JPS63137936A - Production of foamed material - Google Patents

Production of foamed material

Info

Publication number
JPS63137936A
JPS63137936A JP61282166A JP28216686A JPS63137936A JP S63137936 A JPS63137936 A JP S63137936A JP 61282166 A JP61282166 A JP 61282166A JP 28216686 A JP28216686 A JP 28216686A JP S63137936 A JPS63137936 A JP S63137936A
Authority
JP
Japan
Prior art keywords
liquid
slurry
resin
foam
powder
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.)
Pending
Application number
JP61282166A
Other languages
Japanese (ja)
Inventor
Kiyohiko Watanabe
烈彦 渡辺
Kazuhiko Kohama
小浜 一彦
Takuji Mogi
卓治 茂木
Yoshinao Kato
義尚 加藤
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.)
Nippon Steel Chemical and Materials Co Ltd
Original Assignee
Nippon Steel Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Steel Chemical Co Ltd filed Critical Nippon Steel Chemical Co Ltd
Priority to JP61282166A priority Critical patent/JPS63137936A/en
Publication of JPS63137936A publication Critical patent/JPS63137936A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To stably add a solid additive over a long period and to prevent the troubles in apparatus, by mixing a liquid additive such as foaming agent and a solid additive such as inorganic powder in the form of a slurry having high concentration, compounding the slurry to a liquid thermosetting resin and extruding, foaming and curing the resin composition. CONSTITUTION:A liquid thermosetting resin is added with a liquid additive such as foaming agent, curing agent, etc., and a solid additive such as inorganic filler. In the above process, the solid additive is mixed with a small amount of the liquid resin, liquid additive or other liquid to form a slurry having high concentration, the slurry is added to the liquid resin and the whole mixture is extruded, foamed and cured. The resin is a thermosetting resin curable with an acid and the inorganic powder is powder of metal and/or metal compound capable of neutralizing an acid, preferably zinc, aluminum hydroxide, etc. The liquid used in the production of slurry is ethylene glycol, polyvinyl alcohol, etc., and the concentration of the slurry is 40-95wt%.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は熱硬化性樹脂発泡体の製造方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for producing a thermosetting resin foam.

〔従来の技術〕[Conventional technology]

フェノール樹脂、エポキシ樹脂、ユリャ樹脂等の熱硬化
性樹脂の発泡体は断熱パネル等に利用されている(特公
昭50−9826号公報、特開昭60−11520号公
報)。
Foams of thermosetting resins such as phenol resins, epoxy resins, and urea resins are used for heat insulating panels and the like (Japanese Patent Publication No. 50-9826, JP-A No. 60-11520).

これらの発泡体は、熱硬化性樹脂液に発泡剤、整泡剤、
硬化剤や必要に応じて添加される調整剤、例えば、イソ
シアネート化合物等を添加混合し、これを発泡成形する
ことにより得られる。この際、硬化剤として酸を使用し
た場合、発泡硬化後発泡体内に酸が残存し面材となる鋼
板や、後加工での鉄くぎ等を腐食させる。これらの腐食
を防止する目的で、金属粉末や炭酸カルシウム等の無機
粉末を添加する方法が知られている。
These foams are made by adding blowing agents, foam stabilizers, and thermosetting resin liquids.
It is obtained by adding and mixing a curing agent and a regulator added as necessary, such as an isocyanate compound, and then foam-molding the mixture. At this time, when an acid is used as a hardening agent, the acid remains in the foam after the foam is hardened and corrodes the steel plate serving as the face material, iron nails, etc. in post-processing. For the purpose of preventing these corrosions, a method of adding metal powder or inorganic powder such as calcium carbonate is known.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

金属粉末等の無機粉末を連続的に添加する場合、前もっ
て樹脂液に添加分散させておく方法が一般的であるが、
この方法であると樹脂液と金属粉末等の無機粉末の比重
差により、長時間放置すると分離沈降したり、また装入
に使用する定量ポンプの損傷がはげしくなり修繕費が増
大するという問題がある。
When adding inorganic powder such as metal powder continuously, it is common to add and disperse it in the resin liquid in advance.
With this method, due to the difference in specific gravity between the resin liquid and inorganic powder such as metal powder, if left for a long time, they will separate and settle, and the metering pump used for charging will be severely damaged, increasing repair costs. .

