JP2002187138A - Method for manufacturing norbornene polymer molding - Google Patents

Method for manufacturing norbornene polymer molding

Info

Publication number
JP2002187138A
JP2002187138A JP2000389138A JP2000389138A JP2002187138A JP 2002187138 A JP2002187138 A JP 2002187138A JP 2000389138 A JP2000389138 A JP 2000389138A JP 2000389138 A JP2000389138 A JP 2000389138A JP 2002187138 A JP2002187138 A JP 2002187138A
Authority
JP
Japan
Prior art keywords
mold
norbornene
molded article
temperature
resin composition
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
JP2000389138A
Other languages
Japanese (ja)
Inventor
Nobuhiro Goto
信弘 後藤
Masafumi Nakatani
政史 中谷
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP2000389138A priority Critical patent/JP2002187138A/en
Publication of JP2002187138A publication Critical patent/JP2002187138A/en
Pending legal-status Critical Current

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  • Moulds For Moulding Plastics Or The Like (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Moulding By Coating Moulds (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for manufacturing a norbornene polymer molding having excellent mold releasability and productivity. SOLUTION: The method for manufacturing the norbornene polymer molding comprises the steps of introducing a resin composition 3 containing a norbornene monomer and a polymerization catalyst, as main components to an air gap part formed of an outer mold 1 and inner molds 2 and 21 made of a material having smaller linear expansion coefficient than that of a norbornene polymer; polymerizing the composition, molding the composition to the molding; then removing the mold 1; and releasing the molds 2 and 21 in a state in which a temperature of the molding is higher than a polymerization temperature of the composition 3.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ノルボルネン系ポ
リマー成形体の製造方法に関する。
[0001] The present invention relates to a method for producing a norbornene-based polymer molded article.

【0002】[0002]

【従来の技術】従来より、中子等の内型を用いた繊維強
化プラスチック(FRP)成形体の製造方法は、パイプ
等の中空状成形品を製造する際に利用されており、中子
を割型にしたり、テーパーを設ける等の工夫により中子
を脱型し易くする工夫がされている。
2. Description of the Related Art Conventionally, a method of manufacturing a fiber-reinforced plastic (FRP) molded article using an inner mold such as a core has been used when manufacturing a hollow molded article such as a pipe. There is a device that makes it easier to remove the core by using a device such as a split mold or a taper.

【0003】上記FRP成形体に用いられる不飽和ポリ
エステル樹脂やエポキシ樹脂のような熱硬化性樹脂は、
反応による体積収縮が大きく、内型を締めつけたりヒケ
等の変形が生じて内型から抜け難くなるという問題があ
った。
A thermosetting resin such as an unsaturated polyester resin or an epoxy resin used for the above-mentioned FRP molded article is:
There was a problem that the volume shrinkage due to the reaction was large, and the inner mold was tightened or deformed, such as sink marks, making it difficult to remove from the inner mold.

【0004】また、フィラメントワインディング(F
W)成形では中子としてのマンドレルが使用されてい
る。FW成形の場合は成形材料に巻回による張力を与え
ることが多く、成形後の成形体に大きな残留応力が残っ
てマンドレルを締めつけるので容易に脱型できない。そ
のため、割型にしたりマンドレルにテーパー加工を施す
などの必要がある。しかし、割型にすると型が複雑な構
造となり、型の費用が高くなる。また、割型の場合に
は、樹脂が型の割れ目に巻き込まれて脱型し難くなると
いう問題も発生する。テーパー加工により抜き勾配を付
ける場合には、成形体には付けたくないテーパーを付け
ることになり、外観を損ねたり他の部品との接続等にお
ける性能上の問題が発生する場合がある。更に、脱型性
の面から成形体の曲部の曲率半径を小さくすることがで
きないという欠点もある。
Further, filament winding (F
W) In molding, a mandrel as a core is used. In the case of FW molding, a tension is often given to the molding material by winding, and a large residual stress remains in the molded body after molding, and the mandrel is tightened, so that the mold cannot be easily removed. Therefore, it is necessary to form a split mold or taper the mandrel. However, the split mold has a complicated structure, which increases the cost of the mold. In the case of the split mold, there is also a problem that the resin is caught in the cracks of the mold and it is difficult to remove the mold. In the case where a draft is formed by taper processing, a tapered shape which is not desired to be formed on a molded body is formed, which may impair the appearance or cause performance problems in connection with other parts. Further, there is a disadvantage that the radius of curvature of the curved portion of the molded product cannot be reduced from the viewpoint of the mold releasing property.

【0005】特開平5−104571号公報には、中子
に繊維を巻回した繊維予備成形体からマンドレルを抜き
取り、反応射出成形によりマトリックス樹脂を含浸させ
て成形体を得ることが記載されている。しかし、この場
合は巻回した繊維による張力及び樹脂の硬化収縮による
残留応力が中子に加わっているので、中子を成形体から
脱型するのは容易ではない。また、端面に樹脂が回り込
んだ場合には脱型がさらに困難となる。中子を埋め込み
型にすると中子の脱型の必要はなくなるが、中子の再利
用ができずコストアップとなり、成形の度に中子を製作
しなければならない。
Japanese Patent Application Laid-Open No. 5-104571 discloses that a mandrel is extracted from a fiber preform obtained by winding fibers around a core and is impregnated with a matrix resin by reaction injection molding to obtain a molded body. . However, in this case, since the tension caused by the wound fibers and the residual stress due to the curing shrinkage of the resin are applied to the core, it is not easy to remove the core from the molded body. In addition, when the resin comes around the end face, it is more difficult to remove the mold. If the core is made into an embedded type, the core does not need to be removed, but the core cannot be reused, which increases the cost, and the core must be manufactured each time it is formed.

