JP2003342381A - Method for producing fiber reinforced phenolic resin molded product and fiber reinforced phenolic resin molded product - Google Patents
Method for producing fiber reinforced phenolic resin molded product and fiber reinforced phenolic resin molded productInfo
- Publication number
- JP2003342381A JP2003342381A JP2002155490A JP2002155490A JP2003342381A JP 2003342381 A JP2003342381 A JP 2003342381A JP 2002155490 A JP2002155490 A JP 2002155490A JP 2002155490 A JP2002155490 A JP 2002155490A JP 2003342381 A JP2003342381 A JP 2003342381A
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- Japan
- Prior art keywords
- weight
- phenolic resin
- molded product
- resin
- fiber
- 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.)
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- Moulding By Coating Moulds (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Phenolic Resins Or Amino Resins (AREA)
- Reinforced Plastic Materials (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、繊維強化フェノー
ル樹脂(以下、フェノールFRPと称す。)成形物の製
造方法に関する。さらに詳しくは、本発明は、従来のフ
ェノールFRP成形物に比べ、高強度化されたフェノー
ルFRP成形物を製造する方法及び該方法で得られた高
強度のフェノールFRP成形物に関するものである。TECHNICAL FIELD The present invention relates to a method for producing a fiber-reinforced phenolic resin (hereinafter referred to as phenol FRP) molded article. More specifically, the present invention relates to a method for producing a phenol FRP molded product having a higher strength than that of a conventional phenol FRP molded product, and a high-strength phenol FRP molded product obtained by the method.
【0002】[0002]
【従来の技術】近年、フェノールFRP成形物は、不飽
和ポリエステル樹脂、エポキシ樹脂などの熱硬化性樹脂
FRP成形物やポリプロピレン樹脂、ポリエチレン樹
脂、ポリスチレン樹脂などの熱可塑性樹脂FRP成形物
では得られない耐熱性、耐燃性、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。最近では、フェノールFRP成形物の構造材へ
の応用も検討されている。しかしながら、従来のレゾー
ル型フェノール樹脂をガラス繊維に含浸させて熱硬化さ
せる場合、硬化時に発生するガスやガラス繊維とのなじ
みの悪さが影響し、所望の強度が出ないのが現状であ
る。建築物構造材へ応用するためには耐熱性、耐燃性を
保持しつつ、更なる高強度化が求められている。2. Description of the Related Art In recent years, phenol FRP moldings have not been obtained with thermosetting resin FRP moldings such as unsaturated polyester resin and epoxy resin, or thermoplastic resin FRP moldings such as polypropylene resin, polyethylene resin and polystyrene resin. Since it has various excellent properties such as heat resistance, flame resistance, and low smoke generation, its usefulness has received a great deal of attention. Recently, the application of phenol FRP moldings to structural materials has also been investigated. However, in the case of impregnating glass fiber with a conventional resol-type phenolic resin and thermally curing it, it is the present situation that the desired strength cannot be obtained due to influence of gas generated during curing and poor compatibility with glass fiber. In order to apply it to building structural materials, it is required to have higher strength while maintaining heat resistance and flame resistance.
【0003】ところで、レゾルシンを用いたフェノール
FRP成形物の技術としては、フェノール樹脂とレゾル
シノール樹脂を別々に作製しておいて、これらを混合す
る方法が開示されている(特開平2−215879号公
報、特開平7−60928号公報)。しかしながら、こ
れらはいずれもレゾルシノール樹脂成分として、レゾル
シンとホルムアルデヒドとを酸触媒を用いて合成したノ
ボラックが用いられ、このものは基本的に固形あるいは
半固形であることから、液状とするためには希釈剤的な
ものが必要であり、その結果物性、耐燃性などに悪影響
を及ぼしかねない。また、酸触媒残渣(塩等)による金
属に対する腐食が懸念される。By the way, as a technique of a phenol FRP molded article using resorcin, a method of preparing a phenol resin and a resorcinol resin separately and mixing them is disclosed (JP-A-2-215879). , JP-A-7-60928). However, in all of these, novolak, which is a resorcinol resin component synthesized with resorcin and formaldehyde using an acid catalyst, is used, and since this is basically a solid or semi-solid, it is necessary to dilute it to make it a liquid. A chemical agent is required, and as a result, physical properties and flame resistance may be adversely affected. In addition, there is a concern that the acid catalyst residue (salt, etc.) may corrode the metal.
