JPH02173131A - Production of formed phenolic resin - Google Patents

Production of formed phenolic resin

Info

Publication number
JPH02173131A
JPH02173131A JP32778588A JP32778588A JPH02173131A JP H02173131 A JPH02173131 A JP H02173131A JP 32778588 A JP32778588 A JP 32778588A JP 32778588 A JP32778588 A JP 32778588A JP H02173131 A JPH02173131 A JP H02173131A
Authority
JP
Japan
Prior art keywords
phenolic resin
foaming
foam
resin
drying
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
JP32778588A
Other languages
Japanese (ja)
Inventor
Tatsuhiro Kou
達寛 溝
Hitoshi Hatta
八田 均
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.)
Resonac Holdings Corp
Original Assignee
Showa Highpolymer 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 Showa Highpolymer Co Ltd filed Critical Showa Highpolymer Co Ltd
Priority to JP32778588A priority Critical patent/JPH02173131A/en
Publication of JPH02173131A publication Critical patent/JPH02173131A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To produce a foamed phenolic resin containing uniformly dispersed fibers and having high strength by dissolving a novolak phenolic resin in a solvent, impregnating the solution in a nonwoven fiber sheet and foaming the product after drying. CONSTITUTION:The objective foamed phenolic resin is produced by dissolving (A) a novolak phenolic resin produced by reacting phenols with formaldehyde in the presence of an acid catalyst in (B) a volatile polar organic solvent having a boiling point of <=120 deg.C and capable of dissolving the component A (e.g. methanol, acetone or acetonitrile), adding (C) a curing agent (e.g. hexamethylenetetramine) to the solution, adding and uniformly mixing (B) a foaming agent (preferably a decomposition-type organic foaming agent) and (E) a foam stabilizer (preferably a silicone compound), impregnating the obtained solution in a nonwoven fiber sheet (e.g. glass mat), drying at normal temperature in air for about 48hr and foaming the product.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、断熱材、緩衝材、パネル、ボードなどの用途
に有用なフェノール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 phenolic resin foams useful for applications such as heat insulating materials, cushioning materials, panels, boards, and the like.

さらに詳しくは、本発明はノボラック型フェノール樹脂
を溶剤に溶解または、均一に混合させ、その溶液をシー
ト状の不織繊維基材に含浸発泡させるため、発泡時に繊
維が内圧によりほどけ、このため繊維が発泡体内に均一
に分散することを特徴とする高強度のフェノール樹脂発
泡体の製造方法に関する。
More specifically, in the present invention, a novolac type phenolic resin is dissolved in a solvent or mixed uniformly, and the solution is impregnated into a sheet-like nonwoven fiber base material and foamed. The present invention relates to a method for producing a high-strength phenolic resin foam, which is characterized in that phenolic resin is uniformly dispersed within the foam.

(従来の技術) 従来、フェノール樹脂発泡体の機械的強度を向上させる
ために、発泡体中に各種の補強用繊維材を混在させるこ
とが考えられており、その1番目は寸断されたガラス繊
維と、フェノール樹脂初期給金物を含む発泡性樹脂組成
物粉末(フェノール樹脂発泡体の原料)とを混和して型
内で発泡、硬化させる方法、その2番目は粉末状の発泡
性樹脂組成物を多数積層される綿状シート材間に散布さ
せた後これらを熱ロールや熱プレス等で該当樹脂組成物
ごとにフェノール樹脂初期給金物が溶融しうる温度で予
備成形して各綿状シート内部に樹脂組成物を含浸保持さ
せこの多層体を加熱して発泡硬化させる方法(特公昭4
7−8945号公報)、その3番1は粉末状の発泡性樹
脂組成物溶液を含浸させた2枚もしくは、多数積層され
る綿状シー]・間に散布させた後に、これらを低温加熱
して各綿状シート内部に樹脂組成物を含浸保持させこの
多層体を加熱し発泡硬化させる方法(特開昭61−23
3526号公報)が知られている。
(Prior Art) Conventionally, in order to improve the mechanical strength of phenolic resin foam, it has been considered to mix various reinforcing fiber materials into the foam, and the first one is shredded glass fiber. and a foamable resin composition powder (raw material for phenolic resin foam) containing an initial charge of phenolic resin, which is then foamed and cured in a mold. After scattering between a large number of laminated cotton-like sheet materials, these are preformed using hot rolls, hot presses, etc. at a temperature that allows the initial charge of phenolic resin to melt for each corresponding resin composition, and the inside of each cotton-like sheet is preformed. A method of impregnating and retaining a resin composition and heating and foaming the multilayer body to harden it (Special Publications Publication No. 4
No. 7-8945), No. 3, No. 1 is a cotton-like sheet impregnated with a powdered foamable resin composition solution, which is made of two sheets or laminated in large numbers. A method of impregnating and retaining a resin composition inside each cotton-like sheet and heating and foaming and curing this multilayer body (Japanese Patent Laid-Open No. 61-23
3526) is known.

