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JPS6028297B2 - Method for producing phenolic resin foam - Google Patents
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JPS6028297B2 - Method for producing phenolic resin foam - Google Patents

Method for producing phenolic resin foam

Info

Publication number
JPS6028297B2
JPS6028297B2 JP10092679A JP10092679A JPS6028297B2 JP S6028297 B2 JPS6028297 B2 JP S6028297B2 JP 10092679 A JP10092679 A JP 10092679A JP 10092679 A JP10092679 A JP 10092679A JP S6028297 B2 JPS6028297 B2 JP S6028297B2
Authority
JP
Japan
Prior art keywords
parts
resin
foam
phenolic resin
foaming
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
Application number
JP10092679A
Other languages
Japanese (ja)
Other versions
JPS5625434A (en
Inventor
直喜 吉見
明 久保田
士朗 有田
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.)
Fudow Co Ltd
Original Assignee
Fudow 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 Fudow Co Ltd filed Critical Fudow Co Ltd
Priority to JP10092679A priority Critical patent/JPS6028297B2/en
Publication of JPS5625434A publication Critical patent/JPS5625434A/en
Publication of JPS6028297B2 publication Critical patent/JPS6028297B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は均一、微細な発泡粒子を有するフェノール樹脂
発泡体の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a phenolic resin foam having uniform, fine expanded particles.

フェノール樹脂発泡体の製造法としてフェノ−ルとホル
ムアルデヒドを酸性触媒存在下反応させて得られたノボ
ラック樹脂に発泡剤、硬化剤、界面活性剤等を単に粉砕
しながら混合する方法(特公昭47−19624)ある
いはノボラツク樹脂と発泡剤、硬化剤、界面活性剤等を
混合したのち押出機で混練、押出す方法(特公昭48一
133総)等が知られている。
As a method for producing phenolic resin foam, a blowing agent, a curing agent, a surfactant, etc. are mixed with a novolac resin obtained by reacting phenol and formaldehyde in the presence of an acidic catalyst while simply pulverizing it (Japanese Patent Publication No. 1973- 19624) or a method in which a novolac resin is mixed with a blowing agent, a curing agent, a surfactant, etc., and then kneaded and extruded using an extruder (Japanese Patent Publication No. 48-133).

しかしこれらの方法により得られたフェノール樹脂発泡
体は粗く不均質な発泡粒子を有し、均一微細な発泡粒子
を有するフェノール樹脂を得ることは困難であった。又
発泡体のもろさなどの性能改善の為フェノールにポリビ
ニルアルコールを添加してアルデヒドと反応させて得た
ビニルアセタール変性フェノール樹脂と発泡剤、硬化剤
を加熱、混練する方法(特公昭38−12189)等も
知られているが、この樹脂は低融点で粉砕が困難であり
、且つ組成物の固化等により作業性が悪い等の欠点があ
る。
However, the phenolic resin foams obtained by these methods have coarse and non-uniform foamed particles, and it has been difficult to obtain a phenolic resin having uniform and fine foamed particles. In addition, in order to improve performance such as brittleness of foam, there is a method of heating and kneading a vinyl acetal-modified phenol resin obtained by adding polyvinyl alcohol to phenol and reacting it with aldehyde, a blowing agent, and a curing agent (Japanese Patent Publication No. 38-12189). However, this resin has a low melting point and is difficult to crush, and has disadvantages such as poor workability due to solidification of the composition.