【0004】また、アルカリ触媒を用いてレゾール型フ
ェノール樹脂を作製し、その後レゾルシンとホルムアル
デヒドを添加して二段で反応させ、硬化剤としてパラホ
ルムアルデヒドを用いる技術が開示されており(特開平
6−192360号公報)、そして70〜110℃の低
温で速硬化が可能としているが、その反面110℃より
高い型温では、成形表面に凹凸が発生することが示唆さ
れている。レゾルシノール樹脂の架橋反応は、比較的低
温でも進行するが、前記温度域でのレゾール型フェノー
ル樹脂の縮合反応においては完全硬化は望めず、高温
(実施例では125℃)でのポストキュアが必要となる
上、硬化が不均一となりやすく、その結果特性の低下が
懸念される。Further, a technique has been disclosed in which a resole-type phenol resin is prepared using an alkali catalyst, then resorcinol and formaldehyde are added and reacted in two steps, and paraformaldehyde is used as a curing agent. No. 192360), and rapid curing is possible at a low temperature of 70 to 110 ° C. However, it is suggested that a mold temperature higher than 110 ° C. causes unevenness on the molding surface. Although the cross-linking reaction of the resorcinol resin proceeds even at a relatively low temperature, complete curing cannot be expected in the condensation reaction of the resole-type phenol resin in the above temperature range, and post cure at a high temperature (125 ° C. in the example) is required. In addition, the curing tends to be non-uniform, and as a result, there is concern that the characteristics may deteriorate.
【0005】[0005]
【発明が解決しようとする課題】本発明は、このような
状況下で、高強度を有すると共に、耐熱性、耐燃性など
に優れ、建築物構造材への応用が容易なフェノールFR
P成形物を製造する方法及びこの方法で得られた上記特
性を有するフェノールFRP成形物を提供することを目
的とするものである。Under the circumstances, the present invention provides phenol FR which has high strength, excellent heat resistance and flame resistance, and is easily applied to building structural materials.
It is an object of the present invention to provide a method for producing a P molded product and a phenol FRP molded product having the above characteristics obtained by this method.
【0006】[0006]
【課題を解決するための手段】本発明者らは、前記目的
を達成するために鋭意研究を重ねた結果、遊離ホルムア
ルデヒドを含むレゾール型フェノール樹脂液とレゾルシ
ン類を含むレゾール型フェノール樹脂液とを混合するこ
とにより得られた、レゾール型フェノール樹脂と遊離ホ
ルムアルデヒドとレゾルシン類を特定の割合で含む液状
物からなる樹脂組成物を繊維強化材に含浸させて加熱硬
化させた場合、樹脂中に含まれる遊離ホルムアルデヒド
とレゾルシン類が該繊維強化材の周囲で反応するため、
繊維強化材と樹脂とが強く結合し高強度化されたフェノ
ールFRP成形物が得られ、その目的を達成し得ること
を見出した。本発明は、かかる知見に基づいて完成した
ものである。Means for Solving the Problems As a result of intensive studies to achieve the above-mentioned object, the present inventors have found that a resole-type phenol resin solution containing free formaldehyde and a resole-type phenol resin solution containing resorcins are obtained. Obtained by mixing, when the resin composition consisting of a liquid material containing a resol type phenol resin, free formaldehyde and resorcins in a specific ratio is impregnated into the fiber reinforcement and heat-cured, it is contained in the resin. Since free formaldehyde and resorcins react around the fiber reinforcement,
It has been found that a phenol FRP molded article having a high strength obtained by strongly bonding the fiber reinforcing material and the resin can be obtained, and that the object can be achieved. The present invention has been completed based on such findings.
【0007】すなわち、本発明は、(1)(A)遊離ホ
ルムアルデヒド2〜15重量%を含むレゾール型フェノ
ール樹脂液と(B)レゾルシン類15〜60重量%を含
むレゾール型フェノール樹脂液とを混合することにより
得られた、レゾール型フェノール樹脂と、その100重
量部当たり、遊離ホルムアルデヒド3〜18重量部及び
レゾルシン類1〜40重量部を含む液状物からなる樹脂
組成物を繊維強化材に含浸させて熱硬化させることを特
徴とする繊維強化フェノール樹脂成形物の製造方法、
(2)(B)成分において、レゾルシン類を混合溶解す
る前のレゾール型フェノール樹脂液中の遊離ホルムアル
デヒドの含有量が5重量%以下である上記(1)の繊維
強化フェノール樹脂成形物の製造方法、(3)(A)成
分のレゾール型フェノール樹脂液中の樹脂固形分量が6
0〜85重量%である上記(1)又は(2)の繊維強化
フェノール樹脂成形物の製造方法、(4)(B)成分に
おいて、レゾルシン類を混合溶解する前のレゾール型フ
ェノール樹脂液中の樹脂固形分量が40〜80重量%で
ある上記(1)〜(3)のいずれかの繊維強化フェノー
ル樹脂成形物の製造方法、(5)引抜き成形法又はフィ
ラメントワインディング成形法により、120〜200
℃の温度で加熱硬化させる上記(1)〜(4)のいずれ
かの繊維強化フェノール樹脂成形物の製造方法、及び
(6)上記(1)〜(5)のいずれかの方法によって得
られた繊維強化フェノール樹脂成形物、を提供するもの
である。That is, according to the present invention, (1) (A) a resole type phenol resin solution containing 2 to 15% by weight of free formaldehyde and (B) a resole type phenol resin solution containing 15 to 60% by weight of resorcins are mixed. The fiber reinforced material is impregnated with a resin composition comprising a resol-type phenol resin obtained by the above, and a liquid material containing 3 to 18 parts by weight of free formaldehyde and 1 to 40 parts by weight of resorcins per 100 parts by weight thereof. A method for producing a fiber-reinforced phenolic resin molded article, which comprises heat curing by
(2) In the component (B), the method for producing the fiber-reinforced phenolic resin molded product according to (1) above, wherein the content of free formaldehyde in the resole-type phenolic resin liquid before mixing and dissolving the resorcins is 5% by weight or less. , (3) the resin solid content in the resol-type phenolic resin liquid of (A) is 6
0 to 85% by weight of the method for producing a fiber-reinforced phenolic resin molding according to the above (1) or (2), (4) in the component (B), in the resole-type phenolic resin liquid before mixing and dissolving resorcins 120 to 200 by the method for producing a fiber-reinforced phenolic resin molded product according to any one of (1) to (3) above, which has a resin solid content of 40 to 80% by weight, and (5) a pultrusion molding method or a filament winding molding method.
