JPH06218830A - Manufacture of composite molded piece - Google Patents

Manufacture of composite molded piece

Info

Publication number
JPH06218830A
JPH06218830A JP5010785A JP1078593A JPH06218830A JP H06218830 A JPH06218830 A JP H06218830A JP 5010785 A JP5010785 A JP 5010785A JP 1078593 A JP1078593 A JP 1078593A JP H06218830 A JPH06218830 A JP H06218830A
Authority
JP
Japan
Prior art keywords
mold
resin
temperature
mixture
core
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
JP5010785A
Other languages
Japanese (ja)
Inventor
Yasuhiko Kuriyama
康彦 栗山
Hiromitsu Takamoto
裕光 高本
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP5010785A priority Critical patent/JPH06218830A/en
Publication of JPH06218830A publication Critical patent/JPH06218830A/en
Pending legal-status Critical Current

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  • Molding Of Porous Articles (AREA)

Abstract

PURPOSE:To shorten a molding cycle and obtain excellent quality by a method wherein a surface layer molding material is arranged in a mold, a mixture of foaming resin and liquid molding resin system is supplied to a part of foaming core by mixing them immediately before the supply of it, the foaming resin is foamed by heating after the mold is closed and the surface layer molding material is pushed to the inner wall of the mold so as to cure. CONSTITUTION:A surface layer molding material is arranged in a forming mold and a mixture of foaming resin and liquid molding resin system is supplied to a part which is to be a foaming core. At this time, the component which reacts due to the mixing is mixed immediately before the mixture is supplied to the mold. That is, the one is led to a dynamic mixing part 5 equipped with a spindle 1 from a supplying opening 3 of the device and the other is led from a supplying opening 4, which are led to a microwave irradiation part 2 by an exhaust-pipe 6 and heated by microwave coming from a microwave generator 7. The temperature is set to be above room temperature and below the temperature where cubic expansion occurs in the foaming resin particle. After the mold is closed, the foaming resin in the core is foamed by heating, the surface layer molding material is pushed to the inner wall of the mold so as to cure.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は複合成形品の製造方法に
関するものである。更に詳しくは、(i)繊維状補強材
を含有する樹脂層よりなる表層部、及び(ii)発泡した
樹脂を含有する軽量なコア部(芯部)からなる、一体化
された軽量でかつ強靭な複合成形品を効率的に製造する
方法に関するものである。
FIELD OF THE INVENTION The present invention relates to a method for producing a composite molded article. More specifically, an integrated, lightweight and tough body including (i) a surface layer portion made of a resin layer containing a fibrous reinforcing material, and (ii) a lightweight core portion (core portion) containing a foamed resin. The present invention relates to a method for efficiently producing various composite molded articles.

【0002】[0002]

【従来の技術】芯部に発泡コアを有するFRP(繊維強
化樹脂)複合成形品は、軽量性と強靭性に優れているた
め、スポーツ用品、自動車・電車・航空機・船舶など輸
送機器の構造材、内外装部材、医療機器、通信機器の構
造材やハウジングなど極めて広い用途がある。
2. Description of the Related Art FRP (fiber reinforced resin) composite molded products having a foam core in the core are excellent in lightness and toughness, and are therefore structural materials for transportation equipment such as sports equipment, automobiles, trains, aircraft and ships. It has an extremely wide range of uses such as interior and exterior members, medical equipment, and structural materials and housings for communication equipment.

【0003】芯部に発泡コアを有するFRP複合成形品
の製造法としては、例えば芯部に発泡コアを予め成形
し、これを補強材としての織布で包んだ後、あらためて
型に挿入し、液状成形樹脂システムを注入して外殻を形
成する方法(特開昭55―82612号、特開昭61―
279517号参照)、あるいは外殻のFRPを予め成
形しておき、その中心部の空隙内に発泡性ウレタン樹脂
等を注入して空隙内で発泡させる方法等が知られてい
る。
As a method for producing an FRP composite molded article having a foam core in the core, for example, a foam core is preformed in the core, wrapped with a woven cloth as a reinforcing material, and then inserted into a mold again. A method for forming an outer shell by injecting a liquid molding resin system (JP-A-55-82612, JP-A-61-61)
No. 279517), or FRP of the outer shell is preformed, and a foaming urethane resin or the like is injected into the void at the center of the FRP to foam in the void.