【0006】[0006]

【発明が解決しようとする課題】本発明は、脱型性、生
産性に優れたノルボルネン系ポリマー成形体の製造方法
を提供することを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a norbornene-based polymer molded article having excellent demoldability and productivity.

【0007】[0007]

【課題を解決するための手段】本発明のノルボルネン系
ポリマー成形体の製造方法のひとつは、外型と、ノルボ
ルネン系ポリマーよりも線膨張率が小さい材質よりなる
内型とで形成される空隙部分に、ノルボルネン系モノマ
ー及び重合触媒を主成分とする樹脂組成物を導入し、重
合して成形体とした後、外型を外し、樹脂組成物の重合
温度よりも成形体の温度が高い状態で内型から脱型する
ことを特徴とする。
Means for Solving the Problems One of the methods for producing a norbornene-based polymer molded article of the present invention is to provide a method for producing a void portion formed by an outer mold and an inner mold made of a material having a smaller linear expansion coefficient than the norbornene-based polymer. Then, after introducing a resin composition containing a norbornene-based monomer and a polymerization catalyst as main components and polymerizing to form a molded body, the outer mold is removed, and the temperature of the molded body is higher than the polymerization temperature of the resin composition. It is characterized in that it is released from the inner mold.

【0008】また、本発明による他の製造方法は、ノル
ボルネン系モノマー及び重合触媒を主成分とする樹脂組
成物を含浸した強化材を成形型表面に積層あるいは巻回
した状態で重合して成形体とした後、樹脂組成物の重合
温度よりも成形体の温度が高い状態で成形型から脱型す
ることを特徴とする。
[0008] Another production method according to the present invention is a method for producing a molded product by polymerizing a reinforcing material impregnated with a resin composition containing a norbornene-based monomer and a polymerization catalyst as main components in a state of being laminated or wound on the surface of a molding die. After that, the molding is released from the molding die in a state where the temperature of the molding is higher than the polymerization temperature of the resin composition.

【0009】ノルボルネン系ポリマーは、ノルボルネン
系モノマーを重合触媒によってメタセシス重合させるこ
とによって得ることができ、耐衝撃性、耐熱性、耐薬品
性に優れたポリマーである。また、ノルボルネン系モノ
マーがメタセシス重合触媒により開環重合してポリマー
化するので、通常の熱硬化性樹脂を用いる場合と比べて
体積収縮が小さいために残留応力が残りにくく、内型を
締めつける力が小さいという特徴がある。
The norbornene-based polymer can be obtained by subjecting a norbornene-based monomer to metathesis polymerization using a polymerization catalyst, and is a polymer having excellent impact resistance, heat resistance, and chemical resistance. In addition, since the norbornene-based monomer is polymerized by ring-opening polymerization using a metathesis polymerization catalyst, residual stress is less likely to remain because the volume shrinkage is smaller than when a normal thermosetting resin is used. It has the characteristic of being small.

【0010】ノルボルネン系モノマーとしては、2−ノ
ルボルネン、ノルボルナジエンなどの二環体、ジシクロ
ペンタジエンやジヒドロジシクロペンタジエンなどの三
環体、テトラシクロドデセン、エチリデンテトラシクロ
ドデセン、フェニルテトラシクロドデセンなどの四環
体、トリシクロペンタジエンなどの五環体、テトラシク
ロペンタジエンなどの七環体、及びこれらのアルキル置
換体(例えば、メチル、エチル、プロピル、ブチル置換
体など)、アルキリデン置換体(例えば、エチリデン置
換体)、アリール置換体(例えば、フェニル、トリル置
換体)、エポキシ基、メタクリル基、水酸基、アミノ
基、カルボキシル基、シアノ基、ハロゲン基、エーテル
基、エステル結合含有基等の置換基を有する誘導体が挙
げられる。特に、ジシクロペンタジエンは反応性及びポ
リマー化したときの耐熱性等の物性のバランスが優れ、
耐衝撃性にも優れているので好ましい。これらは単独で
使用してもよく、2種以上を混合して使用してもよい。
Examples of the norbornene-based monomer include bicyclics such as 2-norbornene and norbornadiene, tricyclics such as dicyclopentadiene and dihydrodicyclopentadiene, tetracyclododecene, ethylidenetetracyclododecene, and phenyltetracyclododecene. Such as tetracyclic, pentacyclic such as tricyclopentadiene, heptacyclic such as tetracyclopentadiene, and their alkyl-substituted (eg, methyl, ethyl, propyl, butyl-substituted etc.), alkylidene-substituted (eg, , Ethylidene-substituted), aryl-substituted (for example, phenyl and tolyl-substituted), epoxy group, methacrylic group, hydroxyl group, amino group, carboxyl group, cyano group, halogen group, ether group and ester bond-containing group. And derivatives having the formula: In particular, dicyclopentadiene has an excellent balance of physical properties such as reactivity and heat resistance when polymerized,
It is preferable because it has excellent impact resistance. These may be used alone or in combination of two or more.

【0011】また、ノルボルネン系モノマーの1種以上
と共に、開環重合可能なシクロブテン、シクロペンテ
ン、シクロペンタジエン、シクロオクテン、シクロオク
タジエン、シクロドデセン、シクロドデカトリエンなど
の単環シクロオレフィン、あるいはインデン、クマロ
ン、クマロン−インデン系コモノマーのような環状モノ
マーなどを、本発明の目的を損なわない範囲で使用する
ことができる。また、テトラヒドロインデンのような架
橋し得る環状モノマーを併用してもよい。
A ring-opening polymerizable monocyclic cycloolefin such as cyclobutene, cyclopentene, cyclopentadiene, cyclooctene, cyclooctadiene, cyclododecene, cyclododecatriene, or indene, cumarone, or one or more of norbornene monomers. A cyclic monomer such as a coumarone-indene comonomer can be used as long as the object of the present invention is not impaired. A crosslinkable cyclic monomer such as tetrahydroindene may be used in combination.