本発明は以上の如き欠点を解消し、均一微細な発泡粒子
を有すると共に良好な成形加工性を有するフェノール樹
脂発泡体を製造する方法に関するもので、これは、フェ
ノール類とアルデヒド類を酸性触媒存在下反応させ、反
応生成物を中和後樹脂相から水性相を分離除去し、樹脂
相に界面活性剤、ポリビニルアルコール及びアルカリ士
金属もしくは亜鉛の酸化物もしくは水酸化物を添加し加
熱、脱水し、次いで発泡剤、硬化剤を添加、混練したの
ち加熱し発泡、硬化させることにより達成される。本発
明において使用されるフェノール類はフェノール、クレ
ゾール、キシレノール、レゾルシノール等であり、アル
デヒド類としてはホルムアルデヒド、パラホルムアルデ
ヒド、フルフラール等が挙げられる。酸性触媒としては
塩酸、硫酸等の無機酸又はシュウ酸、ベンゼンスルフオ
ン酸等の有機酸が使用される。反応は一般のノボラック
樹脂の製造法と同様フェノール額に対するアルデヒド類
のモル比を1以下とし、温度90〜10000程度で還
流下反応させる。反応完了後カセィソーダ、カセィカリ
、水酸化カルシウム等のアルカリ性物質を加えpH6〜
7に中和し放冷する。冷却により反応生成液は水性相と
樹脂相に分離するので上層の水性相を分離、除去し、樹
脂液に界面活性剤、ポリビニルアルコール及びアルカリ
士金属もしくは亜鉛の酸化物もしくは水酸化物を加える
。界面活性剤は起泡調節剤としての役目を果すもので、
シリコン系(たとえばUCC社製、L−52止 L−5
30、L−5320など)、非イオン活性剤(たとえば
ポリオキシエチレンソルビタンモノラウレート(花王ア
トラス社製、トウィーン20)、ポリオキシエチレンソ
ルビタンモノパルミテート(同、トウイーン40)、ポ
リオキシエチレンノニルフェノールェーテル、東邦化学
製ソルボンF80など)などが用いられる。これらの添
加量はフェノール類 10碇部(以下重量部)に対し0
.5〜3部であり、これを樹脂相に完全に溶解させる。
ポリピニルアルコールはフェノール類 100部に対し
0.05〜1部を水溶液として加え樹脂相に完全に分散
溶解させる。又アルカリ士金属(カルシウム、バリウム
、マグネシウム等)もしくは亜鉛の酸化物もしくは水酸
化物は硬化助剤としての作用を示すもので、これは低発
泡品を目的とする場合にはフェノール類 10碇部‘こ
対し2〜10部、高発泡品を目的とする場合には0.3
〜2部を加える。これらを樹脂相に完全に溶解させ加熱
、脱水すると透明なノボラック樹脂が得られる。加熱、
脱水後の樹脂相に発泡剤、硬化剤、更に必要に応じ鱗型
剤、顔料等を加える。発泡剤としてはジニトロソベンタ
メチレンテトラミン、アゾジカルボンアミド、ベンゼン
スルホニルヒドラジド誘導体、トルェンスルホニルヒド
ラジド誘導体、アゾィソブチロジニトリル、炭酸水素ナ
トリウム等加熱によりガスを発生する物質が挙げられる
。これはノボラック樹脂 10$轍こ対し1〜12部が
添加される。又硬化剤としてはへキサメチレンテトラミ
ン、パラホルムアルデヒドが用いられ、ノボラック樹脂
100部に対し8〜16部が添加される。その他ステ
アリン酸、ステアリン酸カルシウム、ステアリン酸マグ
ネシウム等の滋型剤1〜3部、着色剤(染料、顔料)等
を適宜加え、ポールミル、リボンブレンダー等の混合機
を用い十分混合し、更に加熱ロール、コニーダー等で十
分混練、粉砕して発泡可能な組成物を得る。この組成物
を低温でタブレット又は板状に成型したものを成型箱又
は金型に入れて加熱炉中で加熱し発泡、硬化させること
により均→微細な粒子を有する発泡体を得ることが出来
る。本発明によるノボラック樹脂はその合成工程中にお
いて界面活性剤及びポリビニルアルコールを溶解してい
るので、発泡硬化に際し発生したガスの気泡調節と気泡
の安定作用効果により微細な発泡粒子を有し、かつ均質
な発泡体を与える。
The present invention solves the above-mentioned drawbacks and relates to a method for producing a phenolic resin foam having uniform and fine expanded particles and good moldability. After neutralizing the reaction product, the aqueous phase is separated and removed from the resin phase, and a surfactant, polyvinyl alcohol, and an alkali metal or zinc oxide or hydroxide are added to the resin phase, followed by heating and dehydration. Next, a foaming agent and a curing agent are added, kneaded, and then heated to foam and harden. The phenols used in the present invention include phenol, cresol, xylenol, resorcinol, etc., and the aldehydes include formaldehyde, paraformaldehyde, furfural, etc. As the acidic catalyst, inorganic acids such as hydrochloric acid and sulfuric acid, or organic acids such as oxalic acid and benzenesulfonic acid are used. The reaction is carried out under reflux at a temperature of about 90 to 10,000, with a molar ratio of aldehydes to phenol of 1 or less, similar to the general method for producing novolac resins. After the reaction is complete, add an alkaline substance such as caustic soda, caustic potash, calcium hydroxide, etc. to pH 6~