【0004】しかしながら、上記の技術はいずれも、複
合成形品を得るための工程が多岐にわたり、操作が繁雑
であり、そのため成形品の生産効率が低くコスト高にな
るという欠点を有している。これに対して、特開平3―
183511号、特開平3―180329号、特開平3
―45315号、特開平3―288629号、特開平4
―27532号等に提案された発泡性樹脂と液状成形樹
脂システムを使用し、発泡コアと繊維状補強材を含有す
る樹脂層よりなる表層部とを同時に成形する方法は上記
の欠点を改善したものである。
However, each of the above-mentioned techniques has a drawback that the steps for obtaining the composite molded product are various and the operation is complicated, so that the production efficiency of the molded product is low and the cost is high. On the other hand, JP-A-3-
183511, JP-A-3-180329, JP-A-3
-45315, JP-A-3-288629, JP-A-4
-The method of simultaneously molding a foam core and a surface layer portion made of a resin layer containing a fibrous reinforcing material by using a foamable resin and a liquid molding resin system proposed in No. 27532 and the like is an improvement of the above-mentioned drawbacks. Is.

【0005】[0005]

【発明が解決しようとする課題】しかし、この成形法に
おいても、より一層の生産効率を高めることは非常に重
要である。それ故、本発明の目的は、発泡性樹脂と液状
成形樹脂システムとを使用する上記の複合成形品を製造
する方法において、生産効率を高めるために成形サイク
ルを短縮する方法を提供しようとすることにある。
However, even in this molding method, it is very important to further improve the production efficiency. Therefore, an object of the present invention is to provide a method for shortening a molding cycle in order to increase production efficiency in a method for producing the above-mentioned composite molded article using a foamable resin and a liquid molding resin system. It is in.

【0006】[0006]

【課題を解決するための手段】本発明は、少なくとも液
状成形樹脂システムにより所定の形状に成形された繊維
強化樹脂層からなる表層部及び発泡コアからなる芯部を
有する複合成形品を製造するに当たり、(a)成形用の
型内に、表層部成形用の材料を設置すること、(b)型
内の成形後の発泡コアとなる部分に、少なくとも発泡性
樹脂及び液状成形樹脂システムを含む混合物を供給し、
かつ、その際、少なくとも液状成形樹脂とその硬化剤の
ような混合により反応する成分は型に供給する直前に混
合し、該混合物を室温以上でかつ発泡性樹脂粒子が体積
膨張を生じる以下の温度にマイクロ波によって加熱した
後、型内へ供給すること、(c)型を閉じた後、型の所
定領域を十分高い温度まで加熱すること及び/又は上記
液状成形樹脂システムの反応熱による温度上昇により、
コア部に位置する発泡性樹脂を加熱発泡させて体積膨張
を生じさせ、これにより表層部形成用の材料を型の内壁
面に対して押し付けること、(d)その状態で液状成形
樹脂システムを硬化させること、そして、(e)得られ
た複合成形品を型から取り出すこと、を特徴とするもの
で、特に、上記(b)工程において、型内の成形後の発
泡コアとなる部分に、発泡性樹脂と液状成形樹脂システ
ムを含む混合物を供給する際、少なくとも液状成形樹脂
システムを構成する成分のうち液状成形樹脂とその硬化
剤のように混合により反応する成分は型に供給する直前
に混合すること、そして上記混合物を室温以上で発泡性
樹脂が体積膨張を生じる以下の温度にマイクロ波を使っ
て迅速に加熱して、型に供給することを最大の特徴とす
るものである。
DISCLOSURE OF THE INVENTION The present invention is directed to the production of a composite molded article having at least a surface layer portion made of a fiber reinforced resin layer molded into a predetermined shape by a liquid molding resin system and a core portion made of a foam core. , (A) placing a material for molding a surface layer in a molding die, and (b) a mixture containing at least a foaming resin and a liquid molding resin system in a portion which becomes a foamed core after molding in the mold. Supply
And, at that time, at least the components which react by mixing such as the liquid molding resin and the curing agent thereof are mixed immediately before being supplied to the mold, and the mixture is kept at room temperature or higher and at a temperature below which the expandable resin particles cause volume expansion. After heating by microwave to the mold, (c) after closing the mold, heating a predetermined region of the mold to a sufficiently high temperature and / or increasing the temperature by the reaction heat of the liquid molding resin system. Due to
The foamable resin located in the core part is heated and foamed to cause volume expansion, thereby pressing the material for forming the surface layer part against the inner wall surface of the mold, and (d) curing the liquid molding resin system in that state. And (e) removing the obtained composite molded article from the mold. In particular, in the above step (b), the foamed core is formed on the portion to be the foamed core after molding in the mold. When a mixture containing a polymerizable resin and a liquid molding resin system is supplied, at least components of the liquid molding resin system that react by mixing, such as the liquid molding resin and its curing agent, are mixed immediately before being supplied to the mold. The most feature is that the mixture is rapidly heated to a temperature below the temperature at which the foamable resin causes volume expansion at room temperature or higher by using microwaves and supplied to the mold.