(発明が解決しようとする課題) しかしながら、1番目の方法では、繊維と樹脂組成物を
均一に混和することが困難でフェノール樹脂発泡層と繊
維とが均一に混在した発泡成形体を得ることがむつかし
かった。第二の方法では、発泡硬化がおこらず樹脂が溶
融するできるだけ低い温度でシートに含浸させるものの
この温度の幅が狭いために部分的に発泡硬化が起こりや
すく、また、シートと樹脂の密着性も悪いなどの問題点
もある、第三の方法でも上記点は改良されているが、な
お、粉状の樹脂組成物を使用しているために整泡剤が混
合しにくく発泡状態が悪い、可塑剤等の添加剤を加えに
くい等の問題点があった。
(Problems to be Solved by the Invention) However, in the first method, it is difficult to mix the fibers and the resin composition uniformly, and it is difficult to obtain a foam molded product in which the phenol resin foam layer and the fibers are uniformly mixed. It was difficult. In the second method, the sheet is impregnated at the lowest possible temperature at which the resin melts without causing foaming hardening, but because this temperature range is narrow, foaming hardening tends to occur locally, and the adhesion between the sheet and the resin is poor. The third method also improves the above points, but since it uses a powdered resin composition, it is difficult to mix the foam stabilizer, resulting in poor foaming state and poor plasticity. There were problems such as difficulty in adding additives such as agents.

この発明は、かかる問題点に鑑みなされたもので、繊維
とフェノール樹脂発泡体層とが均一に混在した複合成形
体を簡便に製造し、添加剤等で改質しやすくする方法を
提供するものである。
This invention was made in view of the above problems, and provides a method for easily producing a composite molded article in which fibers and a phenolic resin foam layer are evenly mixed, and for easily modifying it with additives, etc. It is.

(課題を解決するための手段) 本発明者は、シート状の不*i#!維基材に溶剤に溶か
した樹脂を含浸させ、低温で長時間乾燥させることによ
りほぼ完全に溶剤を除去することで。
(Means for Solving the Problems) The present inventor has developed a sheet-like non*i#! The fiber base material is impregnated with a resin dissolved in a solvent, and the solvent is almost completely removed by drying at low temperatures for a long time.

溶剤の発泡体への影響を極力抑えうろことを見いだし、
さらに発泡時に基材の繊維が分散し、発泡体内に均一に
混在されることを見いだしこの発明に到達した。
We found a scale that minimizes the effect of solvent on foam,
Furthermore, it was discovered that the fibers of the base material are dispersed during foaming and are uniformly mixed within the foam, and this invention has been achieved.

すなわち本発明はノボラック及びノボラyりが可溶な溶
剤、発泡剤、硬化剤、整泡剤を含む混合液を、シート状
の不織繊維基材に含浸した後、発泡させることを特徴と
するフェノール樹脂発泡体の製造方法であり、又ノボラ
ックが可溶な溶剤として沸点120℃以下の気化性の極
性有機溶剤を使用するものである。
That is, the present invention is characterized in that a sheet-like nonwoven fiber base material is impregnated with a liquid mixture containing a solvent in which novolak and novolak are soluble, a foaming agent, a hardening agent, and a foam stabilizer, and then foamed. This is a method for producing a phenolic resin foam, and a volatile polar organic solvent with a boiling point of 120° C. or less is used as a solvent in which novolak is soluble.

