyphenyl isocyanate remains in the form of a slurry without solid-liquid separation for several weeks, and hardly reacts at room temperature. do not. Also, a dispersion mixture of polymethylene polyphenyl isocyanate and substituted aminotriazine is stable for several days to several weeks, whereas a dispersion mixture of polymethylene polyphenyl isocyanate and benzoguanamine remains liquid for several days, but gradually increases in viscosity. However, it becomes extremely viscous after two weeks. Next, the slurry-like dispersion mixture is heated and reacted, but depending on the heating temperature and its mode,
The resulting resins exhibit slightly different properties. That is, when the slurry-like mixture is poured into a suitable mold and heated in a heater, the viscosity of the mixture decreases as the temperature rises, but when it reaches a certain temperature, the viscosity rapidly increases and hardens to obtain a resin. The temperature at which this curing occurs depends on the type of components of the dispersion mixture. For example, a mixture of polymethylene polyphenyl isocyanate and melamine
The temperature is 125°C to 135°C, and the viscosity of the mixture of polymethylene polyphenyl isocyanate and benzoguanamine gradually increases from 40°C to 50°C, and it hardens at 80°C, but even at lower temperatures, the heating time is You can harden it by making it longer. The resin obtained at the above temperature was brown in color, and no aminotriazine crystals were observed under the microscope. Therefore, it seems to be a low-molecular polymer of polyphenyl isocyanate and melamine and/or benzoguanamine, and the surface was coated with a metal object. It has a hardness that does not cause scratches even when rubbed vigorously, and a heat resistance that does not soften or melt even when exposed to direct flame. Note that when this resin is rapidly cooled, it takes on the form of a very brittle wax, but unlike ordinary wax, it does not melt when heated. Alternatively, the heat-resistant thermosetting resin obtained as described above may be cured at a temperature of 180°C to 250°C for several minutes to several tens of hours, or the slurry mixture may be cured directly.
Extremely hard resins can be obtained by heating to temperatures between 180°C and 250°C, and the resins thus obtained are very thermally stable and do not survive in air.
At temperatures of 200°C to 250°C, a thin carbonized film is formed on the resin layer, but no substantial thermal decomposition is observed over several tens of hours, and even if it comes into direct contact with flame, it has no ignitability and does not burn. Furthermore, when the resin obtained at the above temperature is heated to 300°C or higher, or when the slurry mixture is heated to this temperature, it softens slightly and foams slightly while releasing gas that is thought to be mainly water. When cured, a resin that exhibits a yellow color and excellent heat resistance is obtained. As shown in Figure 2, the resin treated at 350°C for 2 hours has a temperature range of 300°C to 350°C.
It shows almost no weight loss in thermogravimetric analysis at a heating rate of 5°C per minute up to 350°C. Therefore, the resin obtained by the present invention is insoluble in all solvents at any heating temperature, and can be said to be a typical thermosetting resin.
It can be poured into a mold of a desired shape, poured into a closed mold through a heating device, and solidified, or solidified into a continuous plate.The heating process can be performed under normal pressure or under pressure. Although this may be carried out, it is easier to obtain a dense structure if carried out under pressure. Additionally, this resin may be supplemented with fibrous reinforcing materials such as glass fiber and asbestos, inorganic fillers such as titanium oxide, calcium carbonate, clay, talc, and silica powder, polyfluorinated carbon resin powder, amino resin condensate powder, wood flour, etc. By adding an organic filler, its properties can be changed to favorable ones. However, it is desirable that these reinforcing materials have a heat resistance of at least 150°C or higher. Furthermore, by adding a foaming agent to a mixture of polymethylene polyphenyl isocyanate and melamine and/or benzoguanamine and heating the mixture, a foamed body using the resin can also be produced. For example, by adding a foaming agent such as azobisisobutylonitrile, dinitrosopentamethylenetetramine, or sodium bicarbonate to the mixture, heating and foaming the mixture, and then heat-curing this, a nearly non-flammable foam can be obtained. It's like it's being done. Alternatively, the organic polyisocyanate may be foamed by mixing water in an amount equal to or less than the reaction equivalent, and then heating and curing the resultant mixture. It is flame retardant or non-combustible, and produces almost no smoke even if it comes in direct contact with flame. The heat-resistant thermosetting resin obtained in this way is extremely useful as a hard heat-resistant and flame-resistant material, and by utilizing this excellent property, it can be used as a heat-resistant and flame-retardant building material and insulation material. It can also be used as a friction material for brake linings, clutch facings, etc. It is also suitable for use as a binder for silica sand for shell mode, and for manufacturing particle board by mixing with wood flakes. Hereinafter, the present invention will be specifically explained with reference to Examples. Example 1 Polymethylene polyphenyl isocyanate 1120
(8 grams equivalent) and 340 grams (8 grams equivalent) of melamine were placed in a porcelain pot mill.