【0012】ノルボルネン系モノマーの重合触媒として
は、メタセシス重合触媒が挙げられ、タングステン、モ
リブデン、タンタル、ルテニウム、レニウム、オスミウ
ム、チタンなどのハロゲン化物、オキシハロゲン化物、
酸化物、有機アンモニウム塩などが挙げられる。
Examples of the polymerization catalyst for the norbornene-based monomer include a metathesis polymerization catalyst, and include halides, oxyhalides, such as tungsten, molybdenum, tantalum, ruthenium, rhenium, osmium, and titanium.
Oxides, organic ammonium salts and the like.

【0013】重合触媒としては上記のものの他、空気や
水分に対して安定性に優れる以下のものが挙げられ、本
発明のように強化材と複合化したり、各種プロセスに適
用させる場合には有利である。具体的には下記一般式
〔I〕のルテニウムカルベン触媒や、一般式〔II〕に示
すルテニウムビニリデン触媒が好ましい。
As the polymerization catalyst, in addition to the above-mentioned ones, the following ones having excellent stability against air and moisture can be mentioned, and they are advantageous when they are combined with a reinforcing material or applied to various processes as in the present invention. It is. Specifically, a ruthenium carbene catalyst represented by the following general formula [I] and a ruthenium vinylidene catalyst represented by the following general formula [II] are preferable.

【0014】[0014]

【化3】 Embedded image

【0015】[0015]

【化4】 Embedded image

【0016】〔式中、R1 及びR2 は互いに独立に、水
素、C2〜C20−アルケニル、C1〜C20−アルキ
ル、アリール、C1〜C20−カルボキシレート、C1
〜C20−アルコキシ、C2〜C20−アルケニルオキ
シ、アリールオキシ、C2〜C20−アルコキシカルボ
ニル、C1〜C20−アルキルチオ、C1〜C20−ア
ルキルシリル、アリールシリル、チオアリール、チオア
ルキル(アルキル部分はC1〜C20)、オキシアリー
ル、オキシアルキル(アルキル部分はC1〜C20)
(これらは、C1〜C5−アルキル、ハロゲン、C1〜
C5−アルコキシによって、又は必要に応じてC1〜C
5−アルキル、ハロゲン、C1〜C5−アルコキシによ
って置換されたフェニルによって必要に応じて置換され
ていてもよい。)、フェロセン誘導体を意味し、X1
びX2 は互いに独立に、任意の所望のアニオン性配位子
を意味し、L1 及びL2 は互いに独立に、任意の所望の
中性電子供与体を意味し、そして、X1 、X2 、L1
びL2 の2個又は3個は、更に一緒に多座キレート化配
位子を形成してもよい。〕
Wherein R 1 and R 2 independently of one another are hydrogen, C2-C20-alkenyl, C1-C20-alkyl, aryl, C1-C20-carboxylate, C1
-C20-alkoxy, C2-C20-alkenyloxy, aryloxy, C2-C20-alkoxycarbonyl, C1-C20-alkylthio, C1-C20-alkylsilyl, arylsilyl, thioaryl, thioalkyl (alkyl portion is C1-C20), Oxyaryl, oxyalkyl (the alkyl part is C1 to C20)
(These are C1-C5-alkyl, halogen, C1-C5
By C5-alkoxy or optionally C1-C
It may be optionally substituted by 5-alkyl, halogen, phenyl substituted by C1-C5-alkoxy. ), A ferrocene derivative, X 1 and X 2 independently of one another and any desired anionic ligand, L 1 and L 2 independently of one another and any desired neutral electron donor And two or three of X 1 , X 2 , L 1 and L 2 may further form together a polydentate chelating ligand. ]

【0017】より好ましい触媒の構造は、一般式〔I〕
及び一般式〔II〕において、R1 及びR2 は互いに独立
に、水素、メチル、エチル、フェニル、フェロセニル、
又はメチル、エチル、フェロセニルによって必要に応じ
て置換されたビニルであり、X1 及びX2 は互いに独立
にCl、Brであり、L1 及びL2 は互いに独立に、ト
リメチルホスフィン、トリエチルホスフィン、トエフェ
ニルホスフィン、トリイソプロピルホスフィン又はトリ
シクロヘキシルホスフィンである。
A more preferred structure of the catalyst is represented by the general formula [I]
And in the general formula [II], R 1 and R 2 are each independently hydrogen, methyl, ethyl, phenyl, ferrocenyl,
Or vinyl optionally substituted by methyl, ethyl, ferrocenyl, X 1 and X 2 are each independently Cl, Br, and L 1 and L 2 are each independently trimethylphosphine, triethylphosphine, toluene. Phenylphosphine, triisopropylphosphine or tricyclohexylphosphine.