【0007】本発明方法では、まず成形用の型を用意す
る。この型は成形温度に応じ、金型、木型、樹脂型等の
うちから適宜選択して使用される。この型内、すなわち
この型のキャビティ内壁面に沿って表層部を構成する補
強繊維材料及び/又は分離層を一層又は複数層設置す
る。
In the method of the present invention, first, a molding die is prepared. This mold is appropriately selected and used from a mold, a wooden mold, a resin mold and the like according to the molding temperature. In the mold, that is, along the inner wall surface of the cavity of the mold, one or more layers of the reinforcing fiber material and / or the separation layer forming the surface layer portion are provided.

【0008】ここで分離層としては、熱膨張後の発泡性
樹脂を実質的に通さず液状成形樹脂システムは通す分離
機能を有する部分が少なくともその一部又は全部を構成
し、残りは液状成形樹脂システムをも通さない材料から
なるものを用いる。
Here, as the separating layer, at least a part or all of the separating layer, which has a separating function to allow the liquid molding resin system to pass substantially without passing the expandable resin after thermal expansion, and the rest is the liquid molding resin. Use a material that does not pass through the system.

【0009】かかる分離層の分離機能を発現し得るもの
として、例えば目開きの小さい繊維シート及び/又は多
孔質シートがあげられる。分離層用の繊維シートとして
は、各種天然繊維、合成繊維、無機繊維等の織布、編
物、組物、不織布、紙等が用いられ、多孔質シートとし
ては連通気孔を有するシート又はフイルムであって、ポ
リウレタン、ポリスチレンあるいはポリプロピレン等の
フォームシートや延伸、抽出又は凝固法などでつくるポ
リエチレン、ポリプロピレンあるいはポリスルホン等の
多孔膜が用いられる。その目開きは、発泡性樹脂の種類
や発泡性に応じて、これらが通過しない範囲のものが選
択される。この分離層として、それ自体補強材としての
機能を有するガラス繊維、炭素繊維、アラミド繊維等の
目開きの小さいシートを用いることもできる。この場合
は、分離層自体が表層部の補強材を兼ねる。また、この
分離層として容易に成形品の形状にあわせうるように伸
縮性を有する材料を選択することもできる。
As a material capable of exhibiting the separating function of the separating layer, for example, a fiber sheet and / or a porous sheet having a small opening can be mentioned. As the fibrous sheet for the separation layer, woven fabric, knitted fabric, braid, non-woven fabric, paper or the like of various natural fibers, synthetic fibers, inorganic fibers or the like is used, and the porous sheet is a sheet or film having continuous ventilation holes. For example, a foam sheet of polyurethane, polystyrene, polypropylene or the like, or a porous membrane of polyethylene, polypropylene, polysulfone or the like produced by a stretching, extraction or coagulation method is used. The openings are selected in a range that does not allow them to pass, depending on the type of the expandable resin and the expandability. As the separation layer, a sheet having a small opening such as glass fiber, carbon fiber or aramid fiber, which itself has a function as a reinforcing material, can be used. In this case, the separation layer itself also serves as a reinforcing material for the surface layer portion. Further, a material having elasticity can be selected as the separation layer so that it can be easily matched with the shape of the molded product.

