JPH02284932A - Production of foamed phenolic resin - Google Patents

Production of foamed phenolic resin

Info

Publication number
JPH02284932A
JPH02284932A JP10897689A JP10897689A JPH02284932A JP H02284932 A JPH02284932 A JP H02284932A JP 10897689 A JP10897689 A JP 10897689A JP 10897689 A JP10897689 A JP 10897689A JP H02284932 A JPH02284932 A JP H02284932A
Authority
JP
Japan
Prior art keywords
phenolic resin
foam
resol
solvent
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.)
Granted
Application number
JP10897689A
Other languages
Japanese (ja)
Other versions
JPH0575779B2 (en
Inventor
Tatsuhiro Mizo
達寛 溝
Hitoshi Hatta
八田 均
Katsutoshi Yoshinaga
勝利 吉永
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 JP10897689A priority Critical patent/JPH02284932A/en
Publication of JPH02284932A publication Critical patent/JPH02284932A/en
Publication of JPH0575779B2 publication Critical patent/JPH0575779B2/ja
Granted legal-status Critical Current

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

Abstract

PURPOSE:To obtain the subject foamed material useful as a heat-insulation material, cushioning material, panel, board, etc., by impregnating a liquid mixture containing a mixed phenolic resin consisting of novolak and resol, a solvent, a foaming agent and a foam stabilizer into a nonwoven fiber sheet substrate, drying the liquid and foaming the composition. CONSTITUTION:A liquid mixture containing (A) a mixed phenolic resin consisting of novolak and resol, (B) a solvent of said resin (preferably a volatile polar organic solvent having a boiling point of <=120 deg.C, e.g. methanol or acetone), (C) a foaming agent (e.g. N,N'-dinitrosopentamethylenetetramine) and (D) a foam stabilizer (preferably silicone compound) is impregnated in a nonwoven fiber sheet substrate, dried and foamed to obtain the objective foamed product. The mixing ratio of novolak:resol is preferably 90:10 to 70:80 by weight.

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 Field of Application] 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とレゾールからな
る混合フェノール樹脂を発泡剤、硬化剤、整泡剤などと
共に溶剤に溶解または、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し乾燥した後発泡させるこ
とにより、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, the present invention involves dissolving or uniformly mixing a mixed phenolic resin consisting of novolac and resol in a solvent together with a blowing agent, hardening agent, foam stabilizer, etc., and impregnating a sheet-shaped nonwoven fiber base material with the solution. The present invention relates to a method for producing a high-strength phenolic resin foam, which is characterized in that by foaming after drying, the fibers are unraveled by internal pressure during foaming, so that the fibers are uniformly dispersed within the foam.

〔従来の技術〕[Conventional technology]

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縮合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縮合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番目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
る綿状シート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61−213
528号公報)が知られている。
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. The second method is to mix a foamable resin composition powder containing a condensate (raw material for phenolic resin foam) and foam and harden it in a mold. After being spread between the flocculent sheet materials, these are preformed using hot rolls, hot presses, etc. at a temperature that allows the initial condensate of the phenolic resin to melt for each resin composition, and the inside of each flocculent sheet is impregnated with the resin composition. A method of holding and heating this multilayer body to foam and harden it (Special Publications Publication No. 4
No. 7-8945), and the third method is to spread the powdered foamable resin composition solution between two or multiple laminated cotton-like sheets and then heat them at a low temperature to form individual cotton sheets. A method of impregnating and retaining a resin composition inside a shaped sheet and heating and foaming and curing this multilayer body (Japanese Patent Laid-Open No. 61-213
No. 528) is known.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら、第一の方法では、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、発泡硬化が起こらず樹脂が溶融
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。
However, in the first method, it was difficult to mix the fibers and the resin composition uniformly, and it was difficult to obtain a foam molded article in which the phenol resin foam layer and the fibers were uniformly mixed. In the second method, the sheet is impregnated at the lowest possible temperature at which the resin melts without 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. There are also problems such as bad things. 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 conditions, and it is difficult to add additives such as plasticizers. There were problems such as.