【0018】前記メタセシス触媒の添加量は触媒の活性
度によって異なるので一概には言えないが、全モノマー
に対して1/5〜1/500000モル当量であること
が好ましい。1/5当量よりも多いと得られるポリマー
の分子量が上がらず、1/500000当量よりも少な
いと重合速度が低くなるので好ましくない。更に好まし
い添加量としては、全モノマーに対して1/100〜1
/100000モル当量である。この範囲で必要なポッ
トライフ及び硬化時間を基に触媒の混合比率を設定すれ
ばよい。
Since the amount of the metathesis catalyst varies depending on the activity of the catalyst, it cannot be specified unconditionally, but is preferably 1/5 to 1 / 500,000 molar equivalents relative to all monomers. When the amount is more than 1/5 equivalent, the molecular weight of the obtained polymer does not increase, and when the amount is less than 1 / 500,000 equivalent, the polymerization rate is undesirably reduced. A more preferable addition amount is 1/100 to 1 with respect to all monomers.
/ 100,000 molar equivalents. The mixing ratio of the catalyst may be set based on the necessary pot life and curing time in this range.

【0019】上記ノルボルネン系モノマーには、必要に
応じて酸化防止剤、充填材、発泡剤、消泡剤、揺変性付
与剤、帯電防止剤、分子量調整剤、高分子改質剤、難燃
剤、可塑剤、顔料、染料、着色剤、表面処理剤、分散
剤、エラストマー等の種々の添加剤を配合することがで
きる。
The above norbornene-based monomers may include, if necessary, an antioxidant, a filler, a foaming agent, an antifoaming agent, a thixotropic agent, an antistatic agent, a molecular weight modifier, a polymer modifier, a flame retardant, Various additives such as a plasticizer, a pigment, a dye, a colorant, a surface treatment agent, a dispersant, and an elastomer can be blended.

【0020】充填材としては、炭酸カルシウム、水酸化
アルミニウム、炭酸マグネシウム、炭酸水素ナトリウ
ム、クレー、タルク、マイカ、カオリン、フライアッシ
ュ、モンモリロナイト、ガラスバルーン、シリカバルー
ン、熱膨張性塩化ビニリデン粒子等が挙げられる。
Examples of the filler include calcium carbonate, aluminum hydroxide, magnesium carbonate, sodium hydrogen carbonate, clay, talc, mica, kaolin, fly ash, montmorillonite, glass balloon, silica balloon, thermally expandable vinylidene chloride particles and the like. Can be

【0021】エラストマーとしては、天然ゴム、ポリブ
タジエン、ポリイソプレン、スチレン−ブタジエン−ス
チレンブロック共重合体、スチレン−イソプレン−スチ
レンブロック共重合体、EPDM、エチレン−酢酸ビニ
ル共重合体及びこれらの水素化物が挙げられる。
Examples of the elastomer include natural rubber, polybutadiene, polyisoprene, styrene-butadiene-styrene block copolymer, styrene-isoprene-styrene block copolymer, EPDM, ethylene-vinyl acetate copolymer and hydrides thereof. No.

【0022】ノルボルネン系ポリマーよりも線膨張率が
小さい材質としては、例えば、銅、ニッケル、アルミニ
ウム、鉄、ステンレス等が挙げられる。例えば、ジシク
ロペンタジエンを重合させて得られるポリジシクロペン
タジエンの線膨張率は8.5×10-5程度であり、内型
を線膨張率が3×10-5以下のものとすれば、成形体の
温度が高い状態で容易に脱型することができ、生産性を
向上させることができる。
Examples of the material having a lower linear expansion coefficient than the norbornene-based polymer include copper, nickel, aluminum, iron, and stainless steel. For example, if the linear expansion coefficient of polydicyclopentadiene obtained by polymerizing dicyclopentadiene is about 8.5 × 10 −5 and the inner die has a linear expansion coefficient of 3 × 10 −5 or less, molding The mold can be easily removed in a state where the body temperature is high, and the productivity can be improved.

【0023】又、内部に冷却配管を設けた内型を用い
て、脱型する際に冷却水を循環させて内型を冷却する
と、内型が収縮して脱型性をより高めることができるの
で好ましい。
Further, when the inner mold is cooled by circulating cooling water at the time of demolding by using an inner mold having a cooling pipe provided therein, the inner mold shrinks and the removability can be further improved. It is preferred.

【0024】請求項2の発明で用いる強化材としては、
ロービング、ロービングクロスあるいはチョップドスト
ランドマットのような連続繊維でもよく、チョップドス
トランド、ミルドファイバー等の長短繊維状のものでも
よい。繊維の種類としては、ガラス繊維、カーボン繊
維、金属繊維等の無機繊維、アラミド繊維、ナイロン繊
維、シュート繊維、ケナフ繊維、竹繊維、ポリエチレン
繊維、延伸ポリエチレン繊維、ポリプロピレン繊維、延
伸ポリプロピレン繊維等の有機繊維が挙げられる。
The reinforcing material used in the invention of claim 2 includes:
It may be a continuous fiber such as roving, roving cloth or chopped strand mat, or may be a long or short fiber such as chopped strand or milled fiber. Fiber types include inorganic fibers such as glass fiber, carbon fiber, and metal fiber, and organic fibers such as aramid fiber, nylon fiber, shoot fiber, kenaf fiber, bamboo fiber, polyethylene fiber, drawn polyethylene fiber, polypropylene fiber, and drawn polypropylene fiber. Fiber.