Neutralize to 7 and leave to cool. The reaction product liquid is separated into an aqueous phase and a resin phase by cooling, and the upper aqueous phase is separated and removed, and a surfactant, polyvinyl alcohol, and an oxide or hydroxide of an alkali metal or zinc are added to the resin liquid. Surfactants act as foaming regulators.
Silicon-based (for example, manufactured by UCC, L-52 stop L-5
30, L-5320, etc.), nonionic activators (e.g., polyoxyethylene sorbitan monolaurate (Kao Atlas Co., Ltd., Tween 20), polyoxyethylene sorbitan monopalmitate (Kao Atlas Co., Ltd., Tween 40), polyoxyethylene nonylphenol Solbon F80 (manufactured by Toho Chemical Co., Ltd.), etc.) are used. The amount of these additions is 0 for 10 parts of phenols (hereinafter referred to as parts by weight).
.. 5 to 3 parts to completely dissolve it in the resin phase.
Polypynyl alcohol is added as an aqueous solution in an amount of 0.05 to 1 part per 100 parts of phenol to completely disperse and dissolve it in the resin phase. In addition, oxides or hydroxides of alkali metals (calcium, barium, magnesium, etc.) or zinc act as hardening aids, and when the purpose is to produce low-foaming products, 10 parts of phenols are used. 2 to 10 parts of this, or 0.3 parts for highly foamed products.
Add ~2 parts. When these are completely dissolved in the resin phase, heated and dehydrated, a transparent novolac resin is obtained. heating,
A foaming agent, a curing agent, and if necessary, a scale agent, pigment, etc. are added to the resin phase after dehydration. Examples of the blowing agent include substances that generate gas when heated, such as dinitrosobentamethylenetetramine, azodicarbonamide, benzenesulfonyl hydrazide derivatives, toluenesulfonyl hydrazide derivatives, azoisobutyrodinitrile, and sodium bicarbonate. This is added in an amount of 1 to 12 parts per 10$ of novolak resin. Hexamethylenetetramine and paraformaldehyde are used as curing agents, and are added in an amount of 8 to 16 parts per 100 parts of the novolac resin. Add 1 to 3 parts of other nourishing agents such as stearic acid, calcium stearate, and magnesium stearate, coloring agents (dyes, pigments), etc., as appropriate, mix thoroughly using a mixer such as a pole mill or ribbon blender, and further heat roll, The mixture is thoroughly kneaded and pulverized using a co-kneader or the like to obtain a foamable composition. A foam having uniform to fine particles can be obtained by molding this composition into a tablet or plate shape at a low temperature and placing it in a molding box or mold and heating it in a heating furnace to foam and harden it. Since the novolak resin according to the present invention dissolves surfactant and polyvinyl alcohol during its synthesis process, it has fine foamed particles and is homogeneous due to the bubble control and bubble stabilization effect of the gas generated during foam curing. gives a foam.