(作用) 本発明に使用されるフェノール樹脂は、ノボラック型フ
ェノール樹脂であり常法による、フェノール類とホルム
アルデヒドとを、酸触媒により反応させたもので以後に
記す溶剤に対して可溶または、乳化により均一に混合さ
れるものであればよいため、殆どすべてのノボラック樹
脂が使用可能である。
(Function) The phenol resin used in the present invention is a novolac type phenol resin, which is produced by reacting phenols and formaldehyde using an acid catalyst using a conventional method, and is soluble or emulsifiable in the solvents described below. Almost all novolac resins can be used as long as they can be mixed uniformly.

フェノール類はこのためフェノールのほか、クレゾール
類、キシレノール類、オクチルフェノール類等のアルキ
ルフェノール類、ビスフェノールA、フェニルフェノー
ル、スチレン化フェノール等のアルキルフェノール類似
構造を有するフェノール類、P−ビニルフェノール、イ
ソプロピルフェノール類等のアルケニルフェノール類等
を単独または、2種以上を併用したものを用いてもよく
、アルデヒドとしては、ホルムアルデヒド、パラホルム
アルデヒド、アセl−アルデヒド、フルフラールなど使
用できる。触媒としては、酸性触媒で、通常の反応を行
なってノボラック型フェノール樹脂を作成する。
Therefore, in addition to phenol, phenols include alkylphenols such as cresols, xylenols, and octylphenols, phenols with a structure similar to alkylphenols such as bisphenol A, phenylphenol, and styrenated phenol, P-vinylphenol, isopropylphenol, etc. Alkenylphenols and the like may be used alone or in combination of two or more, and as the aldehyde, formaldehyde, paraformaldehyde, acel-aldehyde, furfural, etc. can be used. A novolac type phenol resin is produced by carrying out a normal reaction using an acidic catalyst as a catalyst.

溶剤は上記のフェノール樹脂を溶解させ且つ不活性のも
のであり、さらには、常温で気化し易い、沸点120℃
以下で、極性有機溶剤を用いる。このような溶剤として
は、メタノール、エタノールのような低級アルコール類
、アセトン等のケトン類、アセトニトリル等のニトリル
類、エーテル類、エステル類、アミン類、及び極性基を
有する芳香族化合物が使用可能である。無視性な炭化水
素、多くの芳香族化合物は、フェノール樹脂を溶解せず
、また、カルボン酸類は発泡剤が分解し易く、使用でき
ない。
The solvent is one that dissolves the above-mentioned phenolic resin and is inert, and furthermore, it has a boiling point of 120°C, which easily vaporizes at room temperature.
Below, a polar organic solvent is used. As such solvents, lower alcohols such as methanol and ethanol, ketones such as acetone, nitriles such as acetonitrile, ethers, esters, amines, and aromatic compounds having polar groups can be used. be. Negligible hydrocarbons and many aromatic compounds do not dissolve phenolic resins, and carboxylic acids cannot be used because blowing agents tend to decompose.

発泡剤としては、 N 、 N ’−ジニトロソペンタ
メチレンテトラミン、ベンゼンスルホニルヒドラジド、
アゾビスイソブチロニトリル、等の有機分解型発泡剤、
重炭酸ナトリウム、亜硝酸アンモニウムなどの無機分解
型発泡剤が用いられるが、溶剤との混合性の点で、有機
分解型発泡剤が望ましい。
As blowing agents, N,N'-dinitrosopentamethylenetetramine, benzenesulfonyl hydrazide,
Organic decomposition type blowing agents such as azobisisobutyronitrile,
Inorganic decomposition type blowing agents such as sodium bicarbonate and ammonium nitrite are used, but organic decomposition type blowing agents are preferred from the viewpoint of miscibility with solvents.

硬化剤としては、一般的なヘキサメチレンテトラミンが
用いられる。整泡剤としては、一般的なシリコン系、金
属石鹸系、高分子系が用いられるが、好ましくは、高温
に強いシリコン系がよい。他に変性剤として、ゴム類、
ポリビニルアルコール類、ポリアミド等を加えることが
可能である。
As a curing agent, common hexamethylenetetramine is used. As the foam stabilizer, common silicone-based, metal soap-based, and polymer-based foam stabilizers are used, but silicone-based foam stabilizers that are resistant to high temperatures are preferred. Other modifiers include rubbers,
It is possible to add polyvinyl alcohols, polyamides, etc.