【0025】次に、請求項1記載のノルボルネン系ポリ
マー成形体の製造方法の一例を図面を参照しながら説明
する。図1乃至図3は配管用の分岐継ぎ手を製造する工
程を示したものである。図1に示す2分割可能な外型1
と、ノルボルネン系ポリマーよりも線膨張率が小さい内
型2との間に形成される空隙部にノルボルネン系モノマ
ー及び重合触媒よりなる樹脂組成物3を注入し、その状
態で樹脂組成物3を重合、硬化させることによりポリマ
ー成形体31が得られる。成形体31を脱型する際に
は、まず外型1を外して成形体31を外部の拘束から解
放し、成形体31の温度を樹脂組成物3の重合温度より
も高くすると、内型2と成形体31との線膨張率の差に
より、内型2と成形体31との間に隙間が発生して脱型
性が大幅に向上する。
Next, an example of a method for producing a norbornene-based polymer molded article according to claim 1 will be described with reference to the drawings. 1 to 3 show steps of manufacturing a branch joint for piping. An outer mold 1 that can be divided into two as shown in FIG.
And a resin composition 3 comprising a norbornene-based monomer and a polymerization catalyst are injected into a gap formed between the inner mold 2 having a smaller coefficient of linear expansion than the norbornene-based polymer, and the resin composition 3 is polymerized in that state. By curing, the polymer molded body 31 is obtained. When the molded body 31 is removed from the mold, the outer mold 1 is first released to release the molded body 31 from external restraint, and when the temperature of the molded body 31 is higher than the polymerization temperature of the resin composition 3, the inner mold 2 is removed. A gap is generated between the inner mold 2 and the molded body 31 due to the difference in the coefficient of linear expansion between the molded body 31 and the molded body 31, and the releasability is greatly improved.

【0026】樹脂組成物の重合温度は脱型時に比べ、で
きるだけ低い温度で行われるのが好ましい。これは、重
合・硬化の段階でポリマーの形状がほぼ固定され、その
後の脱型時の温度との温度差が大きくなり、内型と成形
体との線膨張量の差が大きくなってより脱型性が向上す
るからである。
The polymerization temperature of the resin composition is preferably as low as possible in comparison with the time of demolding. This is due to the fact that the shape of the polymer is almost fixed during the polymerization and curing stages, the temperature difference from the temperature during the subsequent demolding increases, and the difference in the amount of linear expansion between the inner mold and the molded body increases, resulting in more demolding. This is because the moldability is improved.

【0027】樹脂組成物を重合するときの温度と、脱型
する時の成形体との温度差は20℃以上であることが好
ましい。この温度差が20℃よりも小さいと脱型のため
の充分な空間が生じ難くなる。
The temperature difference between the temperature at which the resin composition is polymerized and the temperature at which the resin composition is removed from the molded product is preferably 20 ° C. or more. If this temperature difference is smaller than 20 ° C., it is difficult to create a sufficient space for demolding.

【0028】次に、請求項2記載の製造方法の一例を図
7、図8を参照しながら説明する。図7、8は浴槽を製
造する工程を示す断面図であり、成形型7表面にノルボ
ルネン系モノマー及び重合触媒を主成分とする樹脂組成
物を含浸した樹脂含浸繊維マット8を積層し、この状態
で重合させると繊維で補強されたノルボルネン系ポリマ
ーからなる浴槽81が得られる。浴槽81を脱型する際
には、浴槽81の温度を樹脂含浸繊維マット8の重合時
の温度よりも高い温度とする。これにより、成形型7と
浴槽81の線膨張量の差により両者の間に隙間が生じて
脱型する際の抵抗が非常に小さくなる。この場合の製造
方法では、浴槽や防水パンのような形状のものでコーナ
ー部の曲率半径を小さくしたり、抜きテーパーをなくす
ことが可能となり、浴室ユニットの嵌合部の水密性をよ
くすることが可能である。
Next, an example of the manufacturing method according to claim 2 will be described with reference to FIGS. FIGS. 7 and 8 are cross-sectional views showing steps of manufacturing a bathtub. A resin-impregnated fiber mat 8 impregnated with a resin composition containing a norbornene-based monomer and a polymerization catalyst as main components is laminated on the surface of a mold 7. Is obtained, a bath 81 made of a norbornene-based polymer reinforced with fibers is obtained. When removing the bathtub 81, the temperature of the bathtub 81 is set to a temperature higher than the temperature at the time of polymerization of the resin-impregnated fiber mat 8. Accordingly, a gap is formed between the molding die 7 and the bathtub 81 due to a difference in the amount of linear expansion therebetween, and the resistance when the mold is released is extremely small. In the manufacturing method in this case, it is possible to reduce the radius of curvature of the corner part and eliminate the taper with a shape like a bathtub or a waterproof pan, and to improve the watertightness of the fitting part of the bathroom unit. Is possible.

【0029】(作用)請求項1記載の発明では、ノルボ
ルネン系ポリマーよりも線膨張率が小さい内型を用い
て、外型と内型との間の空隙部分で硬化した成形体を脱
型する際に、まず、外型を外すことにより外部からの拘
束から解放し、成形体の温度を重合時の温度よりも高く
すると、成形体と内型との線膨張量が異なるので、この
間に隙間が生じて容易に脱型することができる。従っ
て、内型にテーパーを設けたり、割型にする必要がな
く、内型の構造を簡単なものとすることができる。ま
た、成形体のコーナー部における曲率を小さくすること
ができる。この方法では外型と内型とを用いるので、例
えば、射出成形、BMC等にも適用することができる。
(Function) According to the first aspect of the present invention, the molded body cured in the gap between the outer mold and the inner mold is released from the mold using the inner mold having a smaller linear expansion coefficient than the norbornene-based polymer. At this time, first, the outer mold is released to release the restraint from the outside, and if the temperature of the molded body is higher than the temperature at the time of polymerization, the linear expansion amount between the molded body and the inner mold is different. And the mold can be easily removed. Accordingly, there is no need to provide a taper or split mold for the inner mold, and the structure of the inner mold can be simplified. Further, the curvature at the corner of the molded body can be reduced. Since this method uses an outer mold and an inner mold, it can be applied to, for example, injection molding, BMC, and the like.