The mixture was pulverized and dispersed for 18 hours with 2000 grams of porcelain balls to obtain a brown slurry mixture 1. The viscosity is
It was 680cps. When a small amount of this slurry mixture 1 is dropped onto a smooth mold kept at 165°C, it becomes a wax-like solid after 30 seconds, and after 120 seconds it has hardened to the extent that it will not cause scratches even if the surface is rubbed strongly with a metal spatula. However, even when this material was exposed to the flame of a burner, no phenomenon of softening and melting was observed. Example 2 Polymethylene polyphenyl isocyanate 1120
(8 grams equivalent) and 605 grams (14.2 grams equivalent) of melamine were placed in a porcelain pot mill and ground and dispersed together with 2200 grams of porcelain balls for 18 hours to obtain brown slurry mixture 2. The viscosity is
It was 1500cps. When a small amount of this slurry mixture 2 is dropped onto a smooth mold kept at 165°C, it becomes a wax-like solid after 20 seconds, and after 60 seconds it has hardened to the extent that it will not cause scratches even if the surface is rubbed strongly with a metal spatula. However, even when this material was exposed to the flame of a burner, no phenomenon of softening and melting was observed. Example 3 Polymethylene polyphenyl isocyanate 1120
g (8 gram equivalent) and 748 g of benzoguanamine
(equivalent to 8 grams) in a porcelain pot mill,
The mixture was pulverized and dispersed for 18 hours with 2000 g of porcelain balls to obtain a brown slurry mixture 3. Viscosity is 800cps
It was hot. When a small amount of this slurry mixture 3 is dropped onto a smooth mold kept at 165°C, it becomes a wax-like solid after 60 seconds, and after 180 seconds it has hardened to the extent that it will not cause scratches even if the surface is rubbed strongly with a metal spatula. However, even when this material was exposed to the flame of a burner, no phenomenon of softening and melting was observed. Example 4 Polymethylene polyphenyl isocyanate 1120
(8 gram equivalent), 170 g (4 gram equivalent) of melamine, and 374 g (4 gram equivalent) of benzoguanamine were placed in a porcelain pot mill.
A brown slurry mixture 4 was obtained by pulverizing and dispersing it together with 2000 g for 18 hours. The viscosity was 720 cps.
When a small amount of this slurry mixture 4 is dropped onto a smooth mold kept at 165°C, it becomes a wax-like solid after 50 seconds, and after 180 seconds it has hardened to the extent that it will not cause scratches even if the surface is rubbed strongly with a metal spatula. However, even when this material was exposed to the flame of a burner, no phenomenon of softening and melting was observed. The changes in viscosity when slurry mixtures 1 and 2 in Examples 1 and 2 were placed at temperatures of 20°C and 40°C are shown in FIG. Example 5 Slurry mixtures 1, 2, 3, and 4 in Examples 1, 2, 3, and 4 were poured into a mold that had been preheated in a dryer whose temperature was adjusted to 165°C, and at the same time the lid was closed. Then, heating was continued for 1 hour in a dryer to obtain a plate-shaped molded product. The physical properties of this product are shown in Table 1.
As shown.
【表】
実施例 6
実施例1,2,3及び4に於けるスラリー状混
合物1,2,3,4を金型中に流し込み、蓋をし
てから、まず165℃の乾燥機中で1時間熱し、次
いで乾燥機の温度を200℃に上げ、18時間加熱し
て板状成型品を得た。このものの物性は表2に示
す通りであつた。[Table] Example 6 Slurry mixtures 1, 2, 3, and 4 from Examples 1, 2, 3, and 4 were poured into a mold, covered, and then heated in a dryer at 165°C. After heating for an hour, the temperature of the dryer was raised to 200°C and heated for 18 hours to obtain a plate-shaped molded product. The physical properties of this product were as shown in Table 2.