【0010】分離層として、一部が液状成形樹脂システ
ムを通さない材料で構成されたものを用いてもよい。例
えば、分離機能を有する材料からなる部分とその部分で
用いている材料とは異なった材料とをつなぎあわせる以
外に、分離機能を有する繊維シート及び/又は多孔質シ
ートの一部を予め樹脂でその目開きを封止処理したも
の、繊維シートがポリプロピレン繊維など加熱処理によ
り融着させうる場合は融着処理により一部の目開きをつ
ぶしたもの、一部にフイルム等を貼り付けたものなどが
ある。
As the separation layer, a layer partially made of a material that does not pass through the liquid molding resin system may be used. For example, in addition to joining a part made of a material having a separating function and a material different from the material used in the part, a part of the fiber sheet and / or the porous sheet having a separating function is previously made of a resin. If the openings are sealed, if the fibrous sheet can be fused by heat treatment such as polypropylene fiber, then some of the openings are crushed by the fusion treatment, or some of which the film or the like is attached. is there.

【0011】上記の分離層の代わりにあるいは分離層と
重ねて、分離機能の乏しい目開きの大きい補強用の繊維
シートやプリフォームを併用してもよい。この場合は、
補強用繊維シートやプリフォームの目開きは自由に選択
でき、例えば一方向繊維配列プリプレグや三次元織物/
編物のプリフォームも使用でき、分離層を用いない場合
は、これらが表層部成形材料となる。分離層と目開きの
大きい補強用の繊維シートやプリフォームとを重ねて用
いる場合は、分離層がコア側に位置するように配するの
が好ましい。
Instead of the above-mentioned separation layer or in addition to the separation layer, a reinforcing fiber sheet or preform having a poor separation function and having a large opening may be used together. in this case,
The openings of the reinforcing fiber sheet or preform can be freely selected, for example, unidirectional fiber array prepreg or three-dimensional fabric /
Knit preforms can also be used, and when the separation layer is not used, these become the surface layer molding material. When the separating layer and the reinforcing fiber sheet or preform having a large opening are overlapped and used, it is preferable to arrange the separating layer so as to be located on the core side.

【0012】また、分離層及び/又は上記の如き補強用
の繊維シートやプリフォーム等は予めプリプレグの形で
樹脂処理しておくことも可能である。
The separating layer and / or the reinforcing fibrous sheet or preform as described above may be treated with a resin in the form of a prepreg in advance.

【0013】本発明方法では、上記のように、例えば分
離層等の表層部形成材料を型のキャビティ内壁面に沿っ
て設置し、次にその型内における発泡コアが形成される
べき部分(通常は表層部形成材料に囲まれる部分)に、
発泡性樹脂と液状成形樹脂システムと、必要に応じて後
述の第三成分とを入れる。上記各成分は、供給する際に
あらかじめ混合物としておく場合と供給直前に混合する
場合があるが、少なくとも液状成形樹脂システムを構成
する樹脂と硬化剤とは、供給直前に混合する。
In the method of the present invention, as described above, for example, a surface layer forming material such as a separation layer is placed along the inner wall surface of the cavity of the mold, and then the portion in the mold where the foam core is to be formed (usually) Is a part surrounded by the surface layer forming material),
A foamable resin, a liquid molding resin system, and optionally a third component described below are added. Each of the above components may be previously mixed as a mixture at the time of supply or may be mixed immediately before the supply. At least the resin and the curing agent constituting the liquid molding resin system are mixed immediately before the supply.

