JP4554092B2 - Phenolic resin moldings and laminates - Google Patents
Phenolic resin moldings and laminates Download PDFInfo
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- JP4554092B2 JP4554092B2 JP2001007253A JP2001007253A JP4554092B2 JP 4554092 B2 JP4554092 B2 JP 4554092B2 JP 2001007253 A JP2001007253 A JP 2001007253A JP 2001007253 A JP2001007253 A JP 2001007253A JP 4554092 B2 JP4554092 B2 JP 4554092B2
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- resin
- polypropylene glycol
- modifier
- phenol
- cured resin
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- Compositions Of Macromolecular Compounds (AREA)
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Description
【0001】
【産業上の利用分野】
本発明はフェノール樹脂系成形材に関するものであつて、詳しくはレゾール系フェノール樹脂が使用され寸法安定性に優れたフェノール樹脂成形物とその成形方法に関するものである。
【0002】
【従来技術】
従来、フェノール樹脂は耐熱性、強靱性、硬度、電気絶縁性等の性能に優れるため、絶縁板、化粧板、成形部品、接着剤等の広い分野において使用されている。
【0003】
【発明が解決しようとする課題】
しかしながら、フェノール樹脂を使用した成形品はガラス等の無機質材料や金属等に比べて寸法安定性が劣るという欠点があり、これに起因する成型品のそり、ねじれ、クラック、接着部分の剥がれ等の欠陥が潜在的に残されていた。殊に他の素材と複合化されて使用された場合には前記の欠陥が顕著になるため改良が求められていた。
従来、寸法変化を低減する一方法として無機質充填材を多量に配合するなどの手段があるが、成型品の強度を低下させる難点があり、他の方法による改良が求められていた。
【0004】
【課題を解決するための手段】
本発明では、前記のような課題を解決すべく鋭意検討してなされた結果、フェノール樹脂にある種の変性剤を配合することにより、寸法安定性の改良ばかりか、成型材の色調を薄くするとともに経時的な色調変化を低減できる効果まで得られることが判明した。
【0005】
この様な特性を実現できる可能性のある変性剤について幅広く検討を進めた結果、水酸基を持つアルキレンオキサイド誘導体をレゾール系フェノール樹脂に変性剤として配合することにより、配合した樹脂組成物の状態では溶解していて、硬化が進行するとともに樹脂から分離し、かつ硬化物中に均一に分散した構造を形成する変性剤が、この様な効果をもたらすことが確認され、本発明に至ったものである。
該アルキレンオキサイド誘導体として例示すると、ポリエチレングリコール、ポリプロピレングリコール、ポリブチレングリコール、ポリエチレングリコールグリセリルエーテル、ポリプロピレングリコールグリセリルエーテル等がある。
また、該アルキレンオキサイド誘導体には分子内に重合性を持つ化合物をレゾール系フェノール樹脂に添加して硬化過程において重合せしめ、高分子量化することにより相分離、均一分散させることも可能である。
これらの例として、例えば、ポリエチレングリコールモノ(メタ)アクリレート、ポリプロピレングリコールモノ(メタ)アクリレート等のポリアルキレングリコール(メタ)アクリレートやポリエチレングリコールアリルエーテル、ポリプロピレングリコールアリルエーテル等のアリル化ポリエーテルが使用できる。
【0006】
レゾール系フェノール樹脂の硬化過程において分離、分散する化合物としては疎水性で分子量が高いほど相分離しやすい。しかしながらある段階以上に疎水性及び分子量が高くなるとレゾール系フェノール樹脂溶液に不溶となつたり、硬化過程で分離するものの均一な分散状態とならず液状で滲み出したりする場合がある。
これらの現象はフェノールとホルムアルデヒドの反応比率、反応触媒、例えばアルキルフェノール、アミノ化合物等の共縮合する化合物、添加される可塑剤等の変性剤及び成形条件により異なってくるため、レゾール系フェノール樹脂の性質、特性に応じてアルキレンオキサイド誘導体の種類、分子量並びに添加量を調整、選定する必要がある。
【0007】
本発明の目的を実現するためには樹脂液の状態においては樹脂と変性剤が溶解した状態であつて、硬化した樹脂中では変性剤が分離し、均一に分散していることが必要である。硬化した樹脂中に均一に溶け合った状態では目的を達することができない。
本発明では硬化した樹脂中に変性剤が分離し、分散しているかどうかの判定として、硬化した時点で透明均一状態であるか、乳白濁状態であるか、変性剤が滲み出しているかどうかにより判断できる。透明均一状態であれば樹脂と変性剤が均一に溶け合って硬化していると判断され、乳白濁状であれば分離、分散している状態と判断される。また変性剤が滲み出している場合は硬化樹脂中に均一に分散せずに分離していると判断される。
【0008】
本発明におけるホルムアルデヒド/フェノールとのモル比は1〜3が望ましく、フェノール樹脂固形分に対する変性剤の添加率は5〜80%が適合する。
添加率が5%以下では十分に分離、分散状態が得れず目的を達することができない。80%以上ではフェノール樹脂の持つ強靱性、耐熱性等が損なわれるため好ましくない。
変性剤は反応当初に配合してもよいが、フェノールとホルムアルデヒドとの初期縮合物が合成されたのち、配合しても構わない。
また、フェノール樹脂は単独でも使用可能であるが、アルキルフェノール類、アミノ化合物等との共縮合物やパラトルエンスルホンアミド、カプロラクタム等を添加した変性樹脂にも応用可能である。
【0009】