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、液状熱硬化性樹脂に整泡剤、発泡剤、硬化剤
等の液状添加剤を加え、更に金属粉末等の無機粉末を添
加して発泡体を連続的に形成させる方法において、金属
粉末等の無機粉末の高濃度スラリーを混合部に添加混合
した後、発泡成形する熱硬化性樹脂発泡体の製造方法で
ある。
The present invention provides a method in which a foam is continuously formed by adding liquid additives such as a foam stabilizer, a foaming agent, and a hardening agent to a liquid thermosetting resin, and further adding an inorganic powder such as a metal powder. This is a method for producing a thermosetting resin foam in which a high concentration slurry of inorganic powder such as powder is added to a mixing section, mixed, and then foam-molded.

熱硬化性樹脂としては、フェノール樹脂、エポキシ樹脂
、ユリア樹脂、ウレタン樹脂等があるが好ましくはフェ
ノール樹脂である。熱硬化性樹脂は粘度500〜20.
  OO0cps程度のものがよく、好ましくは1,0
00〜15. OO0cpsのものが用いられる。発泡
操作上、粘度は低い方が好ましいが、一般に粘度の低い
ものは水分量が多く鋼板との接着性に悪影響を及ぼす。
Examples of the thermosetting resin include phenol resin, epoxy resin, urea resin, and urethane resin, but phenol resin is preferable. The thermosetting resin has a viscosity of 500 to 20.
About OO0cps is good, preferably 1.0
00-15. OO0cps is used. For foaming operations, lower viscosity is preferable, but in general, lower viscosity materials have a higher water content, which adversely affects adhesion to steel plates.

水分量としては20重量%以下が好ましい。The moisture content is preferably 20% by weight or less.

例えば、このよ・うなフェノール樹脂は、フェノール類
とホルマリンとを1:1〜1:3の割合でアルカリ触媒
の存在下に反応させ、酸で中和した後、減圧脱水により
粘度を適度に調整することにより得られる。
For example, such phenolic resins are produced by reacting phenols and formalin at a ratio of 1:1 to 1:3 in the presence of an alkali catalyst, neutralizing with acid, and then adjusting the viscosity appropriately by dehydration under reduced pressure. It can be obtained by

本発明に用いる液状添加剤は整泡剤、発泡剤、硬化剤等
の一種又は二種以上である。整泡剤としては、シリコン
系界面活性剤、ノニオン界面活性剤等がある。整泡剤の
好ましい使用量は樹脂100重量部に対して0.5〜1
0重量部である。
The liquid additive used in the present invention is one or more of a foam stabilizer, a foaming agent, a curing agent, and the like. Examples of foam stabilizers include silicone surfactants and nonionic surfactants. The preferred amount of foam stabilizer used is 0.5 to 1 per 100 parts by weight of resin.
It is 0 parts by weight.

発泡剤としては、低沸点の脂肪族炭化水素又はそのハロ
ゲン化物が挙げられ、例えば、石油エーテル、n−ヘキ
サン、メチレンクロライド、トリクロロフルオロメタン
等のフレオン類等が挙げられる。 硬化剤としては、そ
れぞれの樹脂に使用される硬化剤が用いられる。フェノ
ール樹脂の場合はヘンゼンスルホン酸、パラトルエンス
ルホン酸、フェノールスルホン酸等の有機酸類、塩酸等
の無機酸類があげられこれらを単独あるいは併用しても
よい。この場合における硬化剤の好ましい使用量はフェ
ノール樹脂100重量部に対し、酸として5〜50重量
部である。
Examples of the blowing agent include low-boiling aliphatic hydrocarbons or halides thereof, such as petroleum ether, n-hexane, methylene chloride, freons such as trichlorofluoromethane, and the like. As the curing agent, the curing agent used for each resin is used. In the case of phenol resins, organic acids such as henzenesulfonic acid, p-toluenesulfonic acid, and phenolsulfonic acid, and inorganic acids such as hydrochloric acid are used, and these may be used alone or in combination. In this case, the preferred amount of the curing agent used is 5 to 50 parts by weight of the acid based on 100 parts by weight of the phenol resin.