更に硬化肋剤として加えた金属化合物はホルムアルデヒ
ド塩又はノボラック樹脂との金属化合物として存在して
いるので発泡体を不均質にすることもなく、良好な成型
性を有するフェノール樹脂を与える。実施例 1 風 ノボラツク樹脂の製造 フエ/−ル 100礎部、37%ホルマリン 635部
に触媒としてシュウ酸 7部を加え、乳化後2時間還流
下に反応を行い、2の重量%カ性ソーダ水溶液 22部
で中和したのち放冷する。
Furthermore, since the metal compound added as a curing agent exists as a metal compound with formaldehyde salt or novolac resin, the foam does not become non-uniform and a phenol resin having good moldability is provided. Example 1 Production of wind novolak resin 7 parts of oxalic acid was added as a catalyst to 635 parts of 37% formalin and 100 parts of foam was emulsified. After emulsification, the reaction was carried out under reflux for 2 hours, and a 2% by weight caustic soda aqueous solution was added. After neutralizing with 22 parts, leave to cool.

上層の水性相を除いた樹脂液に界面活性剤としてトウィ
ーン20を11部加えて完全に溶解させる。つぎにポリ
ビニルアルコールの1の重量%水溶液を2の部加えて同
じく完全に溶解させる。最後に硬化助剤として酸化マグ
ネシウム 5部を加えて加熱脱水を行い、融点が70q
○の赤褐色透明のノボラック樹脂を得た。【B)発泡用
組成物の製造 得られたノボラック樹脂 100部に硬化剤としてへキ
サメチレンテトラミン 15部、発泡剤としてジニトロ
ソベンタメチレンテトラミン6部、ステアリン酸 2部
をボールミルを用いて粉砕混合し、高温側80〜90q
0、低温側25〜30℃のロールを用いて8〜10分間
濠練し、冷却後粉砕して発泡用紙成物を得た。
11 parts of Tween 20 as a surfactant is added to the resin liquid from which the upper aqueous phase has been removed and completely dissolved. Next, 2 parts of a 1% by weight aqueous solution of polyvinyl alcohol are added and also completely dissolved. Finally, 5 parts of magnesium oxide was added as a hardening aid and heated and dehydrated until the melting point was 70q.
A reddish-brown transparent novolak resin with a rating of ○ was obtained. [B) Manufacture of foaming composition 100 parts of the obtained novolak resin, 15 parts of hexamethylenetetramine as a hardening agent, 6 parts of dinitrosobentamethylenetetramine as a foaming agent, and 2 parts of stearic acid were ground and mixed using a ball mill. , high temperature side 80~90q
The mixture was kneaded for 8 to 10 minutes using rolls at a low temperature of 25 to 30°C, cooled, and then crushed to obtain a foamed paper composition.

{q 発泡成形 得られた発泡用組成物 310夕を31肌×31仇、厚
み2.5側の板に成形し、31弧×31仇×5(深さ)
弧の成形箱中に入れ、加熱炉中12000で4ぴ分、続
いて160℃で30分間発泡ごせた。
{q Foam molding The obtained foaming composition 310 layers was molded into a board with 31 sides x 31 sides and a thickness of 2.5 mm, and 31 arcs x 31 inches x 5 (depth)
It was placed in an arc molding box and foamed in a heating oven at 12,000° C. for 4 minutes, and then at 160° C. for 30 minutes.

得られた発泡体の嵩比重は0.050であり、微細な発
泡粒子を有する均質な高発泡体が得られた。実施例 2
凶 /ボラック樹脂の製造 実施例1凶において酸化マグネシウムの代りに、水酸化
カルシウム 35部を加えて加熱脱水を行い、融点が7
5ooの赤褐色透明のノボラック樹脂を得た。
The bulk specific gravity of the obtained foam was 0.050, and a homogeneous highly foamed material having fine foamed particles was obtained. Example 2
In Example 1 of Production of Borac Resin, 35 parts of calcium hydroxide was added instead of magnesium oxide, and heat dehydration was performed to obtain a melting point of 7.
A reddish-brown transparent novolac resin of 50 ml was obtained.

‘Bー 発泡用組成物の製造 得られた/ボラック樹脂 100部にへキサメチレンテ
トラミン 15部、ジニトロソベンタメチレンテトラミ
ン 2部、ステアリン酸 2部、顔料 2部をボールミ
ルを用いて粉砕混合し、高温側90〜100oo、低温
側25〜30℃のロールを用いて5〜10分間混練をし
、冷却後粉砕して発泡用組成物を得た。
'B - Manufacture of foaming composition 100 parts of the obtained/borac resin were ground and mixed with 15 parts of hexamethylenetetramine, 2 parts of dinitrosobentamethylenetetramine, 2 parts of stearic acid, and 2 parts of pigment using a ball mill. The mixture was kneaded for 5 to 10 minutes using rolls with a temperature of 90 to 100° C. on the high temperature side and 25 to 30° C. on the low temperature side, and after cooling, was crushed to obtain a foaming composition.

に} 発泡成形 得られた発泡組成物 17夕を直径5伽、厚さ1伽のタ
ブレットに成形し、これを金型に入れて150qoの加
熱炉中で30分間加熱し発泡硬化させた。
} Foam molding The resulting foamed composition No. 17 was molded into a tablet with a diameter of 5 mm and a thickness of 1 mm, which was placed in a mold and heated in a 150 qo heating furnace for 30 minutes to foam and harden.