【0014】本発明の方法で用いる発泡性樹脂として
は、加熱により体積が少なくとも2倍、好ましくは3〜
6倍、更に好ましくは6倍以上に増大するものであり、
使用する成形用の液状樹脂システムには溶解しないもの
である。また該樹脂は発泡空間部に液状樹脂が入らない
よう発泡が独立気泡となるものが用いられる。
The foamable resin used in the method of the present invention has a volume of at least twice when heated, preferably 3 to.
6 times, more preferably 6 times or more,
It does not dissolve in the molding liquid resin system used. Further, as the resin, one in which the foam is closed cells is used so that the liquid resin does not enter the foam space.

【0015】かかる発泡性樹脂としては、例えば、ポリ
ウレタン、フェノール、ポリウレア、メラミン、ポリイ
ミド等の硬化型フォームやその前駆体、ポリ塩化ビニ
ル、ポリ塩化ビニリデン、ポリアクリルニトリル、ポリ
スチレン、ポリエチレン、ポリプロピレン、PPO、ポ
リアミド、ポリカーボネート、PBT、ポリイミド等の
熱可塑性樹脂が挙げられる。
Examples of the foamable resin include curable foams such as polyurethane, phenol, polyurea, melamine and polyimide, precursors thereof, polyvinyl chloride, polyvinylidene chloride, polyacrylonitrile, polystyrene, polyethylene, polypropylene and PPO. Thermoplastic resins such as polyamide, polycarbonate, PBT, and polyimide.

【0016】かかる発泡性樹脂の発泡は、発泡剤分解
法、溶剤気散法、化学反応法、気体混入法等いずれの方
法も適用できる。この中で発泡剤分解法や溶剤気散法が
好ましく用いられる。
For the foaming of the foamable resin, any method such as a foaming agent decomposition method, a solvent vaporization method, a chemical reaction method and a gas mixing method can be applied. Of these, the foaming agent decomposition method and the solvent vaporization method are preferably used.

【0017】発泡性樹脂として特に好ましいものは、
「マイクロスフェアー」、「エクスパンセル」、「エス
レンビーズ」等の商品名で知られる熱膨張性又は発泡性
の物質を内包する粒径約10μm〜1mm程度の熱膨張性
樹脂粒子である。かかる樹脂粒子の例は先に挙げた特開
平4―27532号公報に詳しく記載されている。
Particularly preferred as the foamable resin is
It is a heat-expandable resin particle having a particle diameter of about 10 μm to 1 mm, which contains a heat-expandable or foamable substance known by trade names such as “Microsphere”, “Expancel”, and “Ethren beads”. Examples of such resin particles are described in detail in the above-mentioned JP-A-4-27532.

【0018】一方、液状成形樹脂システムとしては、エ
ポキシ樹脂、不飽和ポリエステル樹脂、ビニルエステル
樹脂、硬化性ジシクロペンタジエン樹脂、非発泡性ウレ
タン樹脂等一般によく知られている液状成形樹脂システ
ムが好ましく用いられ、これらは、多くの場合、液状成
形樹脂と硬化剤との組合せからなる。
On the other hand, as the liquid molding resin system, generally well known liquid molding resin systems such as epoxy resin, unsaturated polyester resin, vinyl ester resin, curable dicyclopentadiene resin, non-foaming urethane resin are preferably used. However, they often consist of a combination of a liquid molding resin and a curing agent.

【0019】発泡性樹脂と液状成形樹脂システムとの混
合物には、上記二成分以外にさらに第三成分としてシリ
カバルーン、シラスバルーンのような非膨張性の無機中
空粒子を混入してもよい。これらの無機中空粒子は、分
離層を基本的に通過しないものが用いられ、平均粒径約
1μm〜約1mmのものが好ましい。
In addition to the above two components, non-expandable inorganic hollow particles such as silica balloons and shirasu balloons may be mixed in the mixture of the foamable resin and the liquid molding resin system. As these inorganic hollow particles, those which do not basically pass through the separation layer are used, and those having an average particle size of about 1 μm to about 1 mm are preferable.