【表】
実施例 7
実施例1,2,3及び4に於けるスラリー状混
合物1,2,3,4を金型中に流し込み、蓋をし
てから、まず165℃の乾燥機中で1時間加熱し、
次いで乾燥機の温度を200℃に上げて18時間加熱
し、更に乾燥機の温度を350℃に上げ2時間加熱
して板状成形品を得た。このものは黄色を呈し、
わずかに発泡していた。物性を表3に、又、1分
間に5℃ずつ昇温した場合の熱重量分析の結果を
第2図に示す。[Table] Example 7 Slurry mixtures 1, 2, 3, and 4 in Examples 1, 2, 3, and 4 were poured into a mold, covered, and then heated in a dryer at 165°C. Heat for an hour,
Next, the temperature of the dryer was raised to 200°C and heated for 18 hours, and the temperature of the dryer was further raised to 350°C and heated for 2 hours to obtain a plate-shaped molded product. This thing has a yellow color,
It was slightly foaming. The physical properties are shown in Table 3, and the results of thermogravimetric analysis when the temperature was increased by 5° C. per minute are shown in FIG.
【表】【table】
【表】
実施例 8
165℃に予熱した金型に、同寸法に裁断した連
続長繊維ガラスマツトを6枚積み重ねて充填し、
スラリー状混合物2を流し込み、直ちに上型をは
め込んでプレスにより加圧し、10分後金型を開い
て板状成型品を得た。このものの物性は表4に示
す通りであつた。[Table] Example 8 Six sheets of continuous long fiber glass mat cut to the same size were stacked and filled into a mold preheated to 165°C.
Slurry mixture 2 was poured into the mold, and an upper mold was immediately fitted and pressurized using a press. After 10 minutes, the mold was opened to obtain a plate-shaped molded product. The physical properties of this product were as shown in Table 4.
【表】
更に、上記成型品を200℃で18時間キユアーし
たところ、このものは表5のような物性を示し
た。[Table] Furthermore, when the above molded product was cured at 200°C for 18 hours, it exhibited the physical properties shown in Table 5.
【表】
実施例 9
スラリー状混合物1と様々な無機材料とを混合
し、金型に入れて165℃、圧力100Kg/cm2で10分間
プレスして、板状成型品を得た。このものの物性
は表6の通りであつた。[Table] Example 9 Slurry mixture 1 and various inorganic materials were mixed, placed in a mold, and pressed at 165° C. and a pressure of 100 Kg/cm 2 for 10 minutes to obtain a plate-shaped molded product. The physical properties of this product were as shown in Table 6.
【表】【table】
【表】
実施例 10
スラリー状混合物1 65グラムにシリコン系界
面活剤1.3c.c.及び発泡剤として炭酸水素ナトリウ
ム10グラムを容量300c.c.のステンレス製ビーカー
に入れ、マントルヒーター上で充分攪拌混合しつ
つ110℃まで加熱した。次いでこれを予め165℃に
加熱した内則寸法200mm×200mm×25mmの金型内に
流し込み、蓋をして165℃の乾燥機内で10分間加
熱した。金型を開いて200mm×200mm×25mmの寸法
を有する独立気泡性の硬質発泡体を得た。更にこ
の発泡体を200℃の乾燥機で2時間キユアーし、
褐色の発泡体を得た。これらの発泡体の物質は表
7に示す通りであつた。[Table] Example 10 65 grams of slurry mixture 1, 1.3 cc of silicone surfactant, and 10 grams of sodium hydrogen carbonate as a blowing agent were placed in a stainless steel beaker with a capacity of 300 cc, and the mixture was thoroughly stirred and mixed on a mantle heater. The mixture was heated to 110°C. Next, this was poured into a mold with internal dimensions of 200 mm x 200 mm x 25 mm that had been preheated to 165°C, the lid was closed, and the mold was heated for 10 minutes in a dryer at 165°C. The mold was opened to obtain a closed-cell rigid foam having dimensions of 200 mm x 200 mm x 25 mm. Furthermore, this foam was cured in a dryer at 200℃ for 2 hours.
A brown foam was obtained. The materials of these foams were as shown in Table 7.
第1図はスラリー状混合物1,2の温度と粘度
上昇との関係を示すグラフ、第2図は本発明によ
り得られた樹脂の一例の熱質量分析の結果を示す
グラフである。
FIG. 1 is a graph showing the relationship between the temperature and viscosity increase of slurry mixtures 1 and 2, and FIG. 2 is a graph showing the results of thermal mass spectrometry of an example of the resin obtained by the present invention.
