JPH0575778B2 - - Google Patents
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- Publication number
- JPH0575778B2 JPH0575778B2 JP2295429A JP29542990A JPH0575778B2 JP H0575778 B2 JPH0575778 B2 JP H0575778B2 JP 2295429 A JP2295429 A JP 2295429A JP 29542990 A JP29542990 A JP 29542990A JP H0575778 B2 JPH0575778 B2 JP H0575778B2
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- Prior art keywords
- phenolic resin
- foam
- acid
- present
- parts
- Prior art date
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Description
〔産業上を利用分野〕
本発明は、特に改善された耐脆性、断熱性能を
有するフエノール樹脂発泡体に関するものであ
り、さらに詳しくは、未変性でん粉を使用したフ
エノール樹脂発泡体に関するものである。
本発明に係るフエノール樹脂発泡体は、主に外
壁材、内壁材、天井材、屋根下地材、床下地材、
雨戸などの建築用断熱材、貯蔵タンク、冷凍冷蔵
倉庫、パイプなどの工業用断熱材として使用され
るが、その他種々の用途にも適用される。
〔従来の技術〕
近年、フエノール樹脂発泡体は、ポリスチレン
樹脂、ポリウレタン樹脂、ポリエチレン樹脂等の
熱可塑性樹脂発泡体では得られない耐熱性、耐火
性、低発煙性等の優れた諸特性を有するため、そ
の有用性に大きな注目が寄せられている。
しかしながら、前記フエノール樹脂発泡体はフ
エノール樹脂固有の脆弱性のため、表面脆性(以
下フライアビリテイーという)が悪く、粉化した
り、表面材と自己接着した場合、表面材が剥がれ
たりするという現象が見られ、又、気泡膜が弱く
崩解し易いため、断熱性能が悪かつたり、断熱性
能の経時低下が非常に大きいという欠点を有し、
その改善が強く要望されているのが現状である。
このような問題点を改善方法の一つとして、特
開昭59−219343号公報に記載のフエノール樹脂発
泡体の製造方法を挙げることができる。この従来
技術の要旨とするところは、液状のレゾール型フ
エノール樹脂初期縮合物、発泡剤、界面活性剤、
整泡剤、酸性硬化剤等を用いてレゾール型フエノ
ール樹脂発泡体を製造する方法において、前記全
成分を混合している途中に、例えばでん粉類とア
クリロニトリルあるいはアクリル酸とを反応させ
て得られるアクリロニトリルグラフト化加水分解
物あるいはアクリル酸グラフト化合物のような、
でん粉系高分子である高吸水性物質の粉末を添加
したことを特徴とするフエノール樹脂発泡体の製
造方法である。しかしながら、この方法によれ
ば、従前の発泡体より、表面脆性、接着性、防火
性等の面で優れた発泡体を得ることが可能である
とされているものの、断熱性能については充分な
ものとは言い難く、特に経時に伴う断熱性能の低
下抑制の観点からの検討はなされていない。
〔発明が解決しようとする問題点〕
本発明は以上のような従来技術の問題点に鑑み
なされたものであり、その目的とするところは前
記従来技術におけるフエノール樹脂発泡体の大き
なフライアビリテイーおよび低い断熱性能又は、
経時に伴なう断熱性能の低下という欠点を解決
し、また、耐熱性、耐火性、低発煙性などの優れ
た諸特性を損なわずに具備したフエノール樹脂発
泡体を提供することである。
〔問題点を解決すくための手段〕
本発明者等は、上記欠点を解決するために、鋭
意研究を行つた結果、フエノール樹脂発泡体を製
造する際に、未変性でん粉を加えることによつて
得られる前記発泡体は、フライアビリテイーが非
常に小さく、又、経時に伴う低下の少ない優れた
断熱性能を有することを見出し、本発明を完成さ
せるに至つたものである。
すなわち、本発明は、液状フエノール樹脂、発
泡剤、酸性硬化剤、整泡剤および未変性でん粉を
必須成分とする配合組成物を発泡硬化させてなる
フエノール樹脂発泡体であつて、でん粉類の配合
量が固形樹脂分に換算した該フエノール樹脂100
重量部に対し、0.1〜50重量部であることを特徴
とするものである。
本発明で使用される未変性でん粉は、コーンス
ターチ、馬鈴しよでん粉等が挙げられるが、これ
らに限定されるものではない。
又、未変性でん粉の配合量は、固形樹脂分に換
算したフエノール樹脂100重量部に対して0.1〜50
重量部であり、0.1重量部未満では本発明の目的
を達成できず、良好なフライアビリテイー、断熱
性能は期待できない。逆に50重量部を超えると、
硬化特性が著しく悪くなる。更に、本発明におけ
る未変性でん粉の配合方法は、液状フエノール樹
脂の製造段階、あるいは製造後に配合しておく方
法や、発泡性樹脂組成物の調製時に配合する方法
などがあるが、いずれの方法でもよく、特に限定
されるものではない。
本発明に係る液状フエノール樹脂としては例え
ばフエノール、o−又はm−ないし、p−クレゾ
ール等のクレゾール類、3,4−又は3,5−キ
シレノール等のキシレノール類、p−ターシヤリ
ーフエノール等のC3以上のアルキル基を有する
アルキルフエノール類、カテコール、レゾルシ