【0020】また、成形品の強度を上げるため、更に炭
素繊維、アラミド繊維や、シリコーンカーバイド、チタ
ン酸カリ、ボロン等の短繊維やウィスカーなども加える
ことができ、また、必要に応じ顔料等を添加することも
できる。いずれにせよ、各成分を成形後の発泡コア部の
密度が0.8g/cm3 以下となるように配合するのが適
当である。
Further, in order to increase the strength of the molded product, carbon fibers, aramid fibers, short fibers such as silicone carbide, potassium titanate and boron, whiskers and the like can be added, and if necessary, pigments and the like can be added. It can also be added. In any case, it is appropriate to mix the components so that the density of the foamed core portion after molding is 0.8 g / cm 3 or less.

【0021】更に、回収再利用を考慮してFRP成形品
の破砕物を添加することもできる。この場合は発泡コア
部の密度が0.8g/cm3 以上になっても経済効果次第
で利用価値のある場合がある。
Further, a crushed product of the FRP molded product can be added in consideration of recovery and reuse. In this case, even if the density of the foamed core is 0.8 g / cm 3 or more, it may be useful depending on the economic effect.

【0022】型内に上記混合物を供給する量は、発泡性
樹脂の配合率、加熱時の体積膨張率を考慮して、適宜選
択すべきであり、先に挙げた特開平4―27532号公
報に詳しく記載されている。
The amount of the above mixture to be supplied into the mold should be appropriately selected in consideration of the compounding ratio of the foamable resin and the volume expansion coefficient during heating, and the above-mentioned JP-A-4-27532. Are described in detail in.

【0023】本発明方法では、上記混合物を、室温以上
でかつ発泡性樹脂が体積膨張を生じる以下の温度に予熱
して型内へ供給する。成形サイクルの上では予熱温度は
高い方が好ましいが、あまりに高い温度では供給してい
る間に発泡性樹脂の体積膨張が始まり、型を閉じる時点
では溢れだす場合があり、溢れ出すことが成形操作に支
障となっては不都合である。
In the method of the present invention, the above mixture is preheated to a temperature not lower than room temperature and not higher than the temperature at which the expandable resin causes volume expansion, and is supplied into the mold. A higher preheating temperature is preferable in the molding cycle, but if the temperature is too high, the volumetric expansion of the expandable resin may start and overflow may occur when the mold is closed. It is inconvenient if it interferes with.

【0024】この際、先に述べた如く、液状成形樹脂シ
ステムのうち、液状成形樹脂とその硬化剤、又はウレタ
ン樹脂システムのような場合イソシアネートとポリオー
ルのように混合により反応を開始するものを、供給直前
まで混合しないでおくことは有効である。
At this time, as described above, among the liquid molding resin systems, the liquid molding resin and its curing agent, or in the case of the urethane resin system, the one that starts the reaction by mixing like isocyanate and polyol, It is effective not to mix until just before supply.

【0025】このため、本発明方法では、少なくとも液
状成形樹脂システムを構成する成分のうち混合により反
応を開始する成分(例えば液状成形樹脂とその硬化剤)
は、型へ供給する直前に混合し、混合直後に、マイクロ
波を用いて急速加熱することにより、混合物を所定温度
まで予熱して型に供給する。例えば、微粒子状の発泡性
樹脂と液状成形樹脂とのスラリー状混合物を調製し、型
への供給直前にこの混合物に硬化剤を加えた後、マイク
ロ波を用いて所定温度まで迅速に加熱する方法が採用さ
れる。
Therefore, in the method of the present invention, at least components constituting the liquid molding resin system that start the reaction upon mixing (for example, the liquid molding resin and its curing agent).
Is mixed immediately before being supplied to the mold, and immediately after mixing, is rapidly heated by using a microwave to preheat the mixture to a predetermined temperature and then is supplied to the mold. For example, a method in which a slurry-like mixture of fine-particle foaming resin and liquid molding resin is prepared, a curing agent is added to this mixture immediately before being supplied to a mold, and then the mixture is rapidly heated to a predetermined temperature by using a microwave. Is adopted.