本発明では、その他の添加剤として、発泡体の機械的物
性をより改善するために、例えば、エチレングリコール
、グリセリン等の多価アルコール類あるいは、例えば、
ジェタノールアミン、トリエタノールアミン、尿素、イ
ソシアネート化合物等の窒素含有化合物類を混合するこ
ともできる。
In the present invention, as other additives, in order to further improve the mechanical properties of the foam, for example, polyhydric alcohols such as ethylene glycol and glycerin, or, for example,
Nitrogen-containing compounds such as jetanolamine, triethanolamine, urea, and isocyanate compounds can also be mixed.

本発明に用いる固体状添加剤としては、金属粉末、金属
化合物、けい酸化合物等の無機粉末がある。金属粉末と
しては、亜鉛粉末、アルミニウム粉末等が挙げられ、無
機粉末としては、炭酸カルシウム、炭酸マグネシウム等
の炭酸塩、水酸化アルミニウム、水酸化バリウム、水酸
化リチウム、水酸化カルシウム等の水酸化物、アルミナ
、酸化亜鉛等の酸化物、その他ガラス粉末、クレー、石
膏、タルク等が挙げられ、これらを単独あるいは併用し
てもよく、また、粉末表面をマイクロカプセル化したも
のも使用できる。酸を中和する目的で添加する場合は、
酸を中和する性質を有する金属および/または金属の化
合物が好ましく、例えば亜鉛、アルミニウム、炭酸カル
シウム、炭酸マグネシウム、水酸化アルミニウム等が挙
げられる。
Solid additives used in the present invention include inorganic powders such as metal powders, metal compounds, and silicic acid compounds. Examples of metal powders include zinc powder and aluminum powder, and examples of inorganic powders include carbonates such as calcium carbonate and magnesium carbonate, and hydroxides such as aluminum hydroxide, barium hydroxide, lithium hydroxide, and calcium hydroxide. , alumina, oxides such as zinc oxide, other glass powders, clay, gypsum, talc, etc. These may be used alone or in combination, and powders whose surfaces are microencapsulated can also be used. When adding for the purpose of neutralizing acid,
Metals and/or metal compounds having the property of neutralizing acids are preferred, such as zinc, aluminum, calcium carbonate, magnesium carbonate, aluminum hydroxide, and the like.

この場合における好ましい使用量としては、改良する性
質により異なるが、例えば酸を中和する目的であればフ
ェノール樹脂の場合、樹脂100重量部に対し、亜鉛粉
末を2〜20重量部加えるとよい。
The preferred amount used in this case varies depending on the property to be improved, but for example, in the case of a phenol resin for the purpose of neutralizing acids, it is preferable to add 2 to 20 parts by weight of zinc powder per 100 parts by weight of the resin.

本発明に用いる金属粉末等の無機粉末をスラリー化する
ための液体としては、原料となる液状の樹脂、液状添加
剤であってもよいが、比較的粘度の高いものが好ましい
。好ましい液体としては、エチレングリコール、ジエチ
レングリコール、グリセリン等の多価アルコール類、ポ
リエチレングリコール、ポリビニルアルコール、ポリブ
チルアルコール等のポリアルコール類、ノニオン系界面
活性剤、ジオクチルフタレート等の可塑剤、有機リン酸
エステル等の液体@燃剤等が挙げられ、これらを単独あ
るいは併用しても良く、更に硬化を促進するためにレゾ
ルシン、m−クレゾール、カテコールといった硬化促進
剤の添加も可能である。
The liquid for slurrying the inorganic powder such as the metal powder used in the present invention may be a liquid resin as a raw material or a liquid additive, but a liquid with relatively high viscosity is preferable. Preferred liquids include polyhydric alcohols such as ethylene glycol, diethylene glycol, and glycerin, polyalcohols such as polyethylene glycol, polyvinyl alcohol, and polybutyl alcohol, nonionic surfactants, plasticizers such as dioctyl phthalate, and organic phosphate esters. These liquids may be used alone or in combination, and it is also possible to add curing accelerators such as resorcinol, m-cresol, and catechol to accelerate curing.