Claims (1)
メラミン及び/又はグアナミンを加熱下に反応さ
せることを特徴とする耐熱性熱硬化性樹脂の製造
方法。 2 ポリメチレンポリフエニルイソシアネートと
メラミン及び/又はグアナミンを60℃以上200℃
以下の温度に加熱し反応させることを特徴とする
特許請求の範囲第1項記載の耐熱性硬化性樹脂の
製造方法。 3 ポリメチレンポリフエニルイソシアネートと
メラミン及び/又はグアナミンを60℃乃至200℃
に加熱し、次いで200℃乃至250℃に加熱し反応さ
せることを特徴とする特許請求の範囲第1項記載
の耐熱性熱硬化性樹脂の製造方法。 4 ポリメチレンポリフエニルイソシアネートと
メラミン及び/又はグアナミンを60℃乃至200℃
に加熱し、次いで200℃乃至250℃に加熱し、更に
300℃以上に加熱し反応させることを特徴とする
特許請求の範囲第1項記載の耐熱性熱硬化性樹脂
の製造方法。 5 ポリメチレンポリフエニルイソシアネートと
メラミン及び/又はグアナミンを加熱下に、適宜
発泡剤の存在下で反応させることを特徴とする特
許請求の範囲第1項記載の耐熱性熱硬化性樹脂の
製造方法。[Claims] 1. A method for producing a heat-resistant thermosetting resin, which comprises reacting polymethylene polyphenyl isocyanate with melamine and/or guanamine under heating. 2 Polymethylene polyphenyl isocyanate and melamine and/or guanamine at 60℃ or higher and 200℃
The method for producing a heat-resistant curable resin according to claim 1, characterized in that the reaction is carried out by heating to the following temperature. 3 Polymethylene polyphenyl isocyanate and melamine and/or guanamine at 60°C to 200°C
2. The method for producing a heat-resistant thermosetting resin according to claim 1, wherein the resin is heated to 200° C. to 250° C. for reaction. 4 Polymethylene polyphenyl isocyanate and melamine and/or guanamine at 60°C to 200°C
, then heated to 200℃ to 250℃, and then
The method for producing a heat-resistant thermosetting resin according to claim 1, characterized in that the reaction is carried out by heating to 300° C. or higher. 5. The method for producing a heat-resistant thermosetting resin according to claim 1, which comprises reacting polymethylene polyphenyl isocyanate with melamine and/or guanamine under heating in the presence of an appropriate blowing agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57151894A JPS5941320A (en) | 1982-09-01 | 1982-09-01 | Heat-resistant thermosetting resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57151894A JPS5941320A (en) | 1982-09-01 | 1982-09-01 | Heat-resistant thermosetting resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5941320A JPS5941320A (en) | 1984-03-07 |
| JPS6149328B2 true JPS6149328B2 (en) | 1986-10-29 |
Family
ID=15528516
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57151894A Granted JPS5941320A (en) | 1982-09-01 | 1982-09-01 | Heat-resistant thermosetting resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5941320A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2632939B2 (en) * | 1987-11-30 | 1997-07-23 | 株式会社イーテック | One-part type thermosetting composition |
| DE3932168A1 (en) * | 1989-09-27 | 1991-04-04 | Bayer Ag | LACK POLYISOCYANATES, A METHOD OF THEIR PREPARATION AND THEIR USE |
| JPH0948836A (en) * | 1995-10-30 | 1997-02-18 | Nisshinbo Ind Inc | Production of thermosetting resin |
| KR101215459B1 (en) | 2008-03-27 | 2012-12-26 | 도쿄 프린팅 잉크 엠에프지. 캄파니 리미티드 | Ink-jet ink composition for etching resist |
| JP6010316B2 (en) * | 2012-03-30 | 2016-10-19 | 株式会社ニデック | Coating material |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4997097A (en) * | 1972-12-25 | 1974-09-13 | ||
| IT1066072B (en) * | 1975-06-09 | 1985-03-04 | Thiokol Corp | POLYURETHANE HARDENING AGENTS |
-
1982
- 1982-09-01 JP JP57151894A patent/JPS5941320A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5941320A (en) | 1984-03-07 |
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