本発明者の一部は、かかる問題点に鑑み、先に、シート
状の不織繊維基材に溶剤に溶かしたノボラック型フェノ
ール樹脂を含浸させ、乾燥した後発泡させることによっ
て、繊維とフェノール樹脂発泡体層とが均一に混在した
発泡複合体を簡便に製造できることを見い出し、既に提
案した。
In view of this problem, some of the inventors of the present invention first impregnated a sheet-shaped nonwoven fiber base material with a novolac type phenolic resin dissolved in a solvent, dried it, and then foamed it, thereby combining the fibers with the phenolic resin. It has been discovered that a foamed composite body in which foam layers are uniformly mixed can be easily manufactured, and the invention has already been proposed.

しかしながら、この方法ではノボラックの硬化剤として
使用されるヘキサメチレンテトラミンからのアンモニア
臭発生が避けられないという不都合があった 〔課題を解決するための手段〕 本発明者らは、さらに検討した結果、ノボラックにレゾ
ールを混合したフェノール樹脂を溶剤に溶かした混合液
を、シート状の不織繊維基材に含浸させ、乾燥させ、発
泡させることによって、前記具の問題が解決されると共
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出し、本発明に到達した。
However, this method had the inconvenience of unavoidably generating ammonia odor from hexamethylenetetramine used as a curing agent for novolac. [Means for Solving the Problem] As a result of further study, the present inventors found that By impregnating a sheet-shaped nonwoven fiber base material with a mixture of phenolic resin, which is a mixture of novolac and resol, dissolved in a solvent, the problem of the above-mentioned tool is solved, and the base material is removed during foaming. The present invention was achieved by discovering that the fibers of the material are dispersed and mixed uniformly within the foam.

すなわち、本発明はノボラック及びレゾールからなる混
合フェノール樹脂、該樹脂が可溶な溶剤、発泡剤、並び
に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 impregnates a sheet-shaped nonwoven fiber base material with a mixed liquid containing a mixed phenolic resin consisting of novolac and resol, a solvent in which the resin is soluble, a foaming agent, and a foam stabilizer, and then drying the mixture. This is a method for producing a phenolic resin foam characterized by foaming, and a vaporizable polar organic solvent with a boiling point of 120° C. or lower is used as a solvent in which novolak is soluble.

本発明に使用されるフェノール樹脂は、ノボラック型及
びレゾール型のフェノール樹脂であり、常法に従って、
フェノール類とホルムアルデヒドとを、酸性触媒または
塩基性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型樹脂またはレ
ゾール型樹脂が使用可能である。しかしながら、レゾー
ルについては、ノボラックとの混合性の点から固形もし
くは溶剤溶解型のものが好適である。
The phenolic resin used in the present invention is a novolak type and resol type phenolic resin, and according to a conventional method,
Almost all novolac-type resins can be used as long as they are made by reacting phenols and formaldehyde with an acidic or basic catalyst and are soluble in the solvents mentioned below or can be mixed uniformly by emulsification. Alternatively, resol type resin can be used. However, from the viewpoint of miscibility with novolak, solid or solvent-soluble resols are preferred.

本発明で使用可能なフェノール類としてはフェノールの
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A1
フエニルフエノール、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、アセトアルデヒド、フル
フラール等が使用できる。
In addition to phenol, the phenols that can be used in the present invention include alkylphenols such as cresols, xylenols, and octylphenols, and bisphenol A1.
Phenylphenols, phenols with alkylphenol-like structures such as styrenated phenols, alkenylphenols such as p-vinylphenol and isopropylphenols, etc. may be used alone or in combination of two or more, and as aldehydes. Formaldehyde, paraformaldehyde, acetaldehyde, furfural, etc. can be used.

ノボラック製造の触媒としては酸性触媒で、レゾール製
造の触媒としては塩基性触媒で、通常の反応を行なって
ノボラック型またはレゾール型のフェノール樹脂が製造
される。
An acidic catalyst is used as a catalyst for novolac production, and a basic catalyst is used as a catalyst for resol production, and a normal reaction is carried out to produce a novolak type or resol type phenol resin.