ン、ピロガロール、ビスフエノールA、ビスフエ
ノールF等の多価フエノール類等の単独又は混合
物であるフエノール類1モルに対し、ホルマリ
ン、パラホルムアルデヒド、グリオキザール等の
単独又は混合物であるアルデヒド類0.8〜3.0モル
をアルカリ金属の水酸化物、アルカリ土類金属の
酸化物又は水酸化物、アミン類、アンモニア等の
アルカリ性触媒の単独又は混合物の存在下に、好
ましくは50〜100℃で反応させたのち必要に応じ
て該触媒を硫酸、p−トルエンスルホン酸等の無
機、有機酸等で中和し、減圧下で脱水濃縮させて
得られる25℃での粘度が500〜200000センチポイ
ズのレゾール型フエノール樹脂が特に好適に使用
されるが、塩酸、シユウ酸、p−トルエンスルホ
ン酸等の無機酸若しくは有機酸又は酢酸亜鉛等の
二価金属塩等を触媒として製造されるノボラツク
型フエノール樹脂、又は酢酸鉛等の二価金属塩等
を触媒として製造されるベンジルエーテル型フエ
ノール樹脂等を含むレゾール型フエノール樹脂主
体の混合樹脂も使用される。
本発明で使用される発泡剤としては、特に以下
に述べるものに限定されるものではないが、例え
ば塩化メチレン等のハロゲン化炭化水素類、トリ
クロロモノフルオロメタン、1,1,2−トリク
ロロトリフルオロエタン、1,2−ジクロロテト
ラフルオロエタン等の弗素含有ハロゲン化炭化水
素類、ブタン、ペンタン、ヘキサン等の脂肪族炭
化水素類、さらには酸を混合することで炭酸ガス
等の気体を発生させるような重曹等の化学的反応
発泡剤の単独又は混合物が挙げられ、その配合量
は、固形樹脂分に換算したフエノール樹脂100重
量部に対して1〜50重量部である。
本発明で使用される硬化剤としては、特に以下
に述べるものに限定されるものではないが、例え
ば、パラトルエンスルホン酸、キシレンスルホン
酸、メタキシレンスルホン酸、ベンゼンスルホン
酸、フエノールスルホン酸、ポリメリツクスルホ
ン酸、スチレンスルホン酸等の有機スルホン酸類
の他、リン酸、硫酸等の無機酸類の単独、又は混
合物が挙げられ、その配合量は固形樹脂分に換算
したフエノール樹脂100重量部に対し3〜100重量
部である。
本発明で使用される整泡剤としては、特に以下
に述べるものに限定されるものではないが、例え
ばポリシロキサン系、ポリオキシエチレンソルビ
タン脂肪酸エステル、ヒマシ油エチレンオキサイ
ド付加物、アルキルフエノールエチレンオキサイ
ド付加物等の単独又はそれらの混合物があげら
れ、その配合量は、固形樹脂分に換算したフエノ
ール樹脂100重量部に対し0.3〜10重量部である。
更に、一般に使われている硬化促進剤、難燃剤、
中和剤、有機系又は無機系充填剤あるいは着色剤
等の添加剤の必要に応じて使用することもでき
る。
次に、本発明のフエノール樹脂発泡体を得るに
は、以上の各成分を適宜に選択配合して均一に混
合させて発泡性樹脂組成物を調製した後、所定の
成形型に注入して発泡硬化させる。例えば、あら
かじめ未変性でん粉、整泡剤を内添したフエノー
ル樹脂システム液に必要に応じて難燃剤、中和
剤、有機系又は無機系充填剤、顔料等を配合し、
更に所定量の発泡剤および硬化剤を順次又は同時
的に投入しつつ撹拌混合し、あらかじめ30〜90℃
に温調させた所定の型に注入した加圧下に発泡硬
化させて目的の発泡体を得る。
工業的な混合方法としては、例えば、バツチ式
による高速撹拌による方法、連続的な高速撹拌に
よる方法、スプレー混合方式による方法、フロス
方式による方法等がある。
又、成型方法としては例えば、上記混合方法に
より得られた発泡性樹脂組成物をエンドレスコン
ベア上に流出させる方法、スポツト的に流出させ
て部分的に発泡させる方法、モールド内で加圧発
泡させる方法、ある大きさの空間中に投入して発
泡ブロツクを作る方法、空洞中に圧入しながら充
填発泡させる方法等がある。
なお、本発明により得られる発泡体、例えば酸
性硬化剤としてフエノールスルホン酸水溶液を用
いて得られた発泡体は、約50℃以上の雰囲気温度
下で約30分以上熱処理を行うことにより、その色
調がピンク色から暗紫色に変色するという発泡用
樹脂組成物の品質管理上極めて有利な特性を有し
ている。
〔作用〕
本発明において、講じられた手段の作用は明確
ではないが、以下のように考えられる。
未変性でん粉は酸性硬化剤により糖類に分解さ
れ、発泡体を形成する気泡膜の表面塑性(ねば
り)を上昇させる作用を持つと考えられ、発泡体
のフエノール樹脂固有の脆弱性により生じる気泡
膜の脆さ、或いはその脆さに起因する膜の破れを
なくし気泡膜中に内包する、空気よりも熱伝導率
の小さい発泡用ガスの移動放出を防止するものと
考えられる。
〔実施例〕
次に実施例、比較例を挙げて本発明を具体的に
説明するが、これらにより本発明は何ら制限を受
けるものではない。尚、例中に於ける部および%
は重量部、重量%を表わす。
実施例 1
フエノール300Kgと濃度47%ホルマリン346Kgを
撹拌機、還流管、温度計付反応釜中に仕込んだ。
次いで20%水酸化ナトリウム水溶液30Kgを投入
して、常温から90℃迄約60分で温度を上昇させ、
同温度で75分間反応を継続させた。反応物の粘度
は30cp/50℃であつた。ついで反応物を40℃に
冷却し、10%硫酸水溶液を加えPHを6.5に調整し、
反応釜を60mmHgに減圧して濃縮を行い25℃に於
ける粘度1800cp、固形樹脂分81%(180℃熱板上
で30分乾固させた不揮発分)の樹脂470Kgを得た。
得られたフエノール樹脂100Kgにコーンスターチ
2.43Kgを加え、整泡剤としてCX−100(商品名、