得られた発泡体の高比重は0.43であり、微細な発泡
粒子を有する均質な低発泡体が得られた。比較例 1 ■ ノボラック樹脂の製造 フェノール 100庇部、37%ホルマリン635部に
触媒としてシュウ酸 7部を加えて乳化後、2時間還流
下反応を行い、2の重量%のカ性ソーダ水溶液 22部
で中和したのち放冷し、上層の水性相を除いた残りの樹
脂液を加熱脱水を行って融点が70qCのノボラック樹
脂を得た。
The high specific gravity of the obtained foam was 0.43, and a homogeneous low-foamed material having fine foamed particles was obtained. Comparative Example 1 ■ Manufacture of novolak resin 100 parts of phenol and 635 parts of 37% formalin were emulsified by adding 7 parts of oxalic acid as a catalyst, followed by a reaction under reflux for 2 hours, followed by 22 parts of a 2% by weight aqueous solution of caustic soda. After neutralizing with water, the mixture was allowed to cool, and the remaining resin liquid after removing the upper aqueous phase was heated and dehydrated to obtain a novolac resin with a melting point of 70 qC.

‘B} 発泡用組成物の製造得られたノポラック樹脂
100部にへキサメチレンテトラミン 15部、ジニト
ロソベンタメチレンテトラミン 6部、トウィーン20
1部、ステアリン酸 1部をボールミルで粉砕混合して
実施例1{Bーと同様にして発泡用組成物を得た。
'B} Manufacture of foaming composition Obtained nopolak resin
100 parts, 15 parts of hexamethylenetetramine, 6 parts of dinitrosobentamethylenetetramine, 20 parts of Tween
1 part of stearic acid and 1 part of stearic acid were pulverized and mixed in a ball mill to obtain a foaming composition in the same manner as in Example 1 {B--.

{C} 発泡成形 得られた発泡用組成物 310夕を実施例1‘qと同様
にして発泡硬化させて高比重0.048の発泡体を得た
が、発泡粒子が粗く不均質であった。
{C} Foam molding The obtained foaming composition 310 was foamed and cured in the same manner as in Example 1'q to obtain a foam with a high specific gravity of 0.048, but the foamed particles were coarse and non-uniform. .

比較例 2 比較例1風のノボラック樹脂 10接触こへキサメチレ
ンテトラミン 15部、ジニトロソベンタメチレンテト
ラミン 2部、トウィーン201部、酸化マグネシウム
2部、ステアリン酸2部、顔料 2部を実施例2{B
ーと同様にして発泡用組成物を得た。
Comparative Example 2 Novolak resin similar to Comparative Example 1: 15 parts of catalytic hexamethylenetetramine, 2 parts of dinitrosobentamethylenetetramine, 201 parts of Tween, 2 parts of magnesium oxide, 2 parts of stearic acid, and 2 parts of pigment in Example 2 { B
A foaming composition was obtained in the same manner as described above.

Claims (1)

【特許請求の範囲】[Claims] 1 フエノール類とアルデヒド類を酸性触媒存在下反応
させ、反応生成物を中和後樹脂相から水性相を分離除去
し、樹脂相に界面活性剤、ポリビニルアルコール及びア
ルカリ土金属もしくは亜鉛の酸化物もしくは水酸化物を
添加し、加熱、脱水し、次いで発泡剤、硬化剤を添加、
混練したのち加熱し発泡、硬化させることを特徴とする
フエノール樹脂発泡体の製造法。
1. Phenols and aldehydes are reacted in the presence of an acidic catalyst, the reaction product is neutralized, the aqueous phase is separated and removed from the resin phase, and a surfactant, polyvinyl alcohol, and alkaline earth metal or zinc oxide or Add hydroxide, heat and dehydrate, then add foaming agent and curing agent,
A method for producing a phenolic resin foam, which comprises kneading, heating, foaming, and curing.
JP10092679A 1979-08-08 1979-08-08 Method for producing phenolic resin foam Expired JPS6028297B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10092679A JPS6028297B2 (en) 1979-08-08 1979-08-08 Method for producing phenolic resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10092679A JPS6028297B2 (en) 1979-08-08 1979-08-08 Method for producing phenolic resin foam

Publications (2)

Publication Number Publication Date
JPS5625434A JPS5625434A (en) 1981-03-11
JPS6028297B2 true JPS6028297B2 (en) 1985-07-04

Family

ID=14286947

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10092679A Expired JPS6028297B2 (en) 1979-08-08 1979-08-08 Method for producing phenolic resin foam

Country Status (1)

Country Link
JP (1) JPS6028297B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61157195U (en) * 1985-03-22 1986-09-29

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60152550A (en) * 1984-01-19 1985-08-10 Kanebo Ltd Material for master model

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61157195U (en) * 1985-03-22 1986-09-29

Also Published As

Publication number Publication date
JPS5625434A (en) 1981-03-11

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