スラリー中の金属粉末あるいは無機粉末の濃度としては
40〜95wt%好ましくは50〜80wt%がよ<、
濃度が低すぎるとスラリーの分離が起こったり、多量の
母液による発泡体物性への悪影響が起こる。また、濃度
が高過ぎるとスラリへ粘度が高くなり、混合吐出部への
供給が困難になったり、発泡体中への金属粉末等の無機
粉末の分散が均一にならないといった問題が起こる。
The concentration of metal powder or inorganic powder in the slurry is 40 to 95 wt%, preferably 50 to 80 wt%.
If the concentration is too low, separation of the slurry may occur, or a large amount of mother liquor may adversely affect the physical properties of the foam. Furthermore, if the concentration is too high, the viscosity of the slurry will increase, causing problems such as difficulty in supplying the slurry to the mixing and discharging section, and uneven dispersion of inorganic powder such as metal powder into the foam.

本発明による発泡体の製造は次のようにして行われる。The foam according to the invention is produced as follows.

すなわち、樹脂、発泡剤、整泡剤、硬化剤等の液状添加
剤と金属粉末等の無機粉末スラリーを定量ポンプを利用
して別々に混合吐出部へ送液し、混合吐出を行う。この
混合を行う前に、樹脂と整泡剤、発泡剤その他の添加剤
等の液状添加剤を事前に混合すること等2.混合すべき
成分の一部を事前に混合し、そこへ残余の成分を混合す
ることは任意であるが、樹脂と硬化剤は直前に混合する
のが望ましい。また、金属粉末等の無機粉末スラリーを
混合した後、移送ポンプを通過させることは本発明の趣
旨に反する。したがって、混合を2段階以上で行う場合
、スラリーは最終の混合部に添加する。
That is, a liquid additive such as a resin, a foaming agent, a foam stabilizer, a hardening agent, etc. and an inorganic powder slurry such as a metal powder are separately sent to a mixing and discharging section using a metering pump, and mixed and discharging is performed. 2. Before performing this mixing, the resin and liquid additives such as a foam stabilizer, foaming agent, and other additives are mixed in advance. Although it is optional to premix some of the components to be mixed and then mix the remaining components therein, it is preferable to mix the resin and curing agent immediately beforehand. Furthermore, it is contrary to the spirit of the present invention to pass an inorganic powder slurry such as metal powder through a transfer pump after mixing it. Therefore, when mixing is performed in two or more stages, the slurry is added to the final mixing section.

樹脂や発泡剤、硬化剤等を連続定量的に送液するポンプ
としては、ギヤポンプ、ダイヤフラムポンプ、プランジ
ャーポンプ等があげられるが、脈動のないギヤポンプ、
多連ダイヤフラムポンプが望ましい。金属粉体や無機粉
末スラリー用ポンプとしては、高粘度のスラリーを定量
できるポンプであれば良いが、ギヤポンプ、スネークポ
ンプ等が好ましい。
Gear pumps, diaphragm pumps, plunger pumps, etc. are examples of pumps that continuously and quantitatively pump resin, foaming agents, curing agents, etc., but gear pumps without pulsation,
A multiple diaphragm pump is preferred. The pump for metal powder or inorganic powder slurry may be any pump that can quantify high viscosity slurry, but gear pumps, snake pumps, etc. are preferable.

混合機としては、高速攪拌タイプのミキシングヘッドや
静止型混合機が挙げられるが、全波の混合が十分に行え
るものであればいずれでもよい。
Examples of the mixer include a high-speed stirring type mixing head and a static mixer, but any device that can perform full-wave mixing may be used.

混合が終了した後は、これを吐出し、型枠に注入する等
の手段で発泡成形する。フェノール樹脂発泡体を製造す
る場合の一例としては、鋼板を走行させておいて、そこ
に、混合、吐出されるフェノール樹脂液を連続的に流し
込み、これを50〜100°Cの加温室へ通すことによ
り連続的に鋼板付発泡体パネルを得る方法を挙げること
ができる。
After the mixing is completed, the mixture is discharged and foam-molded by means such as pouring into a mold. An example of manufacturing a phenolic resin foam is to run a steel plate, continuously pour the mixed and discharged phenolic resin liquid into it, and pass it through a heating chamber at 50 to 100°C. A method of continuously obtaining a foam panel with a steel plate can be mentioned.

この場合、使用される鋼板は、亜鉛鉄板でもよいし、そ
の表面に塗装を施したものでもよい。その塗料としては
、例えば、アクリル樹脂系塗料、ポリエステル樹脂系塗
料等が好ましく用いられる。
In this case, the steel plate used may be a galvanized iron plate or one whose surface is coated. As the paint, for example, acrylic resin paint, polyester resin paint, etc. are preferably used.