第一工業製薬(株)製、ヒマシ油エチレンオキサイド
付加物)、難燃剤としてポリリン酸アンモン3Kg
を混合したものを液とし、発泡剤としてのフロ
ン113を液、硬化剤としての67%フエノールス
ルホン酸を液とし、PA−210フエノール発泡用
発泡機(商品名、東邦機械(株)製)を用い、液/
液/液=100部/25部/35部の比率で混合、
70℃に加熱した化粧鋼板を面材として1800×900
×25mmの発泡体を作成した。この時のゲルタイム
は120秒であつた。この発泡体を常温で4日間放
置後の密度(JISA9514)、フライアビリテイー
(ASTM−421)、面材との結合力(以下に示す測
定法)、酸素指数(JIS K7201)燃伝導率(熱線
法)を測定した。又、熱伝導率は、30日放置後に
も測定した。
ここで面材との結合力は、25×150mmの面材付
発泡体を切り出し、表面材端部に直径5mmの穴を
開け、そこにばね計りを引掛けて引き上げ表面材
が発泡体から剥がれた時のばね計りの指示値を該
結合力として表わしたものである。得られた発泡
体は、表−1に示すように外観の良好なフライア
ビリテイーの小さい、面材との結合力の強い、経
時に伴う低下の小さい優れた断熱性能を有し、さ
らに難燃性をそこなわない非常に優れたものであ
つた。
比較例 1
実施例1に準じてコーンスターチを添加せず発
泡体を作成した。得られた発泡体は、表1に示す
ようにフライアビリテイーの大きい、面材との結
合力の弱い、又断熱性能の経時による劣化の非常
に大きなものであつた。
[Industrial Field of Application] The present invention relates to a phenolic resin foam having particularly improved brittleness resistance and heat insulation performance, and more particularly to a phenolic resin foam using unmodified starch. The phenolic resin foam according to the present invention is mainly used for exterior wall materials, interior wall materials, ceiling materials, roof base materials, floor base materials,
It is used as a thermal insulating material for buildings such as shutters, storage tanks, refrigerated warehouses, pipes, etc., but it is also used for a variety of other purposes. [Prior Art] In recent years, phenolic resin foams have become popular because they have excellent properties such as heat resistance, fire resistance, and low smoke emission that cannot be obtained with thermoplastic resin foams such as polystyrene resins, polyurethane resins, and polyethylene resins. , its usefulness has received a lot of attention. However, due to the inherent fragility of phenolic resin, the phenolic resin foam has poor surface brittleness (hereinafter referred to as flyability), and if it becomes powder or self-adhesively adheres to the surface material, the surface material may peel off. In addition, because the bubble membrane is weak and easily disintegrates, it has the disadvantage of poor insulation performance and a very large decline in insulation performance over time.
At present, there is a strong demand for improvement. One method for improving these problems is the method for producing a phenolic resin foam described in Japanese Patent Application Laid-open No. 59-219343. The gist of this prior art is that a liquid resol type phenolic resin initial condensate, a blowing agent, a surfactant,