本発明に係わる成形品として積層板の例について説明すると、この様にして調製した樹脂素材をガラス繊維、セルロース繊維、合成繊維等の繊維類から加工された紙、不織布、シート、織布等の基材に含浸させた含浸シートを複数枚積層し、熱圧成型されて積層板に仕上げられる。また、積層板表面に化粧層を張り合わせたり、塗装等を施して仕上げられても良い。
あるいは、この様に調製された含浸シートの上に、他の樹脂含浸シート、例えば化粧紙にメラミン樹脂、不飽和ポリエステル樹脂等の樹脂を含浸せしめたものを重ねて成型してしたり、各種の化粧シートを積層するなどして、化粧仕上げ積層板として仕上げることもできる。
【0010】
実施例
レゾール系フェノール樹脂の合成
攪拌装置、温度計、冷却コンデンサーを装備したフラスコにフェノール1モル、47%ホルマリン水溶液1.3モル(ホルムアルデヒド換算)を仕込み、水酸化ナトリウムによりPH8.0に調整した。反応液を昇温し95℃に反応液を保持して、反応液の白濁開始温度が40℃となるまで反応した。そのあと冷却してメタノールを添加して希釈し、固形分50%のレゾール型フェノール樹脂(以下樹脂Aという)を得た。
【0011】
実施例1
実施例により得られた樹脂Aの100重量部(以下単に部という)に対して平均分子量4000、水酸基価26(KOHmg/g)のポリプロピレングリコール20部、メタノール20部を添加した樹脂組成物▲1▼を得た。
樹脂組成物▲1▼を140℃の熱板上に滴下し硬化した樹脂固形物は均一な乳白濁状の褐色であって、ポリプロピレングリコールの滲みだしはなかった。
【0012】
実施例2
実施例で得た樹脂A、100部に対して平均分子量1500、水酸基価39(KOHmg/g)のポリプロピレングリコールモノアリルエーテル20部、ラジカル重合開始剤としてtーブチルパーオキシ−2−エチルヘキサノエート0.75部、メタノール20部を添加した透明褐色の樹脂組成物▲2▼を得た。
樹脂組成物▲2▼を140℃の熱板上に滴下し、硬化した樹脂固形物は均一な乳白濁状の褐色であって、ポリプロピレングリコールモノアリルエーテルの滲みだしはなかった。
【0013】
比較例1
実施例により得られた樹脂Aを、そのまま比較例1とした。比較例1の樹脂を140℃の熱板上に滴下し、硬化した樹脂固形物は均一な透明渇色であった。
【0014】
比較例2
実施例にて得られた樹脂A、100部に対して平均分子量400、水酸基価279(KOHmg/g)のポリプロピレングリコール20部、メタノール20部添加した透明褐色の比較例2の樹脂組成物▲3▼を得た。樹脂組成物▲3▼を140℃の熱板上に滴下し硬化した樹脂固形物は均一な透明渇色であって、滲みだしはなかった。
【0015】
上記の実施例、比較例の各樹脂組成物を使用して下記に従って成形物を成形した。
( 配合 )
樹脂A及び▲1▼〜▲3▼組成物 100重量部
炭酸カルシウム 200重量部
この配合物をメタノールで希釈して含浸塗工用スラリーを得た。
該スラリーを坪量75g/m2、密度0.15g/m3のガラス繊維不織布に含浸塗工したのち、乾燥して坪量900g/m2の積層用プリプレグシートを得た。
当プリプレグシートを7枚積層し、150℃、9.8MPa(100kg/cm2)において30分成形し、厚さ3mmの積層板を得た。積層板の寸法変化率及び色調変化の度合いを表1に示す。
【0016】
【表1】
( 測定方法 )
* 寸法変化率 JISK 6902に準じ、伸び+縮みの合計として表す。
(伸び) 40±2℃ 、相対湿度90〜95%の恒温恒湿装置中に96時間放置して測定。
(縮み) 70±2℃の恒温乾燥機に24時間放置して測定。
* 色差 成形した成形品及び40±2℃、相対湿度90〜95%の恒温恒湿装置中に96時間放置した成形品のLabを分光測色計にて測定し、ハンター色差式に基づき色差ΔEを求める。
* 耐煮沸性 JISK6902に準じる。 50mm角の試験片を2時間煮沸したのち、試験片の層間剥離、充填材の脱落がないかどうかを判定する。
* 曲げ強度 JISK 6902に準ずる。
* 曲げ弾性率 JISK 6902に準ずる。
【0017】
本発明になる成形物は硬化したフェノール樹脂中に変性剤が分離し、分散した状態を形成しているため、環境変化により引き起こされるフェノール樹脂層の収縮、膨張の応力が全体に波及することがない。
このため寸法安定性が大幅に改善される。従って本発明に係わる成形物、例えば積層板が他の基材例えばモルタル下地等に接着剤で一体に接合された場合、環境変化に基づく積層板の寸法変化より引き起こされる接着層の剥離、基材の反り並びにクラックの発生が少なくなるなどの効果が得られる。このため各種の基材等との複合化した場合において度々問題となる剥離、そり、クラック等の問題がなくなり安心して利用できる。
また、電気絶縁材等の成形材料として使用されれば、寸法安定性の改善、狂い等の問題がなく品質向上を図ることができる。
更に、フェノール樹脂の周囲に変性剤が分離、分散した構造であるため色差のブレが少なくなり外観も改善される。[0001]
[Industrial application fields]
The present invention relates to a phenolic resin-based molding material, and more particularly to a phenolic resin molding using a resol-based phenolic resin and excellent in dimensional stability and a molding method thereof.
[0002]
[Prior art]
Conventionally, phenolic resins are excellent in performance such as heat resistance, toughness, hardness, and electrical insulation, and are therefore used in a wide range of fields such as insulating plates, decorative plates, molded parts, and adhesives.
[0003]
[Problems to be solved by the invention]