ノボラックとレゾールとの混合比率は特に制限されない
が、発泡体の強度の面からノボラック:レゾール−90
:10〜70:30(重量比)の割合が好ましい。
The mixing ratio of novolak and resol is not particularly limited, but from the viewpoint of the strength of the foam, novolak:resol-90 is used.
:10 to 70:30 (weight ratio) is preferable.

溶剤は上記の混合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12
0℃以下で、極性有機溶剤を用いる。
The solvent is one that dissolves the above mixed phenolic resin and is inert, and has a boiling point of 12, which easily vaporizes at room temperature.
A polar organic solvent is used at 0°C or lower.

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。無極性な炭化水素、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、レゾールを硬化させるので、使用できない
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. Nonpolar hydrocarbons and many aromatic compounds cannot be used because they do not dissolve phenolic resins, and carboxylic acids tend to decompose blowing agents and harden the resol.

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 the blowing agent, organic decomposition type blowing agents such as N,N'-dinitrosopentamethylenetetramine, benzenesulfonyl hydrazide, azobisisobutyronitrile, etc., and inorganic decomposition type blowing agents such as sodium bicarbonate and ammonium nitrite are used. However, organic decomposition type blowing agents are preferable from the viewpoint of miscibility with solvents.

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 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. In addition, rubbers, polyvinyl alcohols, polyamides, etc. can be added as modifiers.

本発明においては、レゾールがノボラックの硬化剤とし
て作用するので、通常の硬化剤を使用する必要はない。
In the present invention, there is no need to use conventional curing agents since the resol acts as a curing agent for the novolak.

しかし、高強度の発泡体の製造が要求される場合は、ヘ
キサメチレンテトラミン、バラホルムアルデヒドなどが
使用可能であるが、臭の点からみて好ましいとは云えな
い。
However, when production of a high-strength foam is required, hexamethylenetetramine, paraformaldehyde, etc. can be used, but these are not preferred from the viewpoint of odor.

発泡体の製造方法としては、まず、溶剤に混合フェノー
ル樹脂を溶解させ、発泡剤、整泡剤、その地温加物を加
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品い。
As a method for producing a foam, first, a mixed phenolic resin is dissolved in a solvent, and a foaming agent, a foam stabilizer, and their geothermal additives are added and mixed uniformly. At this time, if you add the foaming agent and foam stabilizer last, they will mix well.

混合フェノール樹脂の濃度は20%(歪量%、以下同じ
)以上がよいが、作業性の点で溶液の粘度が100−1
0000cpsになるようにすることが望ましい。
The concentration of the mixed phenolic resin is preferably 20% (% strain, the same applies hereinafter) or more, but from the viewpoint of workability, the viscosity of the solution should be 100-1.
It is desirable to set it to 0000 cps.

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。
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
1〜lO%となるように加える。整泡剤も適宜加えるが
、その量は、混合フェノール樹脂100部に対し1〜I
O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. It is usually added in an amount of 1 to 10%. A foam stabilizer is also added as appropriate, but the amount is 1 to 1 per 100 parts of mixed phenolic resin.
Part O is preferred.

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、混合フェノール樹脂バ基材−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, it is desirable that the ratio of the mixed liquid to the base material be 2:8 to 9:1 of the mixed phenol resin base material.

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、含浸不
織繊維基材を吊すか、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。
Drying is preferably done by air drying at room temperature for about 48 hours. Drying by applying heat is also possible, but applying heat causes the blowing agent to decompose, which is not preferable. For air drying, hang the impregnated nonwoven fiber base material in a shaded and well-ventilated place or dry it on release paper to form a clean sheet. When applying heat, 1 to 2 at 40 to 70℃
Let dry for an hour.

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切っ
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801I11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 801I11 or more using a press or other device that heats the surface of the mold. Heating temperature is 120-180
The optimum temperature is ℃, and foaming and curing takes place within several minutes to several tens of minutes.

〔作  用〕[For production]

本発明方法においては、溶剤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、
また不織繊維基材の中まで樹脂が含浸させることができ
るため、発泡時の発泡圧により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、このために発泡複合体は高強度となる。
In the method of the present invention, since the resin is dissolved in the solvent, it is easy to mix additives, and it is easy to add foam stabilizers and plasticizers.
In addition, since the resin can be impregnated into the inside of the non-woven fiber base material, the binder of the non-woven fiber base material is peeled off by the foaming pressure during foaming, and the fibers are uniformly dispersed within the foam. , which gives the foamed composite high strength.