In a method for producing a resol type phenolic resin foam using a foam stabilizer, an acidic curing agent, etc., acrylonitrile obtained by, for example, reacting starch with acrylonitrile or acrylic acid is added during mixing of all the components. such as grafted hydrolysates or acrylic acid graft compounds,
This is a method for producing a phenolic resin foam, characterized in that powder of a highly water-absorbing substance, which is a starch-based polymer, is added. However, although this method is said to be able to produce foams that are superior to conventional foams in terms of surface brittleness, adhesion, fire retardancy, etc., the insulation performance is still insufficient. It is difficult to say that this is the case, and no study has been made particularly from the viewpoint of suppressing the decline in heat insulation performance over time. [Problems to be Solved by the Invention] The present invention has been made in view of the problems of the prior art as described above, and its purpose is to solve the high flyability and Low insulation performance or
It is an object of the present invention to provide a phenolic resin foam that solves the drawback of deterioration in heat insulation performance over time and has excellent properties such as heat resistance, fire resistance, and low smoke emission without impairing it. [Means for solving the problem] In order to solve the above-mentioned drawbacks, the present inventors conducted intensive research and found that by adding unmodified starch when producing a phenolic resin foam. It was discovered that the resulting foam has very low flyability and excellent heat insulating performance with little deterioration over time, leading to the completion of the present invention. That is, the present invention provides a phenolic resin foam obtained by foaming and curing a blended composition containing a liquid phenolic resin, a blowing agent, an acidic curing agent, a foam stabilizer, and an unmodified starch as essential components, and which contains starch. The amount of the phenolic resin converted to solid resin content is 100
It is characterized by being 0.1 to 50 parts by weight. The unmodified starch used in the present invention includes, but is not limited to, corn starch, potato starch, and the like. In addition, the amount of unmodified starch added is 0.1 to 50 parts by weight of phenolic resin converted to solid resin content.