However, molded products using phenolic resin have the disadvantage that the dimensional stability is inferior compared to inorganic materials such as glass and metals, etc., resulting in molding warping, twisting, cracking, peeling of the adhesive part, etc. Defects were potentially left behind. In particular, when the composite material is used in combination with other materials, the above-mentioned defects become prominent, and improvement has been demanded.
Conventionally, there is means such as blending a large amount of an inorganic filler as one method for reducing the dimensional change, but there is a difficulty in reducing the strength of the molded product, and improvement by other methods has been demanded.
[0004]
[Means for Solving the Problems]
In the present invention, as a result of intensive studies to solve the above-mentioned problems, by adding a certain modifier to the phenol resin, not only the dimensional stability is improved, but the color tone of the molding material is reduced. At the same time, it has been found that the effect of reducing the change in color tone over time can be obtained.
[0005]
As a result of a wide range of investigations on modifiers that may be able to achieve these characteristics, by incorporating an alkylene oxide derivative having a hydroxyl group into a resole phenolic resin as a modifier, it dissolves in the state of the blended resin composition. Thus, it has been confirmed that a modifier that forms a structure that is separated from the resin and that is uniformly dispersed in the cured product as the curing proceeds, has led to the present invention. .
Examples of the alkylene oxide derivative include polyethylene glycol, polypropylene glycol, polybutylene glycol, polyethylene glycol glyceryl ether, and polypropylene glycol glyceryl ether.
Further, the alkylene oxide derivative can be phase-separated and uniformly dispersed by adding a compound having polymerizability in the molecule to the resol phenol resin, polymerizing it in the curing process, and increasing the molecular weight.
Examples of these include polyalkylene glycol (meth) acrylates such as polyethylene glycol mono (meth) acrylate and polypropylene glycol mono (meth) acrylate, and allylated polyethers such as polyethylene glycol allyl ether and polypropylene glycol allyl ether. .
[0006]
As the compound which is separated and dispersed in the curing process of the resole phenolic resin, the higher the molecular weight is, the easier it is to separate the phases. However, if the hydrophobicity and molecular weight are higher than a certain level, they may become insoluble in the resol-based phenol resin solution, or may be separated in the curing process but may not be uniformly dispersed but may ooze out in liquid form.