〔実 施 例〕〔Example〕

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重量部に対して、フェノールとホルムア
ルデヒドを塩基触媒で常法により製造した固形レゾール
10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■製)5
重量部、整泡剤としてシリコンオイル(L−7002:
日本ユニカ■製)2重量部をミキサーで撹拌しこの混合
液を、25cmX25csのガラスマット(MC450
A:日東紡■製)にどぶ漬は含浸させ、かるくしぼり陰
干しで風乾した。乾燥後の含浸量は、ガラス:樹脂−5
0:50であり、厚みは、1.5關であった。このシー
ト1〜6枚を25cm X 25G!1 X O,8〜
2 amの金型にいれ、120℃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 1 10 parts by weight of a 50% by weight methanol solution of novolak resin prepared using phenol and formaldehyde using an acid catalyst according to a conventional method, and 10 parts by weight of a solid resol prepared using a base catalyst using phenol and formaldehyde according to a conventional method. As a blowing agent, N,N'-dinitrosopentamethylenediamine (Celmic A: manufactured by Sankyo Kasei) 5
Part by weight, silicone oil (L-7002:
2 parts by weight (manufactured by Nippon Unica ■) were stirred with a mixer, and the mixed liquid was poured into a 25cm x 25cs glass mat (MC450).
A: Nittobo ■) was impregnated with dobu-zuke, lightly squeezed and air-dried in the shade. The amount of impregnation after drying is glass: resin-5
The ratio was 0:50, and the thickness was 1.5 mm. 1 to 6 of these sheets are 25cm x 25G! 1 X O, 8~
The mixture was placed in a 2 am mold and heated at 120° C. for 10 minutes to form 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25cmx25
(至)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、樹脂:不織布−40: G
oであり、厚みは1關であった。このシート、3枚を2
5cm X 25cm X 2(至)の金型にいれ、こ
れを150℃lO分加熱、発泡させると金型と同型の発
泡体が得られた。発泡体中の不織布はほぼ均一に分散し
ていた。
Example 2 A mixed solution prepared in the same manner as in Example 1 was placed in a 25 cm x 25
The nylon nonwoven fabric (to) was impregnated with a roller and air-dried in the shade. The amount of resin after drying is: Resin: Nonwoven Fabric-40: G
o, and the thickness was 1 inch. This sheet, 3 sheets 2
The mixture was placed in a mold of 5 cm x 25 cm x 2 (maximum) and heated at 150°C for 10 min to foam, yielding a foam having the same shape as the mold. The nonwoven fabric in the foam was almost uniformly dispersed.

実施例 3 ノボラック樹脂の70vL%メタノール溶液100重量
部に実施例1で用いたレゾール15ffiffi部、発
泡剤6重量部、整泡剤3重量部、およびポリビニル7.
1/ニア−/I/ (PVA202;クラレ■製> 5
ffi量部を混合し、アルミ繊維不織布(25cm X
 25an )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、樹脂:不織布−20:80であっ
た。
Example 3 15 parts by weight of the resol used in Example 1, 6 parts by weight of a foaming agent, 3 parts by weight of a foam stabilizer, and 7.0 parts by weight of a foam stabilizer were added to 100 parts by weight of a 70 vL% methanol solution of novolac resin.
1/Near/I/ (PVA202; Made by Kuraray ■> 5
ffi amount was mixed and aluminum fiber nonwoven fabric (25cm x
25an) by hand lay-up method. The amount of resin after air drying was resin:nonwoven fabric-20:80.

これを25cm X 25cm X O,5CD+の金
型にいれ180℃12分発泡硬化させたところ金型と同
型に発泡体を得た。発泡体中のアルミ繊維はほぼ均一に
分散していた。
This was placed in a 25cm x 25cm x O, 5CD+ mold and foamed and cured at 180°C for 12 minutes to obtain a foam having the same shape as the mold. The aluminum fibers in the foam were almost uniformly dispersed.