【0030】請求項2記載の発明では、ノルボルネン系
ポリマーよりも線膨張率が小さい成形型を用いるので、
成形型表面で硬化した成形体を脱型する際に、成形体の
温度を重合時の温度よりも高くすると、成形型と成形体
との線膨張量が異なるため、この間に隙間が生じて容易
に脱型することができる。また、成形型に大きなテーパ
ーを設けたりする必要がなく、成形体のコーナー部にお
ける曲率を小さくすることもできる。この方法による
と、外型を用いない成形方法に適用することができ、例
えば、FRPのハンドレイアップ成形、スプレーアップ
成形、FW成形等に用いることができる。
According to the second aspect of the present invention, since a mold having a smaller linear expansion coefficient than the norbornene-based polymer is used,
If the temperature of the molded body is higher than the temperature at the time of polymerization when the molded body cured on the mold surface is removed from the mold, the amount of linear expansion between the mold and the molded body is different, so a gap is created between the molds. Can be removed from the mold. Also, there is no need to provide a large taper in the molding die, and the curvature at the corners of the molded body can be reduced. According to this method, it can be applied to a molding method that does not use an outer mold. For example, it can be used for hand lay-up molding, spray-up molding, and FW molding of FRP.

【0031】[0031]

【発明の実施の形態】(実施例1)図4に示すように、
パイプ製造用の筒状の内型4(75mmφ×65cm,
テーパーなし,SUS)の外側に2つ割りの外型5(S
US)を組み合わせたものを用いた。内型4と外型5の
温度は25℃とした。40℃に加熱したジシクロペンタ
ジエン100重量部に対して、トルエン200重量部に
ビス(トリシクロヘキシルホスフィン)ベンジリデンル
テニウムジクロリド10重量部を溶解した溶液を、ビス
(トリシクロヘキシルホスフィン)ベンジリデンルテニ
ウムジクロリドのジシクロペンタジエンに対するモル比
が1/10000となるように添加し、混合して樹脂組
成物を作製した。上記樹脂組成物6を図4に示すよう
に、上記外型5と内型4とで形成された空隙部に充填
し、加熱炉(図示略)内で80℃で30分間加熱した
後、外型5のみ脱型した(図5)。更に80℃で10分
間加熱した後、直ちに内型4を脱型したところ、スムー
ズに脱型することができ、ノルボルネン系ポリマーより
なる図6に示すような内径75mmφ、長さ65cmの
パイプ61が得られた。
(Embodiment 1) As shown in FIG.
A cylindrical inner mold 4 for pipe production (75 mmφ × 65 cm,
Two outer molds 5 (S without taper, SUS)
US) was used. The temperature of the inner mold 4 and the outer mold 5 was 25 ° C. A solution prepared by dissolving 10 parts by weight of bis (tricyclohexylphosphine) benzylidene ruthenium dichloride in 200 parts by weight of toluene with respect to 100 parts by weight of dicyclopentadiene heated to 40 ° C. was treated with bis (tricyclohexylphosphine) benzylidene ruthenium dichloride dicyclopentadiene. It was added so that the molar ratio to pentadiene was 1/10000, and mixed to prepare a resin composition. As shown in FIG. 4, the resin composition 6 is filled in the space formed by the outer mold 5 and the inner mold 4 and heated at 80 ° C. for 30 minutes in a heating furnace (not shown). Only mold 5 was released (FIG. 5). After further heating at 80 ° C. for 10 minutes, the inner mold 4 was immediately removed from the mold. The inner mold 4 can be removed smoothly, and a pipe 61 made of norbornene-based polymer having an inner diameter of 75 mmφ and a length of 65 cm as shown in FIG. Obtained.

【0032】(実施例2)実施例1で用いた内型の内部
に冷却配管を配置したものと、実施例1で用いた外型と
を使用し、内型及び外型の温度は25℃とした。40℃
に加熱したジシクロペンタジエン100重量部に対し
て、トルエン200重量部に下記式〔III 〕のルテニウ
ムビニリデン錯体を10重量部溶解した溶液を、ルテニ
ウムビニリデン錯体のジシクロペンタジエンに対するモ
ル比が1/10000となるように添加、混合して樹脂
組成物を作製した。上記樹脂組成物を外型と内型とで形
成された空隙部に充填し、加熱炉内で80℃で30分間
加熱し、先ず外型のみ脱型した。更に80℃で10分間
加熱後、内型に5℃の冷却水を暫く通してから内型を脱
型したところ、スムーズに脱型することができ、実施例
1と同様のパイプを得た(図示略)。
(Embodiment 2) A cooling pipe was disposed inside the inner mold used in the first embodiment, and the outer mold used in the first embodiment was used. The temperature of the inner mold and the outer mold was 25 ° C. And 40 ℃
A solution prepared by dissolving 10 parts by weight of a ruthenium vinylidene complex represented by the following formula [III] in 200 parts by weight of toluene with respect to 100 parts by weight of dicyclopentadiene heated to a temperature of 1 / 10,000 was used. Was added and mixed so as to obtain a resin composition. The resin composition was filled in the voids formed by the outer mold and the inner mold, and heated at 80 ° C. for 30 minutes in a heating furnace. First, only the outer mold was removed. Further, after heating at 80 ° C. for 10 minutes, cooling water at 5 ° C. was passed through the inner mold for a while, and then the inner mold was released. As a result, it was possible to remove the mold smoothly, and a pipe similar to that of Example 1 was obtained ( Not shown).