発泡体の製造方法としては、まず、溶剤にノボラックを
溶解させ、硬化剤、発泡剤、整泡剤、その他添加物を加
え均一に混合させる。このとき、発泡剤、整泡剤は、最
後に入れると混合し易い。
As a method for producing a foam, first, novolak is dissolved in a solvent, and a curing agent, a foaming agent, a foam stabilizer, and other additives are added and mixed uniformly. At this time, it is easier to mix the foaming agent and foam stabilizer if they are added last.

ノボラック樹脂の濃度は任意で構わないが、作業性の点
でノボラック溶液の粘度が100〜10QQOcpsに
なるようにすることが望ましい。この粘度では溶剤に難
溶性の物質も均一に混合され、また基材への含浸も容易
となる。
The concentration of the novolak resin may be arbitrary, but from the viewpoint of workability, it is desirable that the viscosity of the novolac solution be 100 to 10 QQOcps. At this viscosity, even substances that are poorly soluble in the solvent can be mixed uniformly, and it is also easy to impregnate the base material.

発泡剤量については、発泡倍率、発泡剤の基材への付着
密度により適量添加する。発泡剤の量が少ないと十分な
発泡が行われず発泡体の形状、物性に悪影響を及ぼし、
逆に発泡剤量が多いと発泡時に型枠内の圧力が高くなり
すぎ型枠からの吹き出し等が起こり危険である。通常は
発泡倍率が2〜10倍の時に、発泡剤量が5〜50 g
/ mとなるように加える。硬化剤、整泡剤もそれぞれ
適宜加えるが、その量は、ノボラック100部に対し硬
化剤で3〜20部、整泡剤で1〜10部が好ましい。
The appropriate amount of blowing agent is added depending on the expansion ratio and the adhesion density of the blowing agent to the base material. If the amount of foaming agent is small, sufficient foaming will not occur and the shape and physical properties of the foam will be adversely affected.
On the other hand, if the amount of foaming agent is too large, the pressure inside the mold becomes too high during foaming, which may cause blowing out of the mold, which is dangerous. Usually, when the foaming ratio is 2 to 10 times, the amount of blowing agent is 5 to 50 g.
/ m. A curing agent and a foam stabilizer are also added as appropriate, and the amounts thereof are preferably 3 to 20 parts for the curing agent and 1 to 10 parts for the foam stabilizer per 100 parts of the novolak.

この混合溶液を、シート状の不織繊維基材に含浸させる
が、通常の含浸、塗布等の方法でよいが基材の中まで樹
脂を含浸させる必要がある。このときの混合液と基材の
割合は、ノボラック樹脂:基材=2:8〜9:1となる
ようにすることが望ましい。
This mixed solution is impregnated into a sheet-like nonwoven fiber base material, and conventional methods such as impregnation and coating may be used, but it is necessary to impregnate the resin into the base material. At this time, the ratio of the mixed liquid and the base material is desirably such that the novolak resin:base material=2:8 to 9:1.

乾燥は、常温風乾で48時間程度がよい、熱をかけた乾
燥もできるが熱をかけると発泡剤の分解が起こり好まし
くない。風乾は、日陰で風通しのよいところで、含浸子
Wt繊維基材を吊すか、離型紙上で乾かすときれいなシ
ートができる。熱をかける場合は、40−70℃で1−
2時間乾燥させる。
For drying, it is best to air dry at room temperature for about 48 hours; drying by applying heat is also possible, but applying heat causes decomposition of the foaming agent, which is not preferable. For air drying, hang the impregnator Wt fiber base material in a shaded and well-ventilated place or dry it on release paper to form a clean sheet. When applying heat, heat at 40-70℃.
Let dry for 2 hours.