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で用いたレゾール樹脂10重量部、発泡
剤10重量部及び整泡剤2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発泡性樹脂組成物を得た
。この粉末55g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 X 
25CQI X 1 cmの金型にいれ150℃10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, 10 parts by weight of the resol resin used in Example 1, 10 parts by weight of a foaming agent, and 2 parts by weight of a foam stabilizer were added, kneaded using heated rolls, and then crushed to obtain a powdered foamable resin composition. Sprinkle 55 g of this powder on the mat used in Example 1, and cover it with another mat to make a two-layer stack of 25 cm x
The mixture was placed in a 25CQI x 1 cm mold and foamed and cured at 150°C for 10 minutes to obtain a foam. However, this foam was difficult to handle because the powder moved when the resin composition was loaded, and 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と処方のものを加熱ロールにて混練した後、粉
砕して粉末の発泡性樹脂組成物を得た。
Comparative Example 2 The formulation of Comparative Example 1 was kneaded with a heating roll and then ground to obtain a powdered foamable 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
用したマットに5g噴霧した。この結合剤を吸収したマ
ットの上に発泡性樹脂組成物30g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10
0分間乾燥した。次いでこのシートを25cm X 2
5cm X 1 cmの金型にいれ150℃IO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。
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 mat used in Example 1 in a mist form using a nozzle. 30g of the foamable resin composition was sprinkled on the mat that had absorbed the binder, and then a mat that had also absorbed the binder was placed on top of it, preformed under a pressure of about 1 kg, and then hot air circulated at 60°C. 10 in a tank
Dry for 0 minutes. Next, divide this sheet into 25cm x 2
The mixture was placed in a 5 cm x 1 cm mold and heated at 150° C. for IO minutes to form a foam. 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〕〔Effect of the invention〕

本発明によれば、レゾールが硬化剤として作用するため
発泡硬化時のアンモニア臭の発生の問題もなく、また繊
維とフェノール樹脂が均一に混在する発泡複合体が効率
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。
According to the present invention, since the resol acts as a curing agent, there is no problem of generation of ammonia odor during foam curing, and a foamed composite in which fibers and phenolic resin are evenly mixed can be efficiently and stably obtained. . Since this sheet-shaped foamed 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.

特許出願人 昭和高分子株式会社 代 理 人Patent applicant: Showa Kobunshi Co., Ltd. teenager Reason Man

Claims (3)

【特許請求の範囲】[Claims] (1)ノボラック及びレゾールからなる混合フェノール
樹脂、該樹脂が可溶な溶剤、発泡剤並びに整泡剤を含む
混合液を、シート状の不織繊維基材に含浸し、乾燥した
後に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) Impregnating a sheet-shaped nonwoven fiber base material with a mixed liquid containing a mixed phenolic resin consisting of novolac and resol, a solvent in which the resin is soluble, a foaming agent, and a foam stabilizer, and foaming after drying. A method for producing a phenolic resin foam characterized by:
(2)ノボラック及びレゾールからなる混合フェノール
樹脂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 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 solvent in which the mixed phenolic resin consisting of novolak and resol is soluble. manufacturing method.
(3)レゾールの自己架橋により硬化を行うことを特徴
とする特許請求の範囲第1項又は第2項記載のフェノー
ル樹脂発泡体の製造方法。
(3) The method for producing a phenolic resin foam according to claim 1 or 2, wherein the curing is carried out by self-crosslinking of the resol.
JP10897689A 1989-04-27 1989-04-27 Production of foamed phenolic resin Granted JPH02284932A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10897689A JPH02284932A (en) 1989-04-27 1989-04-27 Production of foamed phenolic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10897689A JPH02284932A (en) 1989-04-27 1989-04-27 Production of foamed phenolic resin

Publications (2)

Publication Number Publication Date
JPH02284932A true JPH02284932A (en) 1990-11-22
JPH0575779B2 JPH0575779B2 (en) 1993-10-21

Family

ID=14498423

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10897689A Granted JPH02284932A (en) 1989-04-27 1989-04-27 Production of foamed phenolic resin

Country Status (1)

Country Link
JP (1) JPH02284932A (en)

Also Published As

Publication number Publication date
JPH0575779B2 (en) 1993-10-21

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