Obtained by the method for producing a fiber-reinforced phenolic resin molded product according to any one of (1) to (4) above, which is heat-cured at a temperature of ° C, and (6) any one of the above methods (1) to (5). A fiber-reinforced phenolic resin molded product is provided.
【0008】[0008]
【発明の実施の形態】本発明のフェノールFRP成形物
の製造方法において、繊維強化材に含浸させて使用する
樹脂組成物は、レゾール型フェノール樹脂と遊離ホルム
アルデヒドとレゾルシン類を含む液状物からなるもので
ある。該樹脂組成物においては、レゾール型フェノール
樹脂100重量部当たり、遊離ホルムアルデヒドは3〜
18重量部の範囲で含まれ、一方レゾルシン類は1〜4
0重量部の範囲で含まれる。前記遊離ホルムアルデヒド
の含有量が3重量部未満では、レゾルシン類との反応が
少ないため、硬化が遅くなるおそれがあり、また18重
量部を超えると、ポットライフが短くなる傾向がある
上、成形物中の遊離ホルムアルデヒドが多くなり、環境
衛生の点でも好ましくない。この遊離ホルムアルデヒド
のより好ましい含有量は、4〜10重量部の範囲であ
る。BEST MODE FOR CARRYING OUT THE INVENTION In the method for producing a phenol FRP molded article according to the present invention, the resin composition used by impregnating the fiber reinforced material is a liquid material containing a resol type phenol resin, free formaldehyde and resorcins. Is. In the resin composition, the free formaldehyde is 3 to 100 parts by weight of the resol type phenol resin.
The content of resorcinol is 1 to 4
It is contained in the range of 0 parts by weight. When the content of the free formaldehyde is less than 3 parts by weight, the reaction with resorcins is small, so that the curing may be delayed, and when it exceeds 18 parts by weight, the pot life tends to be shortened, and the molded product is also formed. The amount of free formaldehyde in the product increases, which is not preferable in terms of environmental hygiene. The more preferable content of the free formaldehyde is in the range of 4 to 10 parts by weight.
【0009】一方、レゾルシン類の含有量が、1重量部
未満では、成形物の機械的強度が充分に向上せず、また
40重量部を超えるとレゾルシン類をレゾール型フェノ
ール樹脂液中に完全に溶解させることができにくくな
る。このレゾルシン類の好ましい含有量は、5〜15重
量部の範囲である。前記レゾルシン類としては、例えば
レゾルシン、アルキル置換レゾルシン、アルコキシ置換
レゾルシンなどが挙げられ、これらは一種を単独で用い
てもよく、二種以上を組み合わせて用いてもよい。本発
明で使用する樹脂組成物におけるレゾール型フェノール
樹脂及びレゾルシン類の合計濃度としては、繊維強化材
に含浸させるのに適した粘度が得られればよく、特に制
限はないが、通常50〜90重量%、好ましくは60〜
85重量%の範囲である。On the other hand, if the content of the resorcins is less than 1 part by weight, the mechanical strength of the molded product is not sufficiently improved, and if it exceeds 40 parts by weight, the resorcins are completely contained in the resol type phenol resin solution. It becomes difficult to dissolve it. The preferable content of the resorcins is in the range of 5 to 15 parts by weight. Examples of the resorcins include resorcin, alkyl-substituted resorcin, and alkoxy-substituted resorcin. These may be used alone or in combination of two or more. The total concentration of the resole type phenolic resin and the resorcins in the resin composition used in the present invention is not particularly limited as long as a viscosity suitable for impregnating the fiber reinforcement is obtained, but is usually 50 to 90 weight. %, Preferably 60 to
It is in the range of 85% by weight.