【0033】[0033]

【化5】 Embedded image

【0034】(実施例3)温調配管を設けた1600m
mサイズの浴槽製造用の成形型7(ニッケル電鋳,立ち
面の抜き勾配1.5度,コーナー部の曲率は1mm)を
準備し、この成形型7の温度を25℃とした。実施例2
で作製した樹脂組成物を、#450のチョップドストラ
ンドマットに含浸させながら、樹脂含浸繊維マット8を
上記成形型7表面に積層した。これを80℃で30分間
加熱してから、成形型7に5℃の冷却水を暫く通した
後、成形体7から脱型したところスムーズに脱型するこ
とができ、ノルボルネン系ポリマーよりなる1600m
mサイズの浴槽81が得られた。
(Example 3) 1600 m provided with a temperature control pipe
A moulding mold 7 (nickel electroforming, draft angle of upright face 1.5 degrees, curvature of corner portion 1 mm) for preparing an m-size bathtub was prepared, and the temperature of this mold 7 was set to 25 ° C. Example 2
While impregnating the resin composition prepared in the above into a chopped strand mat of # 450, a resin-impregnated fiber mat 8 was laminated on the surface of the mold 7. After heating at 80 ° C. for 30 minutes, cooling water at 5 ° C. was passed through the mold 7 for a while, and then the mold was removed from the molded body 7.
An m-size bathtub 81 was obtained.

【0035】(比較例1)実施例1で空隙内に充填した
樹脂組成物を、加熱炉内で80℃で30分間加熱しただ
けで脱型を試みた。外型は2つ割りであるため脱型でき
たが、内型から脱型することはできなかった。
(Comparative Example 1) The demolding was attempted by simply heating the resin composition filled in the voids in Example 1 at 80 ° C for 30 minutes in a heating furnace. Since the outer mold was divided into two parts, it could be removed from the mold, but could not be removed from the inner mold.

【0036】(比較例2)1600mmサイズの浴槽製
造用の成形型(エポキシ樹脂製,立ち面の抜き勾配1.
5度,コーナー部の曲率は1mm)を準備し、この成形
型の温度を25℃とした。オルソ系不飽和ポリエステル
樹脂100重量部及び硬化剤としてメチルエチルケトン
パーオキサイド1重量部の混合物を#450のチョップ
ドストランドマットに含浸ローラーにて含浸させながら
成形型表面に積層した。これを80℃で1時間加熱して
から脱型しようとしたが、脱型することはできなかっ
た。
(Comparative Example 2) A molding die (made of epoxy resin, draft of a standing surface) for manufacturing a bathtub of 1600 mm size.
5 °, the curvature of the corner portion was 1 mm), and the temperature of the mold was 25 ° C. A mixture of 100 parts by weight of ortho-unsaturated polyester resin and 1 part by weight of methyl ethyl ketone peroxide as a curing agent was laminated on the surface of a mold while impregnating a # 450 chopped strand mat with an impregnating roller. This was heated at 80 ° C. for 1 hour and then tried to be released, but could not be released.

【0037】[0037]

【発明の効果】本発明によると、ノルボルネン系ポリマ
ーよりも線膨張率の小さい材質よりなる内型又は成形型
を使用し、樹脂組成物の重合温度よりも高い温度の状態
で内型あるいは成形型から脱型するので、抵抗なく成形
体を脱型することができる。また、内型や成形型を割型
にしたり、テーパーを設けるなどの必要がなく、成形体
の形状設計の自由度が向上する。また、脱型時の作業性
が大幅に向上するので生産性が高くなり、脱型時の製品
の損傷も低減することができる。更に、複数個の中子を
必要とする製品や多数個取りの製造も可能となる。
According to the present invention, an inner mold or a molding die made of a material having a smaller coefficient of linear expansion than a norbornene-based polymer is used, and the inner mold or the molding die is heated at a temperature higher than the polymerization temperature of the resin composition. Since the molded article is released from the mold, the molded article can be released without resistance. In addition, there is no need to split the inner mold or the forming die or to provide a taper, so that the degree of freedom in the shape design of the formed body is improved. Further, since the workability at the time of removing the mold is greatly improved, the productivity is increased, and the damage of the product at the time of removing the mold can be reduced. Further, it is possible to manufacture a product requiring a plurality of cores or a multi-cavity production.

【図面の簡単な説明】[Brief description of the drawings]

【図1】外型と内型との間の空隙に樹脂組成物を充填し
た状態を示す斜視図。
FIG. 1 is a perspective view showing a state in which a gap between an outer mold and an inner mold is filled with a resin composition.

【図2】図1の外型を外した状態を示す斜視図。FIG. 2 is a perspective view showing a state where an outer mold of FIG. 1 is removed.

【図3】図2の内型を脱型した成形体を示す斜視図。FIG. 3 is a perspective view showing a molded body from which the inner mold of FIG. 2 is removed.

【図4】外型と内型の間に樹脂含浸強化材を巻き付けた
状態を示す斜視図。
FIG. 4 is a perspective view showing a state in which a resin impregnated reinforcing material is wound between an outer mold and an inner mold.

【図5】図4の外型を外した状態を示す斜視図。FIG. 5 is a perspective view showing a state where the outer mold of FIG. 4 is removed.

【図6】図4の内型を脱型したパイプを示す斜視図。FIG. 6 is a perspective view showing a pipe from which the inner mold of FIG. 4 is removed.

【図7】浴槽製造用成形型表面に樹脂含浸繊維マットを
積層した状態を示す断面図。
FIG. 7 is a cross-sectional view showing a state in which a resin-impregnated fiber mat is laminated on the surface of a mold for producing a bathtub.