本発明で使用される不織繊維基材は、ガラス繊維、金属
繊維、炭素繊維等の無機不織繊維、木綿、再生繊維、合
成繊維等の有機不織繊維をシート状に形成させた不織布
が用いられ、ガラスマットがその代表例である。その厚
み、秤量は任意で可能である。
The nonwoven fiber base material used in the present invention is a nonwoven fabric formed into a sheet of inorganic nonwoven fibers such as glass fiber, metal fiber, and carbon fiber, and organic nonwoven fibers such as cotton, recycled fiber, and synthetic fiber. A typical example is glass mat. The thickness and weight can be set arbitrarily.

このシート状基材の発泡は、金型に適当な大きさにきっ
た基材を装填し加熱することにより行なわれる。基材は
、1枚から何枚でも使用可能であるが、加熱装置により
多層にしたときの厚みに制限を受ける場合がある。加熱
方法は、一般に知られている方法でよく、加熱プレス、
赤外線、乾燥器等なんでも用いられる。ただしプレス等
の金型の表面より加熱するものでは厚み30mm以上の
成形品は作りにくい。加熱温度は、120−180℃が
最適であり数分から数十分で発泡硬化が行なわれる。
Foaming of this sheet-like base material is carried out by loading the base material cut into an appropriate size into a mold and heating it. Although it is possible to use one or more base materials, the thickness of the base material may be limited by the heating device when the base material is made into multiple layers. The heating method may be a generally known method such as a heating press,
Anything can be used, such as infrared rays and a dryer. However, it is difficult to make molded products with a thickness of 30 mm or more using a press that heats the surface of the mold. The optimal heating temperature is 120-180°C, and foaming and curing is performed in several minutes to several tens of minutes.

本発明方法においては、液状物質に樹脂を溶解するため
に添加剤の混合が容易となり、整泡剤、可塑剤を加え易
く、より有用な発泡体が得られるようになる。また不織
繊維基材に樹脂を含浸させているために発泡時に、発泡
圧のために不織繊維基材のバインダーがはがれ繊維が発
泡体の中に均一に分散される特徴を持っており、このた
めに高強度となる。
In the method of the present invention, since the resin is dissolved in the liquid substance, additives can be easily mixed, and foam stabilizers and plasticizers can be easily added, making it possible to obtain more useful foams. In addition, since the non-woven fiber base material is impregnated with resin, the binder of the non-woven fiber base material is peeled off due to the foaming pressure during foaming, and the fibers are uniformly dispersed within the foam. This results in high strength.

(実施例) 実施例1 フェノールと、ホルムアルデヒドを酸触媒により常法に
したがって作成したノボラック樹脂の50重量%メタノ
ール溶液100重量部に対し硬化剤として、ヘキサメチ
レンテトラミン5重量部、発泡剤として、N、N’−ジ
ニトロソペンタメチレンジアミン(セルマイクA:三協
化成(株)製)5重量部、整泡剤としてシリコンオイル
(L−7002二日本ユニカ(株)製)2重量部をミキ
サーで撹拌しこの混合液を、25CIIIX25dll
のガラスマット(MC450A:日東紡(株)1!II
)  にとぶ漬は含浸させ、かるくしぼり陰干しで風乾
した。乾燥後の含浸量は、ノボラック樹脂:マット=1
=1であり、厚みは、1.511nであった。このシー
ト1−3枚を25国×25■x0.6−2Gの金型にい
れ、150℃10分加熱し発泡させると金型と同型のガ
ラス繊維入り発泡体を得た。この発泡体中のガラス繊維
はほぼ均一に分散していた。強度等は、第1表に記載の
通りである。
(Example) Example 1 5 parts by weight of hexamethylenetetramine as a curing agent and 5 parts by weight of hexamethylenetetramine as a blowing agent were added to 100 parts by weight of a 50% by weight methanol solution of novolac resin prepared in a conventional manner using phenol and formaldehyde as an acid catalyst. , 5 parts by weight of N'-dinitrosopentamethylene diamine (Celmic A, manufactured by Sankyo Kasei Co., Ltd.), and 2 parts by weight of silicone oil (L-7002 manufactured by Nippon Unica Co., Ltd.) as a foam stabilizer were stirred with a mixer. 25CIIIX25dll of Shiko mixed liquid
Glass mat (MC450A: Nittobo Co., Ltd. 1!II
) Nitobuzuke was impregnated, lightly squeezed and air-dried in the shade. The amount of impregnation after drying is Novolac resin: Matte = 1
=1, and the thickness was 1.511n. One to three of these sheets were placed in a mold of 25 mm x 25 mm x 0.6-2 G and heated at 150° C. for 10 minutes to foam, thereby obtaining a glass fiber-containing foam having the same shape as the mold. The glass fibers in this foam were almost uniformly dispersed. Strength etc. are as described in Table 1.