【0010】本発明の方法においては、このようなレゾ
ール型フェノール樹脂と共に、遊離ホルムアルデヒド及
びレゾルシン類を含む樹脂組成物を、(A)遊離ホルム
アルデヒド2〜15重量%を含むレゾール型フェノール
樹脂液と(B)レゾルシン類15〜60重量%を含むレ
ゾール型フェノール樹脂液とを混合することにより調製
することが必要であり、単にレゾール型フェノール樹脂
液に遊離ホルムアルデヒド及びレゾルシン類を添加して
前記の含有割合に調整したのでは、所期の効果を十分に
得ることはできない。In the method of the present invention, a resin composition containing free formaldehyde and resorcins together with such a resole type phenolic resin is (A) a resol type phenolic resin liquid containing 2 to 15% by weight of free formaldehyde. B) It is necessary to prepare by mixing with a resole-type phenol resin solution containing 15 to 60% by weight of resorcins, and it is necessary to simply add free formaldehyde and resorcins to the resole-type phenol resin solution and the above content ratio. If you adjust to, you can not get the desired effect.
【0011】前記(A)成分及び(B)成分におけるレ
ゾール型フェノール樹脂液は、従来公知の方法、すなわ
ちフェノール類とホルムアルデヒドを、アルカリ触媒の
存在下に反応させることにより、得ることができる。こ
こで、フェノール類としては、例えばフェノール、クレ
ゾール類、キシレノール類、ブチルフェノール類、p−
メトキシフェノール、ビスフェノールA、ビスフェノー
ルFなどが挙げられ、これらは一種を単独で用いてもよ
く、二種以上を組み合わせて用いてもよい。The resol type phenol resin solution in the components (A) and (B) can be obtained by a conventionally known method, that is, by reacting phenols with formaldehyde in the presence of an alkali catalyst. Here, as the phenols, for example, phenol, cresols, xylenols, butylphenols, p-
Methoxyphenol, bisphenol A, bisphenol F, etc. may be mentioned, and these may be used alone or in combination of two or more.
【0012】一方、アルカリ触媒としては、例えば金属
水酸化物、金属酸化物、金属塩及びアミノ基を含むアミ
ノ化合物などを挙げることができ、具体的には水酸化ナ
トリウム、水酸化アンモニウム、水酸化カリウム、水酸
化カルシウム、水酸化バリウム、水酸化マグネシウム、
酸化マグネシウム、酸化カルシウム、酸化ナトリウム、
酸化カリウム、酢酸亜鉛、酢酸鉛、トリエチルアミン、
ヘキサメチレンテトラミン、ジメチルエタノールアミ
ン、アンモニア等が例示される。これらのアルカリ触媒
は、一種を単独で用いてもよく、二種以上を組み合わせ
て用いてもよい。On the other hand, examples of the alkali catalyst include metal hydroxides, metal oxides, metal salts and amino compounds containing amino groups. Specific examples thereof include sodium hydroxide, ammonium hydroxide, and hydroxide. Potassium, calcium hydroxide, barium hydroxide, magnesium hydroxide,
Magnesium oxide, calcium oxide, sodium oxide,
Potassium oxide, zinc acetate, lead acetate, triethylamine,
Hexamethylenetetramine, dimethylethanolamine, ammonia and the like are exemplified. These alkali catalysts may be used alone or in combination of two or more.
【0013】前記(A)成分と(B)成分の混合割合に
ついては、得られる樹脂組成物の遊離ホルムアルデヒド
及びレゾルシン類の含有量が、レゾール型フェノール樹
脂に対して、前記の範囲にあればよく、特に制限はな
い。また、(B)成分において、レゾルシン類を混合溶
解する前のレゾール型フェノール樹脂液中の遊離ホルム
アルデヒドの含有量は、5重量%以下に調整することが
好ましい。この遊離ホルムアルデヒドの含有量が5重量
%を超えるとレゾルシン類とホルムアルデヒドとの反応
が進み、その反応物の影響により、粘度上昇が速く、
(B)成分自体の貯蔵安定性が悪化する原因となる。更
にまた、(A)成分のレゾール型フェノール樹脂液中の
樹脂固形分量は、60〜85重量%であるのが好まし
く、(B)成分において、レゾルシン類を混合溶解する
前のレゾール型フェノール樹脂液中の樹脂固形分量は、
40〜80重量%であるのが好ましい。樹脂固形分量が
これらの範囲未満では成形品の強度等の物性の低下を生
じる恐れがあり、これらの範囲を超えると樹脂液自体の
粘度が高くなり、両成分の混合時に混合不良を起す恐れ
がある。Regarding the mixing ratio of the above-mentioned components (A) and (B), the content of free formaldehyde and resorcins in the obtained resin composition may be within the above range with respect to the resole type phenol resin. , There is no particular limitation. In the component (B), the content of free formaldehyde in the resol type phenol resin solution before mixing and dissolving the resorcins is preferably adjusted to 5% by weight or less. If the content of free formaldehyde exceeds 5% by weight, the reaction between resorcinols and formaldehyde proceeds, and the viscosity of the reaction product increases rapidly due to the influence of the reaction product.