【図8】図6で成形された浴槽を成形型から脱型した状
態を示す断面図。
FIG. 8 is a cross-sectional view showing a state in which the bathtub formed in FIG. 6 is removed from a forming die.

【符号の説明】[Explanation of symbols]

1,5:外型 2,21,4:内型 3,6:樹脂組成物 7 :成形型 8 :樹脂含浸繊維マット 31:パイプ 61:成形体 81:浴槽 1,5: Outer mold 2,21,4: Inner mold 3,6: Resin composition 7: Mould 8: Resin impregnated fiber mat 31: Pipe 61: Molded body 81: Bath tub

───────────────────────────────────────────────────── 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 105:06 B29C 67/14 E Fターム(参考) 4F202 AA12 AJ11 AJ12 AR06 CA01 CB01 CN05 4F204 AA12 AD16 EA03 EA04 EB01 EB11 EF01 EF05 EK15 EK17 EK24 EK25 4F205 AA12 AB03 AD16 AG08 AG29 AJ11 HA02 HA03 HA14 HA25 HA33 HA45 HB01 HK04 HK05 HK08 HK32 HM02 4J032 CA34 CA38 CB01 CD02 CE06 CG07 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B29K 105: 06 B29C 67/14 EF term (Reference) 4F202 AA12 AJ11 AJ12 AR06 CA01 CB01 CN05 4F204 AA12 AD16 EA03 EA04 EB01 EB11 EF01 EF05 EK15 EK17 EK24 EK25 4F205 AA12 AB03 AD16 AG08 AG29 AJ11 HA02 HA03 HA14 HA25 HA33 HA45 HB01 HK04 HK05 HK08 HK32 HM02 4J032 CA34 CA38 CB01 CD02 CE06 CG07

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 外型と、ノルボルネン系ポリマーよりも
線膨張率が小さい材質よりなる内型とで形成される空隙
部分に、ノルボルネン系モノマー及び重合触媒を主成分
とする樹脂組成物を導入し、重合して成形体とした後、
外型を外し、樹脂組成物の重合温度よりも成形体の温度
が高い状態で内型から脱型することを特徴とするノルボ
ルネン系ポリマー成形体の製造方法。
1. A resin composition containing a norbornene-based monomer and a polymerization catalyst as main components is introduced into a void portion formed by an outer mold and an inner mold made of a material having a smaller coefficient of linear expansion than a norbornene-based polymer. After polymerization to form a molded body,
A method for producing a norbornene-based polymer molded article, comprising removing an outer mold and releasing the molded article from the inner mold in a state where the temperature of the molded article is higher than the polymerization temperature of the resin composition.
【請求項2】 ノルボルネン系モノマー及び重合触媒を
主成分とする樹脂組成物を含浸した強化材を成形型表面
に積層あるいは巻回した状態で重合して成形体とした
後、樹脂組成物の重合温度よりも成形体の温度が高い状
態で成形型から脱型することを特徴とするノルボルネン
系ポリマー成形体の製造方法。
2. A molding obtained by laminating or winding a reinforcing material impregnated with a resin composition containing a norbornene-based monomer and a polymerization catalyst as main components on a surface of a molding die to form a molded product, and then polymerizing the resin composition. A method for producing a norbornene-based polymer molded article, comprising releasing the molded article from the mold in a state where the temperature of the molded article is higher than the temperature.
【請求項3】 内型又は成形型を冷却しながら脱型する
ことを特徴とする請求項1又は2のいずれかに記載のノ
ルボルネン系ポリマー成形体の製造方法。
3. The method for producing a norbornene-based polymer molded article according to claim 1, wherein the inner mold or the mold is released while being cooled.
【請求項4】 ノルボルネン系モノマーがジシクロペン
タジエンであり、内型又は成形型の材質の線膨張率が3
×10-5以下であることを特徴とする請求項1乃至3の
いずれかに記載のノルボルネン系ポリマー成形体の製造
方法。
4. The norbornene-based monomer is dicyclopentadiene, and the material of the inner mold or the mold has a coefficient of linear expansion of 3
The method for producing a norbornene-based polymer molded article according to any one of claims 1 to 3, wherein the density is × 10 -5 or less.
【請求項5】 重合触媒が下記一般式〔I〕のルテニウ
ムカルベン錯体又は下記一般式〔II〕のルテニウムビニ
リデン錯体であることを特徴とする請求項1乃至4のい
ずれかに記載のノルボルネン系ポリマー成形体の製造方
法。 【化1】 【化2】
5. The norbornene-based polymer according to claim 1, wherein the polymerization catalyst is a ruthenium carbene complex represented by the following general formula [I] or a ruthenium vinylidene complex represented by the following general formula [II]: A method for producing a molded article. Embedded image Embedded image
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018192659A (en) * 2017-05-15 2018-12-06 住友ゴム工業株式会社 Rigid core for vulcanization molding of ring-shaped rubber member, demolding apparatus, demolding method and manufacturing method
CN110900907A (en) * 2019-11-29 2020-03-24 南京金三力高分子科技有限公司 Forming die and processing method of wire harness rubber protective sleeve

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018192659A (en) * 2017-05-15 2018-12-06 住友ゴム工業株式会社 Rigid core for vulcanization molding of ring-shaped rubber member, demolding apparatus, demolding method and manufacturing method
CN110900907A (en) * 2019-11-29 2020-03-24 南京金三力高分子科技有限公司 Forming die and processing method of wire harness rubber protective sleeve
CN110900907B (en) * 2019-11-29 2021-05-28 南京金三力高分子科技有限公司 Forming die and processing method of wire harness rubber protective sleeve

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