実施例2 実施例1と同様にして作成した混合液を25anX25
anのナイロン不織布にローラー含浸させ陰干しで風乾
した。乾燥後の樹脂量は、ノボラック樹脂:不織布=6
:4であり、厚みは1膿であった。このシート、3枚を
25 an X 25■×2■の金型にいれ、これを1
50℃10分加熱、発泡させると金型と同型の発泡体が
成形した。
Example 2 A mixed solution prepared in the same manner as in Example 1 was mixed with 25anX25
A nylon nonwoven fabric of AN was impregnated with a roller and air-dried in the shade. The amount of resin after drying is: Novolac resin: Nonwoven fabric = 6
: 4, and the thickness was 1 pus. Put 3 of these sheets into a mold of 25 an x 25 x 2 x 1
When heated and foamed at 50° C. for 10 minutes, a foam having the same shape as the mold was formed.

実施例3 ノボラック樹脂の70Lllt%メタノール溶液100
重量部に実施例1で用いた硬化剤8重量部、発泡剤6重
量部、整泡剤3重量部、およびポリビニルアルコール(
PVA 202 、クラレ■製)5重量部を混合し、ア
ルミ繊維不織布(25anX25(2))にハンドレイ
アップ法により含浸させた。風乾後の樹脂量は、ノボラ
ック樹脂:不織布=2:1であった。
Example 3 70Lllt% methanol solution of novolak resin 100
The weight parts include 8 parts by weight of the curing agent used in Example 1, 6 parts by weight of the foaming agent, 3 parts by weight of the foam stabilizer, and polyvinyl alcohol (
5 parts by weight of PVA 202 (manufactured by Kuraray ■) were mixed and impregnated into an aluminum fiber nonwoven fabric (25anX25(2)) by a hand lay-up method. The amount of resin after air drying was novolac resin:nonwoven fabric=2:1.

これを25 aIIX 25 an X 1 cn の
金型にいれ120℃12分発泡硬化させたところ金型と
同型に発泡体を得た。
This was placed in a mold of 25 aIIX 25 an

比較例1 実施例1で用いたノボラック樹脂100重量部に対し、
同様に実施例1で用いた発泡剤10重地部、硬化剤10
重量部を加え加熱ロールにより混練し、その後粉砕し粉
末の樹脂組成物を得た。この粉末30gを実施例1で用
いたマット上にまき上からマットをもう一枚重ね二枚重
ねとし25cm×250Xlanの金型にいれ150’
CIO分発泡硬化させ発泡体を得た。しかしこの発泡体
は、樹脂組成物の装填時に粉が移動し取り扱いにくく、
さらに発泡体自体もフェノール発泡層の充填していない
空洞があり不均一なものであった。
Comparative Example 1 For 100 parts by weight of the novolak resin used in Example 1,
Similarly, the foaming agent used in Example 1 was 10% heavy base, and the hardening agent 10%
Parts by weight were added, kneaded using heated rolls, and then pulverized to obtain a powdered resin composition. 30g of this powder was sprinkled on the mat used in Example 1, and then another layer of mat was placed on top of the mat, and the two layers were put into a 25cm x 250Xlan mold with a size of 150'.
A foam was obtained by foaming and curing for CIO. However, this foam is difficult to handle because the powder moves when the resin composition is loaded.
Furthermore, the foam itself was non-uniform as it had cavities that were not filled with the phenol foam layer.

比較例2 比較例1と同じノボラック樹脂100重量部に対し、発
泡剤10重量部、硬化剤10重量部を加え、加熱ロール
にて混練した。その後粉砕して粉末の樹脂組成物を得た
Comparative Example 2 To 100 parts by weight of the same novolac resin as in Comparative Example 1, 10 parts by weight of a foaming agent and 10 parts by weight of a curing agent were added, and the mixture was kneaded with a heated roll. Thereafter, it was pulverized to obtain a powdered resin composition.