If it is less than 0.1 part by weight, the object of the present invention cannot be achieved and good flyability and heat insulation performance cannot be expected. Conversely, if it exceeds 50 parts by weight,
Curing properties become significantly worse. Furthermore, methods for blending unmodified starch in the present invention include a method in which it is blended at the manufacturing stage of the liquid phenolic resin, a method in which it is blended after the production, and a method in which it is blended at the time of preparing the foamable resin composition. Well, there are no particular limitations. Examples of the liquid phenolic resin according to the present invention include phenol, cresols such as o- or m- or p-cresol, xylenols such as 3,4- or 3,5-xylenol, and C such as p-tertiary leaf phenol. Formalin, paraformaldehyde, glyoxal per mole of phenols, either alone or in mixtures, such as alkylphenols having three or more alkyl groups, catechol, resorcinol, pyrogallol, bisphenol A, bisphenol F, and other polyvalent phenols. 0.8 to 3.0 mol of aldehydes, either alone or as a mixture, in the presence of an alkaline catalyst, such as an alkali metal hydroxide, an alkaline earth metal oxide or hydroxide, an amine, or an alkaline catalyst such as ammonia, alone or as a mixture; Preferably, after reacting at 50 to 100°C, the catalyst is neutralized with an inorganic or organic acid such as sulfuric acid or p-toluenesulfonic acid, etc., and then dehydrated and concentrated under reduced pressure. Resol-type phenolic resins with a viscosity of 500 to 200,000 centipoise are particularly preferably used, but inorganic or organic acids such as hydrochloric acid, oxalic acid, p-toluenesulfonic acid, or divalent metal salts such as zinc acetate are used as catalysts. Also used are novolac-type phenolic resins produced, or mixed resins mainly composed of resol-type phenolic resins, including benzyl ether-type phenolic resins produced using divalent metal salts such as lead acetate as catalysts. The blowing agent used in the present invention is not particularly limited to those described below, but includes, for example, halogenated hydrocarbons such as methylene chloride, trichloromonofluoromethane, 1,1,2-trichlorotrifluoromethane, etc. Gases such as carbon dioxide can be generated by mixing fluorine-containing halogenated hydrocarbons such as ethane and 1,2-dichlorotetrafluoroethane, aliphatic hydrocarbons such as butane, pentane, and hexane, and even acids. Chemically reactive foaming agents such as sodium bicarbonate may be used alone or in combination, and the amount thereof is 1 to 50 parts by weight per 100 parts by weight of the phenolic resin calculated as solid resin content. The curing agent used in the present invention is not particularly limited to those described below, but examples include para-toluenesulfonic acid, xylenesulfonic acid, meta-xylenesulfonic acid, benzenesulfonic acid, phenolsulfonic acid, and polymeric acid. In addition to organic sulfonic acids such as sulfonic acid and styrene sulfonic acid, inorganic acids such as phosphoric acid and sulfuric acid may be used singly or as a mixture. ~100 parts by weight. Foam stabilizers used in the present invention are not particularly limited to those described below, but include, for example, polysiloxanes, polyoxyethylene sorbitan fatty acid esters, castor oil ethylene oxide adducts, and alkylphenol ethylene oxide adducts. The compounding amount thereof is 0.3 to 10 parts by weight per 100 parts by weight of the phenolic resin calculated as solid resin content.