This causes deterioration of storage stability of the component (B) itself. Furthermore, the resin solid content in the resol type phenolic resin liquid of the component (A) is preferably 60 to 85% by weight, and the resole type phenolic resin liquid before mixing and dissolving the resorcins in the component (B). The resin solid content in the
It is preferably 40 to 80% by weight. If the resin solid content is less than these ranges, physical properties such as strength of the molded product may be deteriorated, and if the resin solid content exceeds these ranges, the viscosity of the resin liquid itself becomes high, and there is a risk of poor mixing when mixing both components. is there.
【0014】本発明のフェノールFRP成形物の製造方
法においては、このようにして得られた樹脂組成物を繊
維強化材に含浸させ、熱硬化させるが、(A)成分と
(B)成分とを混合した液状物の状態で長時間置いた場
合、レゾルシン類とホルムアルデヒドとの反応が進み、
本発明の効果を十分得ることができない恐れがあるた
め、混合してから24時間以内に繊維強化材に含浸させ
るのが好ましい。この樹脂組成物は、通常120〜20
0℃の範囲の温度で熱硬化させることができる。また、
一般の引抜き成形機を用いる場合、金型の温度が150
〜200℃程度において、成形が可能である。樹脂組成
物には、必要に応じ、従来フェノールFRP成形物用と
して用いられるフェノール系樹脂組成物に慣用されてい
る各種添加剤を配合することができる。該添加剤として
は、例えば炭酸カルシウム、クレー、タルク、水酸化ア
ルミニウム、硫酸バリウム、硫酸カルシウム等の充填
材、金属石鹸、ワックス類等の離型剤などを挙げること
ができる。In the method for producing a phenol FRP molded article of the present invention, the resin composition thus obtained is impregnated into the fiber reinforced material and heat cured, but the components (A) and (B) are combined. When left in a mixed liquid state for a long time, the reaction between resorcins and formaldehyde proceeds,
Since the effects of the present invention may not be sufficiently obtained, it is preferable to impregnate the fiber reinforcement within 24 hours after mixing. This resin composition is usually 120 to 20.
It can be thermoset at temperatures in the range of 0 ° C. Also,
When using a general pultrusion machine, the mold temperature is 150
Molding is possible at about 200 ° C. If necessary, the resin composition may be mixed with various additives that are conventionally used in phenolic resin compositions conventionally used for phenol FRP molded products. Examples of the additive include fillers such as calcium carbonate, clay, talc, aluminum hydroxide, barium sulfate and calcium sulfate, and release agents such as metal soaps and waxes.
【0015】本発明の製造方法において使用する繊維強
化材としては、例えばガラス繊維、炭素繊維、あるいは
アラミド繊維等の合成繊維などからなるチョップドスト
ランドマット、コンティニュアスマット、ロービング、
ロービングクロス、すだれクロス等が挙げられる。ま
た、各種繊維強化材は、シラン処理、ボロン処理等、通
常の表面処理を行ったものを用いることができる。Examples of the fiber reinforcement used in the production method of the present invention include chopped strand mats, continuous mats, rovings made of synthetic fibers such as glass fibers, carbon fibers, or aramid fibers.
Examples include roving cloth and blind cloth. Further, as various fiber reinforcing materials, those subjected to usual surface treatment such as silane treatment and boron treatment can be used.
【0016】また、成形方法としては、従来公知の各種
成形法、例えば、フィラメントワインディング(FW)
法、レジンインジェクション(RTM)法、引抜き(P
L)法、SMC法などを採用することができるが、これ
らの成形法の中で、引抜き法又はフィラメントワインデ
ィング法を用い、120〜200℃程度の温度で硬化さ
せることが好ましい。本発明においては、この熱硬化時
に樹脂成分中に含まれる遊離ホルムアルデヒドとレゾル
シン類とが反応し、接着性に優れるレゾルシノール樹脂
が効率よく、繊維強化材周辺に該繊維強化材とレゾール
型フェノール樹脂になじむ形で形成されるものと思われ
る。その結果、得られたフェノールFRP成形物は、機
械的強度、耐熱性、耐燃性などに優れ、特に機械的強度
は、従来のものに比べて大幅に向上する。As the molding method, various conventionally known molding methods such as filament winding (FW) can be used.
Method, resin injection (RTM) method, drawing (P
L) method, SMC method, etc. can be adopted, but among these molding methods, it is preferable to use a drawing method or a filament winding method and cure at a temperature of about 120 to 200 ° C. In the present invention, the free formaldehyde contained in the resin component reacts with the resorcins during the heat curing, and the resorcinol resin having excellent adhesiveness is efficiently used, and the fiber reinforced material and the resole type phenol resin are efficiently formed around the fiber reinforced material. It seems to be formed in a conforming manner. As a result, the obtained phenol FRP molded product is excellent in mechanical strength, heat resistance, flame resistance and the like, and in particular, the mechanical strength is significantly improved as compared with the conventional one.