次いで結合剤として、メチルアルコール(試薬特級)と
、トリクロロトリフルオロエタンを容量比で1:5に混
合したものを用い、ノズルにより霧状に、実施例1で使
用したマントに5g噴霧した。
Next, as a binder, a mixture of methyl alcohol (special grade reagent) and trichlorotrifluoroethane in a volume ratio of 1:5 was used, and 5 g of the mixture was sprayed onto the cloak used in Example 1 in the form of a mist using a nozzle.

この結合剤を吸収したマットの上に発泡性樹脂組成物3
0gを散布しさらにその上に同様に結合剤を吸収させた
マットを置き約1kgの圧力で予備成形し次いで60℃
の温風循環高温槽で100分間乾燥した。次いでこのシ
ートを25cmX 25cmX1cmの金型にいれ15
0℃10分加熱、発泡させると発泡体ができた。この発
泡体は、発泡状態が悪く、表面のガラス層に樹脂が付い
ておらず表面が凸凹したものであった。
The foamable resin composition 3 is placed on the mat that has absorbed this binder.
0g was sprinkled on top of the mat, which had been similarly absorbed with the binder, and preformed under a pressure of about 1kg, and then heated at 60°C.
It was dried for 100 minutes in a hot air circulating high temperature bath. Next, put this sheet into a 25cm x 25cm x 1cm mold15
A foam was formed by heating and foaming at 0°C for 10 minutes. This foam had a poor foaming condition, no resin was attached to the glass layer on the surface, and the surface was uneven.

第1表は、実施例1〜3で作成した発泡体の物性を示し
たものである。
Table 1 shows the physical properties of the foams produced in Examples 1 to 3.

(発明の効果) この発明によれば、繊維とフェノール樹脂が均一に混在
する複合体が効率よく安定して得ることができる。そし
てこのシート状発泡性複合体は、製造時に熱を使わない
ため簡便に製造され、様々な添加物を混合することが可
能であり複合体の用途に合わせ様々な組合せが使えるよ
うになる。
(Effects of the Invention) According to the present invention, a composite in which fibers and phenol resin are uniformly mixed can be efficiently and stably obtained. Since this sheet-like foamable composite does not use heat during production, it is easily manufactured, and various additives can be mixed in, allowing various combinations to be used depending on the use of the composite.

Claims (2)

【特許請求の範囲】[Claims] (1)ノボラック及びノボラックが可溶な溶剤、発泡剤
、硬化剤、整泡剤を含む混合液を、シート状の不織繊維
基材に含浸し乾燥した後発泡させることを特徴とするフ
ェノール樹脂発泡体の製造方法。
(1) A phenolic resin characterized by impregnating a sheet-shaped nonwoven fiber base material with a liquid mixture containing novolak and a novolac-soluble solvent, a foaming agent, a hardening agent, and a foam stabilizer, drying it, and then foaming it. Method of manufacturing foam.
(2)ノボラックが可溶な溶剤として沸点120℃以下
の気化性の極性有機溶剤を使用することを特徴とする特
許請求の範囲第1項記載のフェノール樹脂発泡体の製造
方法。
(2) The method for producing a phenolic resin foam according to claim 1, characterized in that a volatile polar organic solvent with a boiling point of 120° C. or less is used as the novolac-soluble solvent.
JP32778588A 1988-12-27 1988-12-27 Production of formed phenolic resin Pending JPH02173131A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32778588A JPH02173131A (en) 1988-12-27 1988-12-27 Production of formed phenolic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32778588A JPH02173131A (en) 1988-12-27 1988-12-27 Production of formed phenolic resin

Publications (1)

Publication Number Publication Date
JPH02173131A true JPH02173131A (en) 1990-07-04

Family

ID=18202958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32778588A Pending JPH02173131A (en) 1988-12-27 1988-12-27 Production of formed phenolic resin

Country Status (1)

Country Link
JP (1) JPH02173131A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0565358A (en) * 1991-07-11 1993-03-19 Dainippon Ink & Chem Inc Prepreg

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0565358A (en) * 1991-07-11 1993-03-19 Dainippon Ink & Chem Inc Prepreg

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