These phenomena vary depending on the reaction ratio of phenol and formaldehyde, reaction catalysts such as co-condensing compounds such as alkylphenols and amino compounds, modifiers such as added plasticizers, and molding conditions. Depending on the characteristics, it is necessary to adjust and select the type, molecular weight and addition amount of the alkylene oxide derivative.
[0007]
In order to realize the object of the present invention, it is necessary that the resin and the modifier are dissolved in the resin liquid state, and that the modifier is separated and uniformly dispersed in the cured resin. . The objective cannot be achieved if the resin is uniformly dissolved in the cured resin.
In the present invention, whether or not the modifier is separated and dispersed in the cured resin depends on whether it is in a transparent uniform state, a milky turbid state, or if the modifier is exuded at the time of curing. I can judge. If it is in a transparent and uniform state, it is determined that the resin and the modifier are uniformly dissolved and cured. If it is milky, it is determined that the resin and the modifier are separated and dispersed. When the modifier is exuded, it is determined that the modifier is separated without being uniformly dispersed in the cured resin.
[0008]
In the present invention, the molar ratio of formaldehyde / phenol is preferably 1 to 3, and the addition ratio of the modifier to the phenol resin solid content is 5 to 80%.
If the addition rate is 5% or less, the separation and dispersion state cannot be obtained sufficiently and the purpose cannot be achieved. If it is 80% or more, the toughness, heat resistance, etc. of the phenol resin are impaired, which is not preferable.
The modifier may be blended at the beginning of the reaction, but it may be blended after the initial condensate of phenol and formaldehyde is synthesized.
In addition, the phenol resin can be used alone, but can also be applied to a modified resin to which a cocondensate with an alkylphenol, an amino compound or the like, paratoluenesulfonamide, caprolactam, or the like is added.
[0009]
An example of a laminate as a molded article according to the present invention will be described. Papers, nonwoven fabrics, sheets, woven fabrics, etc., which are obtained by processing the resin material thus prepared from fibers such as glass fibers, cellulose fibers, and synthetic fibers. A plurality of impregnated sheets impregnated into a base material are laminated, and hot-press molded to finish a laminated plate. Moreover, it may be finished by pasting a decorative layer on the surface of the laminated plate or by applying a coating or the like.
Alternatively, on the impregnated sheet prepared in this manner, another resin-impregnated sheet such as decorative paper impregnated with a resin such as a melamine resin or an unsaturated polyester resin can be molded, It can also be finished as a decorative laminate by laminating decorative sheets.
[0010]
Example Synthesis of resol phenolic resin A flask equipped with a stirrer, thermometer, and cooling condenser was charged with 1 mol of phenol and 1.3 mol of a 47% formalin aqueous solution (in terms of formaldehyde), and adjusted to pH 8.0 with sodium hydroxide. . The temperature of the reaction solution was raised and the reaction solution was maintained at 95 ° C., and the reaction was continued until the cloudiness start temperature of the reaction solution reached 40 ° C. Thereafter, the mixture was cooled and diluted with methanol to obtain a resol type phenol resin (hereinafter referred to as Resin A) having a solid content of 50%.
[0011]
Example 1
Resin composition in which 20 parts of polypropylene glycol having an average molecular weight of 4000 and a hydroxyl value of 26 (KOHmg / g) and 20 parts of methanol are added to 100 parts by weight (hereinafter referred to simply as “parts”) of Resin A obtained in Examples 1 I got ▼.
The resin solid material obtained by dripping the resin composition (1) on a hot plate at 140 ° C. and curing was a uniform milky brown color, and there was no bleeding of polypropylene glycol.
[0012]
Example 2
100 parts of the resin A obtained in the examples, 20 parts of polypropylene glycol monoallyl ether having an average molecular weight of 1500 and a hydroxyl value of 39 (KOHmg / g), and t-butylperoxy-2-ethylhexano as a radical polymerization initiator A transparent brown resin composition (2) to which 0.75 parts of ate and 20 parts of methanol were added was obtained.
The resin composition (2) was dropped on a hot plate at 140 ° C., and the cured resin solid was a uniform milky brown color, and there was no bleeding of polypropylene glycol monoallyl ether.
[0013]
Comparative Example 1
Resin A obtained in the examples was used as Comparative Example 1 as it was. The resin of Comparative Example 1 was dropped on a hot plate at 140 ° C., and the cured resin solid had a uniform transparent dull color.