【0017】[0017]
【実施例】次に、本発明を実施例により、さらに詳細に
説明するが、本発明は、これらの例によってなんら限定
されるものではない。
製造例1
フェノール100重量部と37重量%ホルマリン水溶液
123重量部と酢酸亜鉛水和物2.0重量部の混合物
を、100℃で3時間加熱して反応させたのち、減圧脱
水して遊離ホルムアルデヒド含有量が2.5重量%、2
5℃粘度が6,000mPa・s、樹脂固形分量が74
重量%のレゾール型フェノール樹脂液Iを150重量部
得た。EXAMPLES The present invention will now be described in more detail with reference to examples, but the present invention is not limited to these examples. Production Example 1 A mixture of 100 parts by weight of phenol, 123 parts by weight of a 37% by weight aqueous formalin solution and 2.0 parts by weight of zinc acetate hydrate was heated at 100 ° C. for 3 hours to cause reaction, and then dehydrated under reduced pressure to form free formaldehyde. 2.5% by weight, 2
5 ° C viscosity 6,000 mPa · s, resin solid content 74
150 parts by weight of a resol type phenol resin solution I having a weight percentage of 50% was obtained.
【0018】製造例2
フェノール100重量部と37重量%ホルマリン水溶液
170重量部と酢酸亜鉛水和物2.0重量部の混合物
を、100℃で3時間加熱して反応させたのち、減圧脱
水して遊離ホルムアルデヒド含有量が13.4重量%、
25℃粘度が5,500mPa・s、樹脂固形分量が7
0重量%のレゾール型フェノール樹脂液IIを155重量
部得た。Production Example 2 A mixture of 100 parts by weight of phenol, 170 parts by weight of 37% by weight formalin aqueous solution and 2.0 parts by weight of zinc acetate hydrate was heated at 100 ° C. for 3 hours to cause reaction, and then dehydrated under reduced pressure. Has a free formaldehyde content of 13.4% by weight,
25 ° C viscosity 5,500 mPa · s, resin solid content 7
155 parts by weight of 0% by weight of resol type phenol resin solution II was obtained.
【0019】製造例3
フェノール100重量部と37重量%ホルマリン水溶液
150重量部と水酸化ナトリウム2.0重量部の混合物
を、80℃で2時間加熱して反応させたのち、減圧脱水
して遊離ホルムアルデヒド含有量が3.5重量%、25
℃粘度が4,000mPa・s、樹脂固形分量が73重
量%のレゾール型フェノール樹脂液IIIを160重量部
得た。Production Example 3 A mixture of 100 parts by weight of phenol, 150 parts by weight of a 37% by weight formalin aqueous solution and 2.0 parts by weight of sodium hydroxide was heated at 80 ° C. for 2 hours to cause a reaction, and then dehydrated under reduced pressure to liberate. Formaldehyde content 3.5% by weight, 25
160 parts by weight of a resol type phenolic resin liquid III having a viscosity of 4,000 mPa · s and a resin solid content of 73% by weight was obtained.
【0020】製造例4
フェノール100重量部と37重量%ホルマリン水溶液
108重量部と水酸化ナトリウム8重量部の混合物を、
70℃で3時間加熱して反応させたのち、反応生成物を
減圧脱水して遊離ホルムアルデヒド含有量が0.6重量
%、樹脂固形分量が69重量%のレゾール型フェノール
樹脂液150重量部を得た。なおレゾール型フェノール
樹脂のポリスチレン換算重量平均分子量は150であっ
た。次いで、このレゾール型フェノール樹脂液100重
量部に対し、レゾルシン20重量部を加え、35℃で3
0分間撹拌溶解し、25℃粘度が500mPa・s、p
H8.0のレゾール型フェノール樹脂液IVを120重量
部得た。Production Example 4 A mixture of 100 parts by weight of phenol, 108 parts by weight of 37% by weight aqueous formalin solution and 8 parts by weight of sodium hydroxide was added,
After heating at 70 ° C. for 3 hours to cause reaction, the reaction product was dehydrated under reduced pressure to obtain 150 parts by weight of a resol type phenol resin solution having a free formaldehyde content of 0.6% by weight and a resin solid content of 69% by weight. It was The polystyrene-reduced weight average molecular weight of the resol-type phenol resin was 150. Then, 20 parts by weight of resorcin was added to 100 parts by weight of this resole type phenol resin solution, and the mixture was mixed at 35 ° C. for 3 hours.
Dissolve with stirring for 0 minutes and the viscosity at 25 ° C is 500 mPa · s, p
120 parts by weight of H8.0 resol type phenol resin solution IV was obtained.