〔実施例〕〔Example〕

以下、実施例及び比較例に基づいて、本発明方法を具体
的に説明する。
The method of the present invention will be specifically explained below based on Examples and Comparative Examples.

実施例ル ゾール100重量部(粘度1.000cps)に整泡剤
2重量部(L、−5340:日本ユニカー社製)を加え
た液と、発泡剤20重量部(フレオン113)と、硬化
剤30重量部(66,7製L%−p−トルエンスルフォ
ン酸水溶液)と亜鉛粉(150メソシユ)にレゾールを
加えて混練したスラリー(亜鉛濃度ニア0wt%)5.
7重量部をそれぞれ定量ポンプを使用して、20nφで
25エレメントの静止型混合機を通過させ十分に混合さ
せた後、連続的にロールで成形した金属型枠に流し込み
ベルトコンベアを持つ90℃の連続硬化炉中で発泡硬化
させ、金属サイディングパネルを得た。この作業を2時
間連続運転し、−夜停止後翌日再び同様の作業を2時間
連続で行った。第1日目、2日目共に運転はスムーズに
行え、運転開始から翌日停止まで得られた発泡体の浸漬
水pHを測定した結果4.0から4.3の範囲であり、
亜鉛粉の分散性が良いことが判った。
Example A liquid prepared by adding 2 parts by weight of a foam stabilizer (L, -5340: manufactured by Nippon Unicar Co., Ltd.) to 100 parts by weight of Lusol (viscosity 1.000 cps), 20 parts by weight of a foaming agent (Freon 113), and 30 parts by weight of a hardening agent. Slurry (zinc concentration near 0 wt%) made by adding resol to part by weight (L%-p-toluenesulfonic acid aqueous solution manufactured by 66,7) and zinc powder (150 mesoyu) and kneading.5.
Using a metering pump, 7 parts by weight were thoroughly mixed by passing through a static mixer with 20 nφ and 25 elements, and then continuously poured into a metal form formed by rolls and heated to 90°C using a belt conveyor. A metal siding panel was obtained by foaming and curing in a continuous curing furnace. This operation was performed continuously for 2 hours, and after stopping at night, the same operation was performed again the next day for 2 hours continuously. The operation was smooth on both the first and second days, and the pH of the water immersed in the foam obtained from the start of operation until it was stopped the next day was measured and was in the range of 4.0 to 4.3.
It was found that the dispersibility of zinc powder was good.

実施例2 実施例1と同様な作業を1ケ月間継続して、運転状況を
観察したが、運転はスムーズでポンプからの液漏れ等の
異常もなかった。
Example 2 The same operation as in Example 1 was continued for one month and the operating conditions were observed. The operation was smooth and there were no abnormalities such as liquid leakage from the pump.

比較例ル ゾール100重量部(粘度10.  OO0cps)に
整泡剤2重量部(L−5340:日本ユニカー社製)と
亜鉛粉4重量部(1560メソシユ)を加えてよく攪拌
した液と、発泡剤20重量部(フレオン113)と硬化
剤30重量部(66,7wt% P−)ルエンスルホン
酸水溶液)をそれぞれ定量ポンプを使用して、実施例1
と同じ静止型混合機を通過させた他は実施例1と同様な
作業を行い、金属サイディングパネルを得た。
Comparative Example A liquid obtained by adding 2 parts by weight of a foam stabilizer (L-5340: manufactured by Nippon Unicar Co., Ltd.) and 4 parts by weight of zinc powder (1560 mesoyu) to 100 parts by weight of Luzol (viscosity 10.00 cps) and stirring well, and a foaming agent. Example 1: 20 parts by weight (Freon 113) and 30 parts by weight (66.7 wt% P-) luenesulfonic acid aqueous solution) were added using a metering pump.
A metal siding panel was obtained by carrying out the same operation as in Example 1, except that the sample was passed through the same static mixer.