[0014]
Comparative Example 2
Transparent brown resin composition of Comparative Example 2 in which 20 parts of polypropylene glycol having an average molecular weight of 400 and a hydroxyl value of 279 (KOHmg / g) and 20 parts of methanol were added to 100 parts of the resin A obtained in the examples (3) I got ▼. The resin solid material obtained by dripping the resin composition (3) on a hot plate at 140 ° C. and curing was uniform and transparent, and there was no bleeding.
[0015]
A molded product was molded according to the following using each of the resin compositions of the above Examples and Comparative Examples.
(Composition)
Resin A and (1) to (3) Composition 100 parts by weight Calcium carbonate 200 parts by weight This blend was diluted with methanol to obtain a slurry for impregnation coating.
The slurry was impregnated and coated on a glass fiber nonwoven fabric having a basis weight of 75 g / m 2 and a density of 0.15 g / m 3 and then dried to obtain a prepreg sheet for lamination having a basis weight of 900 g / m 2.
Seven prepreg sheets were laminated and molded at 150 ° C. and 9.8 MPa (100 kg / cm 2) for 30 minutes to obtain a laminated plate having a thickness of 3 mm. Table 1 shows the rate of dimensional change and the degree of color tone change of the laminate.
[0016]
[Table 1]
( Measuring method )
* Dimensional change rate Expressed as the sum of elongation + shrinkage in accordance with JISK 6902.
(Elongation) Measured by leaving it in a constant temperature and humidity apparatus of 40 ± 2 ° C. and a relative humidity of 90 to 95% for 96 hours.
(Shrinkage) Measured by leaving in a constant temperature dryer at 70 ± 2 ° C. for 24 hours.
* Color difference The Lab of the molded product and the molded product left for 96 hours in a constant temperature and humidity device with a temperature of 40 ± 2 ° C and relative humidity of 90 to 95% was measured with a spectrocolorimeter, and the color difference ΔE based on the Hunter color difference equation. Ask for.
* Boiling resistance Conforms to JISK6902. After boiling a test piece of 50 mm square for 2 hours, it is determined whether there is no delamination of the test piece or dropping of the filler.
* Bending strength Conforms to JISK 6902.
* Flexural modulus According to JISK 6902.
[0017]
In the molded product according to the present invention, since the modifier is separated and dispersed in the cured phenol resin, the shrinkage and expansion stress of the phenol resin layer caused by the environmental change may be spread over the whole. Absent.
For this reason, dimensional stability is greatly improved. Therefore, when the molded product according to the present invention, for example, a laminate is integrally bonded to another substrate such as a mortar substrate with an adhesive, peeling of the adhesive layer caused by a change in the size of the laminate due to environmental changes, the substrate Such effects as less warpage and occurrence of cracks can be obtained. For this reason, problems such as peeling, warping and cracks, which are often problematic when combined with various base materials, are eliminated and can be used safely.
Further, if used as a molding material such as an electrical insulating material, it is possible to improve quality without problems such as improvement in dimensional stability and deviation.
Furthermore, since the modifier is separated and dispersed around the phenol resin, the color difference blur is reduced and the appearance is improved.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001007253A JP4554092B2 (en) | 2001-01-16 | 2001-01-16 | Phenolic resin moldings and laminates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001007253A JP4554092B2 (en) | 2001-01-16 | 2001-01-16 | Phenolic resin moldings and laminates |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002212308A JP2002212308A (en) | 2002-07-31 |
| JP4554092B2 true JP4554092B2 (en) | 2010-09-29 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001007253A Expired - Fee Related JP4554092B2 (en) | 2001-01-16 | 2001-01-16 | Phenolic resin moldings and laminates |
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| Country | Link |
|---|---|
| JP (1) | JP4554092B2 (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5521415A (en) * | 1978-07-28 | 1980-02-15 | Matsushita Electric Works Ltd | Thermosetting resin molding compound |
| JPS55151019A (en) * | 1979-05-12 | 1980-11-25 | Matsushita Electric Works Ltd | Production of plasticization-modified phenolic resin |
| JPS55164215A (en) * | 1979-06-08 | 1980-12-20 | Matsushita Electric Works Ltd | Preparation of plasticized phenolic resin |
| JPS58113244A (en) * | 1981-12-26 | 1983-07-06 | Sumitomo Bakelite Co Ltd | Thermosetting resin aqueous emulsion |
-
2001
- 2001-01-16 JP JP2001007253A patent/JP4554092B2/en not_active Expired - Fee Related
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| Publication number | Publication date |
|---|---|
| JP2002212308A (en) | 2002-07-31 |
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