【0021】製造例5
フェノール100重量部と37重量%ホルマリン水溶液
125重量部と水酸化ナトリウム8重量部の混合物を、
70℃で3時間加熱して反応させたのち、反応生成物を
減圧脱水して遊離ホルムアルデヒド含有量が1.5重量
%、樹脂固形分量が67重量%のレゾール型フェノール
樹脂液150重量部を得た。なおレゾール型フェノール
樹脂のポリスチレン換算重量平均分子量は150であっ
た。次いで、このレゾール型フェノール樹脂液100重
量部に対し、レゾルシン80重量部を加え、35℃で3
0分間撹拌溶解し、25℃粘度が900mPa・s、p
H7.5のレゾール型フェノール樹脂液Vを180重量
部得た。Production Example 5 A mixture of 100 parts by weight of phenol, 125 parts by weight of a 37% by weight aqueous formalin solution, and 8 parts by weight of sodium hydroxide was added.
After heating at 70 ° C. for 3 hours for reaction, the reaction product was dehydrated under reduced pressure to obtain 150 parts by weight of a resol-type phenol resin solution having a free formaldehyde content of 1.5% by weight and a resin solid content of 67% by weight. It was The polystyrene-reduced weight average molecular weight of the resol-type phenol resin was 150. Next, 80 parts by weight of resorcin was added to 100 parts by weight of this resol type phenol resin solution, and the mixture was mixed at 35 ° C. for 3 days.
Dissolve with stirring for 0 minutes, and the viscosity at 25 ° C is 900 mPa · s, p
180 parts by weight of H7.5 resol type phenol resin solution V was obtained.
【0022】実施例1
レゾール型フェノール樹脂液I:100重量部、レゾー
ル型フェノール樹脂液IV:5重量部、クレー20重量部
及び離型剤2重量部を混合し、樹脂組成物を調製すると
共に、この樹脂組成物のポットライフ(40℃で樹脂組
成物の流動性がなくなるまでの時間)を測定した。次
に、上記樹脂組成物をガラス繊維材に含浸させ、引抜き
成形機を用いて、厚さ3mm、幅300mmのボードを
成形した。その際、金型の温度は200℃、引抜き成形
速度は20cm/minとした。上記ボードの機械的特
性を測定し、その結果を前記ポットライフと共に、第1
表に示す。なお、レゾール型フェノール樹脂液I及びレ
ゾール型フェノール樹脂液IVを混合してから、ガラス繊
維材に含浸させるまでの時間は、7時間であった。Example 1 Resol type phenol resin solution I: 100 parts by weight, resol type phenol resin solution IV: 5 parts by weight, 20 parts by weight of clay and 2 parts by weight of a releasing agent are mixed to prepare a resin composition. The pot life of this resin composition (time until the resin composition loses fluidity at 40 ° C.) was measured. Next, a glass fiber material was impregnated with the above resin composition, and a board having a thickness of 3 mm and a width of 300 mm was molded using a pultrusion molding machine. At that time, the temperature of the mold was 200 ° C., and the drawing speed was 20 cm / min. The mechanical properties of the board were measured, and the result was measured along with the pot life to
Shown in the table. The time from the mixing of the resol type phenol resin solution I and the resol type phenol resin solution IV to the impregnation of the glass fiber material was 7 hours.
【0023】実施例2〜5
第1表に示す配合組成の樹脂組成物を調製し、実施例1
と同様にしてボードを成形した。樹脂組成物のポットラ
イフ及びボードの機械的特性を第1表に示す。Examples 2 to 5 A resin composition having the composition shown in Table 1 was prepared, and Example 1 was prepared.
A board was molded in the same manner as in. The pot life of the resin composition and the mechanical properties of the board are shown in Table 1.
【0024】比較例1
従来型のレゾール樹脂として、「BRL−240」〔昭
和高分子(株)製、商品名〕を用い、第1表に示す配合
組成の樹脂組成物を調製し、実施例1と同様にしてボー
ドを成形した。樹脂組成物のポットライフ及びボードの
機械的特性を第1表に示す。Comparative Example 1 As a conventional resole resin, "BRL-240" (trade name, manufactured by Showa Highpolymer Co., Ltd.) was used to prepare a resin composition having the composition shown in Table 1, and an example was prepared. Boards were molded as in 1. The pot life of the resin composition and the mechanical properties of the board are shown in Table 1.
【0025】比較例2、3
第1表に示す配合組成の樹脂組成物を調製し、実施例1
と同様にしてボードを成形した。樹脂組成物のポットラ
イフ及びボードの機械的特性を第1表に示す。Comparative Examples 2 and 3 A resin composition having the composition shown in Table 1 was prepared, and Example 1 was prepared.
A board was molded in the same manner as in. The pot life of the resin composition and the mechanical properties of the board are shown in Table 1.