第1白目の運転はスムースに行えたが、第2日月はレゾ
ール中の亜鉛粉が沈降し、運転開始時にポンプのシェヤ
ーピンが折れた。修理して運転を再開し2時間連続運転
した。第1白目に得られた発泡体の浸漬水pHは4.1
〜4.3の範囲であったが、2日目に得られた発泡体の
浸漬水pHは4.8〜3,0と後半になる程低くなり亜
鉛粉の濃度が減少していることが判った。
The operation of the first pewter was smooth, but on the second day and month, the zinc powder in the resol settled and the shear pin of the pump broke at the start of operation. After repairs were made, the vehicle resumed operation and continued for two hours. The pH of the immersion water for the foam obtained in the first pewter was 4.1.
4.3, but the pH of the immersion water for the foam obtained on the second day was 4.8 to 3.0, which became lower in the latter half, indicating that the concentration of zinc powder was decreasing. understood.

比較例2 比較例1の液を用いて、運転する前に必ずレゾールと整
泡剤と亜鉛粉の混合液を調製して使用した他は、比較例
2と同様な作業を1ケ月間連続して運転状況を観察した
。運転はスムースに行えたが、10日経過後レゾールと
整泡剤と亜鉛粉の混合液用ポンプより異常音が確認され
、20日経過後より同ポンプの軸受は部より液漏れが発
見された。
Comparative Example 2 The same operations as in Comparative Example 2 were carried out continuously for one month, except that the liquid in Comparative Example 1 was used and a mixed solution of resol, foam stabilizer, and zinc powder was prepared and used before operation. The driving conditions were observed. The operation was smooth, but after 10 days, an abnormal noise was confirmed from the pump for the mixture of resol, foam stabilizer, and zinc powder, and after 20 days, it was discovered that the pump was leaking from the bearing.

〔発明の効果〕〔Effect of the invention〕

本発明の製造方法によれば、無機粉末等の固体状添加剤
を長時間安定して添加することができるので、添加量の
変動、装置の故障等を著しく減少させることができる。
According to the manufacturing method of the present invention, solid additives such as inorganic powders can be added stably for a long period of time, so fluctuations in the amount added, equipment failures, etc. can be significantly reduced.

Claims (3)

【特許請求の範囲】[Claims] (1)液状の熱硬化性樹脂に発泡剤、硬化剤等の液状添
加剤および無機粉末等の固体状添加剤を加えて発泡体を
形成させる方法において、固体状添加剤は少量の液状の
樹脂若しくは液状添加剤又はその他液体と混合して高濃
度のスラリーとし、このスラリーを樹脂と液状添加剤の
混合部に混合、吐出し、発泡硬化させることを特徴とす
る発泡体の製造方法。
(1) In a method of forming a foam by adding liquid additives such as blowing agents and hardening agents, and solid additives such as inorganic powder to liquid thermosetting resin, the solid additives are added to a small amount of liquid resin. Alternatively, a method for producing a foam, which comprises mixing with a liquid additive or other liquid to form a highly concentrated slurry, mixing the slurry into a resin and liquid additive mixing area, discharging the slurry, and foaming and hardening the slurry.
(2)樹脂が酸硬化型の熱硬化性樹脂である特許請求の
範囲第1項記載の発泡体の製造方法。
(2) The method for producing a foam according to claim 1, wherein the resin is an acid-curable thermosetting resin.
(3)無機粉体が酸を中和する性質を有する金属および
/又は金属化合物の粉末である特許請求の範囲第1項又
は第2項記載の発泡体の製造方法。
(3) The method for producing a foam according to claim 1 or 2, wherein the inorganic powder is a powder of a metal and/or a metal compound having the property of neutralizing acids.
JP61282166A 1986-11-28 1986-11-28 Production of foamed material Pending JPS63137936A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61282166A JPS63137936A (en) 1986-11-28 1986-11-28 Production of foamed material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61282166A JPS63137936A (en) 1986-11-28 1986-11-28 Production of foamed material

Publications (1)

Publication Number Publication Date
JPS63137936A true JPS63137936A (en) 1988-06-09

Family

ID=17648959

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61282166A Pending JPS63137936A (en) 1986-11-28 1986-11-28 Production of foamed material

Country Status (1)

Country Link
JP (1) JPS63137936A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01178536A (en) * 1987-12-30 1989-07-14 Toyo Tire & Rubber Co Ltd Production of rust-inhibiting phenol resin foam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01178536A (en) * 1987-12-30 1989-07-14 Toyo Tire & Rubber Co Ltd Production of rust-inhibiting phenol resin foam

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