Furthermore, commonly used curing accelerators, flame retardants,
Additives such as a neutralizing agent, an organic or inorganic filler, or a coloring agent may also be used as required. Next, in order to obtain the phenolic resin foam of the present invention, a foamable resin composition is prepared by suitably selecting and blending each of the above components and mixing them uniformly, and then injected into a predetermined mold and foamed. Let it harden. For example, if necessary, flame retardants, neutralizers, organic or inorganic fillers, pigments, etc. are blended into a phenolic resin system liquid to which unmodified starch and foam stabilizer have been internally added.
Furthermore, predetermined amounts of blowing agent and curing agent are added sequentially or simultaneously and mixed with stirring, and heated to 30 to 90℃ in advance.
The foam is injected into a predetermined mold at a controlled temperature and then foamed and cured under pressure to obtain the desired foam. Examples of industrial mixing methods include a batch type high-speed stirring method, a continuous high-speed stirring method, a spray mixing method, a floss method, and the like. Examples of the molding method include a method in which the foamable resin composition obtained by the above-mentioned mixing method is flowed onto an endless conveyor, a method in which the foamable resin composition is flowed out in spots and foamed partially, and a method in which the foamable resin composition is foamed under pressure in a mold. There are two methods: a method of making a foam block by inserting the material into a space of a certain size, and a method of filling and foaming the material by press-fitting it into a cavity. Note that the foam obtained by the present invention, for example, the foam obtained using an aqueous phenolsulfonic acid solution as an acidic curing agent, can be heat-treated at an ambient temperature of about 50°C or higher for about 30 minutes or more to change its color tone. It has an extremely advantageous property in terms of quality control of foaming resin compositions, in that it changes color from pink to dark purple. [Effect] Although the effect of the measures taken in the present invention is not clear, it is thought to be as follows. Unmodified starch is decomposed into saccharides by an acidic curing agent, and is thought to have the effect of increasing the surface plasticity (stickiness) of the cell membrane that forms the foam. It is thought that this eliminates fragility or breakage of the membrane due to the fragility, and prevents movement and release of the foaming gas, which has a lower thermal conductivity than air and is contained in the bubble membrane. [Example] Next, the present invention will be specifically explained with reference to Examples and Comparative Examples, but the present invention is not limited in any way by these. In addition, parts and % in examples
represents parts by weight, weight %. Example 1 300 kg of phenol and 346 kg of 47% formalin were charged into a reaction vessel equipped with a stirrer, a reflux tube, and a thermometer. Next, 30 kg of 20% sodium hydroxide aqueous solution was added, and the temperature was raised from room temperature to 90°C in about 60 minutes.
The reaction was continued for 75 minutes at the same temperature. The viscosity of the reactant was 30 cp/50°C. Then, the reaction mixture was cooled to 40°C, and a 10% aqueous sulfuric acid solution was added to adjust the pH to 6.5.
The pressure of the reaction vessel was reduced to 60 mmHg and concentration was performed to obtain 470 kg of resin with a viscosity of 1800 cp at 25°C and a solid resin content of 81% (non-volatile content after drying on a 180°C hot plate for 30 minutes).
Add cornstarch to 100kg of the obtained phenolic resin.