【0026】[0026]
【表1】 [Table 1]
【0027】[0027]
【表2】 [Table 2]
【0028】〔注〕
離型剤:モールドウイズJNT−1850HT(商品
名、アクセル社製)
圧縮強さ:JIS K 7056
曲げ強さ:JIS K 7055
曲げ弾性率:JIS K 7055
引張り強度:JIS K 7054
引張り弾性率:JIS K 7054[Note] Release agent: Moldwith JNT-1850HT (trade name, manufactured by Axel) Compressive strength: JIS K 7056 Bending strength: JIS K 7055 Bending elastic modulus: JIS K 7055 Tensile strength: JIS K 7054 Tensile modulus: JIS K 7054
【0029】[0029]
【発明の効果】本発明の方法によれば、従来のフェノー
ルFRP成形物に比べて、高強度化され、機械的特性に
優れたフェノールFRP成形物を製造することができ
る。According to the method of the present invention, it is possible to produce a phenol FRP molded product having higher strength and excellent mechanical properties as compared with the conventional phenol FRP molded product.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // B29K 61:04 B29C 67/14 A 105:06 D Fターム(参考) 4F072 AA04 AA07 AB09 AB22 AD16 AG02 AG03 AH04 AH22 AJ04 AK11 AK17 AL17 4F205 AA37 AB11 AD16 HA02 HA05 HA33 HA35 HA46 HM02 HM03 4J002 CC041 CC042 EJ016 FD010 FD146 HA04 4J033 CA02 CA09 CA11 CA13 CA29 CB18 CB21 HA13 HB02 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) // B29K 61:04 B29C 67/14 A 105: 06 DF term (reference) 4F072 AA04 AA07 AB09 AB22 AD16 AG02 AG03 AH04 AH22 AJ04 AK11 AK17 AL17 4F205 AA37 AB11 AD16 HA02 HA05 HA33 HA35 HA46 HM02 HM03 4J002 CC041 CC042 EJ016 FD010 FD146 HA04 4J033 CA02 CA09 CA11 CA13 CA29 CB18 CB21 HA13 HB02
Claims (6)
量%を含むレゾール型フェノール樹脂液と(B)レゾル
シン類15〜60重量%を含むレゾール型フェノール樹
脂液とを混合することにより得られた、レゾール型フェ
ノール樹脂と、その100重量部当たり、遊離ホルムア
ルデヒド3〜18重量部及びレゾルシン類1〜40重量
部を含む液状物からなる樹脂組成物を繊維強化材に含浸
させて熱硬化させることを特徴とする繊維強化フェノー
ル樹脂成形物の製造方法。1. A mixture of (A) a resole type phenol resin solution containing 2 to 15% by weight of free formaldehyde and (B) a resole type phenol resin solution containing 15 to 60% by weight of resorcins, A resin composition composed of a resole-type phenol resin and a liquid material containing 3 to 18 parts by weight of free formaldehyde and 1 to 40 parts by weight of resorcin per 100 parts by weight thereof is impregnated into a fiber reinforced material and thermally cured. And a method for producing a fiber-reinforced phenolic resin molded product.
合溶解する前のレゾール型フェノール樹脂液中の遊離ホ
ルムアルデヒドの含有量が5重量%以下である請求項1
記載の繊維強化フェノール樹脂成形物の製造方法。2. In the component (B), the content of free formaldehyde in the resol type phenol resin solution before mixing and dissolving resorcins is 5% by weight or less.
A method for producing the fiber-reinforced phenolic resin molding described.
液中の樹脂固形分量が60〜85重量%である請求項1
又は2に記載の繊維強化フェノール樹脂成形物の製造方
法。3. The resin solid content in the resol type phenolic resin liquid of the component (A) is 60 to 85% by weight.
Or the method for producing a fiber-reinforced phenolic resin molded article according to item 2.
合溶解する前のレゾール型フェノール樹脂液中の樹脂固
形分量が40〜80重量%である請求項1〜3のいずれ
かに記載の繊維強化フェノール樹脂成形物の製造方法。4. The fiber reinforced according to claim 1, wherein the component (B) has a resin solid content of 40 to 80% by weight in the resol type phenol resin solution before mixing and dissolving the resorcins. Method for producing phenolic resin molded product.
ィング成形法により、120〜200℃の温度で加熱硬
化させる請求項1〜4のいずれかに記載の繊維強化フェ
ノール樹脂成形物の製造方法。5. The method for producing a fiber-reinforced phenolic resin molded product according to claim 1, which is heat-cured at a temperature of 120 to 200 ° C. by a pultrusion molding method or a filament winding molding method.
よって得られた繊維強化フェノール樹脂成形物。6. A fiber-reinforced phenolic resin molded product obtained by the method according to claim 1.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012112043A1 (en) * | 2011-02-16 | 2012-08-23 | Trespa International B.V. | A method for reducing the formaldehyde content of a resinous starting material |
JP2017206611A (en) * | 2016-05-18 | 2017-11-24 | Dic株式会社 | Phenol resin composition and method for producing the same, and fiber-reinforced composite material |
-
2002
- 2002-05-29 JP JP2002155490A patent/JP2003342381A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012112043A1 (en) * | 2011-02-16 | 2012-08-23 | Trespa International B.V. | A method for reducing the formaldehyde content of a resinous starting material |
JP2017206611A (en) * | 2016-05-18 | 2017-11-24 | Dic株式会社 | Phenol resin composition and method for producing the same, and fiber-reinforced composite material |
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