2.43Kg was added and CX-100 (trade name,
Daiichi Kogyo Seiyaku Co., Ltd., castor oil ethylene oxide adduct), ammonium polyphosphate 3Kg as a flame retardant
A mixture of the above is used as a liquid, Freon 113 is used as a foaming agent, and 67% phenolsulfonic acid is used as a hardening agent. used, liquid/
Mix at a ratio of liquid/liquid = 100 parts/25 parts/35 parts,
1800 x 900 with decorative steel plate heated to 70℃ as surface material
A foam with a size of 25 mm was created. The gel time at this time was 120 seconds. After leaving this foam at room temperature for 4 days, the density (JISA9514), flyability (ASTM-421), bond strength with the surface material (measurement method shown below), oxygen index (JIS K7201), and flame conductivity (hot wire method) was measured. The thermal conductivity was also measured after being left for 30 days. Here, the bonding force with the facing material is determined by cutting out a 25 x 150 mm foam with a facing material, making a hole with a diameter of 5 mm at the end of the facing material, hooking a spring gauge there, and pulling it up until the facing material is peeled off from the foam. The value indicated by the spring meter when the force is applied is expressed as the bonding force. As shown in Table 1, the obtained foam has a good appearance, low flyability, strong bonding strength with the facing material, excellent heat insulation performance with little deterioration over time, and is also flame retardant. It was a very good product that did not harm the sex. Comparative Example 1 A foam was created according to Example 1 without adding cornstarch. As shown in Table 1, the obtained foam had a high flyability, a weak bonding force with the face material, and a very large deterioration in heat insulation performance over time.
【表】【table】
本発明に係るフエノール樹脂発泡体は、フライ
アビリテイーおよび表面材との接着力が大巾に向
上するため、施工時の作業性が良好になり、又経
時に伴う熱伝導率を低下の少ない優れた断熱性能
を有するため施工コストを低減できる。更には、
耐熱性、耐火性、低発煙性などの優れた諸物性を
そこなわない等の利点を有する
The phenolic resin foam according to the present invention greatly improves flyability and adhesion to the surface material, so it improves workability during construction and has excellent thermal conductivity with little decline over time. Because it has excellent heat insulation performance, construction costs can be reduced. Furthermore,
It has the advantage of not compromising its excellent physical properties such as heat resistance, fire resistance, and low smoke emission.
Claims (1)
製泡剤および未変性でん粉を必須成分とする配合
組成物を発泡硬化させてなるフエノール樹脂発泡
体であつて、未変性でん粉の配合量が固形樹脂分
に換算した該フエノール樹脂100重量部に対し、
0.1〜50重量部であることを特徴とするフエノー
ル樹脂発泡体。1 Liquid phenolic resin, foaming agent, acidic curing agent,
A phenolic resin foam obtained by foaming and curing a blended composition containing a foaming agent and unmodified starch as essential components, in which the amount of unmodified starch is based on 100 parts by weight of the phenolic resin converted to solid resin content. ,
A phenolic resin foam having a content of 0.1 to 50 parts by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29542990A JPH03179041A (en) | 1990-11-02 | 1990-11-02 | Phenolic resin foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29542990A JPH03179041A (en) | 1990-11-02 | 1990-11-02 | Phenolic resin foam |
Related Parent Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7926585A Division JPS61238833A (en) | 1985-04-16 | 1985-04-16 | Phenolic resin foam |
| JP7926588A Division JPS63288482A (en) | 1988-03-31 | 1988-03-31 | Recording or reproducing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03179041A JPH03179041A (en) | 1991-08-05 |
| JPH0575778B2 true JPH0575778B2 (en) | 1993-10-21 |
Family
ID=17820490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29542990A Granted JPH03179041A (en) | 1990-11-02 | 1990-11-02 | Phenolic resin foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03179041A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11326036B2 (en) | 2018-04-27 | 2022-05-10 | Asahi Kasei Construction Materials Corporation | Flame-retardant phenolic resin foam |
| CN110684316B (en) * | 2019-11-12 | 2022-03-08 | 江阴市威腾铝箔合成材料有限公司 | Low-thermal-conductivity phenolic foam material and preparation method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59219343A (en) * | 1983-05-27 | 1984-12-10 | Ig Tech Res Inc | Production of phenolic resin foam |
-
1990
- 1990-11-02 JP JP29542990A patent/JPH03179041A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03179041A (en) | 1991-08-05 |
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