【0026】図1は、発泡性樹脂と液状成形樹脂システ
ムとを混合し、加熱する装置の1例を示すもので、液状
成形樹脂システムのうち少なくとも樹脂と硬化剤とは分
けて、2液を調製し、一方を装置の供給口3から、他方
を別の供給口4から、それぞれスピンドル1を備えたダ
イナミック混合部5へ導入し、ここで均一に混合された
後、その下流部に並設したマイクロ波照射部2へ排出管
6により導かれてマイクロ波発振部7からのマイクロ波
で直接に所定温度まで加熱される。
FIG. 1 shows an example of an apparatus for mixing a foaming resin and a liquid molding resin system and heating the mixture. In the liquid molding resin system, at least the resin and the curing agent are separated into two liquids. After being prepared, one is introduced from a supply port 3 of the apparatus and the other is introduced from another supply port 4 into a dynamic mixing section 5 equipped with a spindle 1, respectively, and after being uniformly mixed therein, they are arranged side by side in the downstream section. It is guided to the microwave irradiation unit 2 by the discharge pipe 6 and is heated directly to a predetermined temperature by the microwave from the microwave oscillation unit 7.

【0027】混合物は、供給時点の量が体積基準で出来
上がった複合成形品の体積の40%以上95%以下であ
ることが望ましい。40%未満の場合は混合物の持ち込
む熱量及び反応により生じる発熱量が不十分になりやす
く、かつ型の所定領域からの伝熱も少なく、さらに体積
膨張により置換する必要のある気層部の占める割合が大
きく、出来上がった成形品にボイドが多くなる傾向があ
る。更に極端な場合は、成形品の下型に面した側で樹脂
含浸不良がみられる。95%を超える場合は発泡性樹脂
粒子の体積膨張の余地が少なく、出来上がった成形品の
芯部の軽量化が充分でない場合がみられる。
It is desirable that the amount of the mixture at the time of supply is 40% or more and 95% or less of the volume of the completed composite molded article on a volume basis. If it is less than 40%, the amount of heat brought into the mixture and the amount of heat generated by the reaction tend to be insufficient, and the heat transfer from a predetermined region of the mold is small, and the proportion of the gas layer portion that needs to be replaced by volume expansion is occupied. Is large, and voids tend to increase in the finished molded product. In a more extreme case, defective resin impregnation is observed on the side of the molded product facing the lower mold. If it exceeds 95%, there is little room for volume expansion of the expandable resin particles, and there are cases where the weight reduction of the core of the finished molded product is not sufficient.

【0028】一般に、ここで述べたような、少なくとも
発泡性樹脂、液状成形樹脂システムからなる混合物を調
製する場合、空気や窒素などの非凝縮性ガスが多く含ま
れ易い。これらの非凝縮性ガスは液状成形樹脂システム
に随伴して分離層及び/又はその他の表層部形成材料に
浸透し、その一部は該材料を通り抜け成形品の表面層を
形成するため、特に成形サイクルを短縮する場合、この
過程も早くなるので、ガスが取り残されて成形品中や表
層部にボイドとして残りやすい。成形品中や表層面のボ
イドこれを防ぐためには混合物の調製時に混合物中にで
きるだけ非凝縮性ガスが含まれないよう配慮するか、あ
るいは型に供給する前に混合物を一時的に減圧下に置く
などして脱気した後、型に供給することが望ましい。
Generally, when preparing a mixture of at least a foamable resin and a liquid molding resin system as described above, a large amount of non-condensable gas such as air or nitrogen is likely to be contained. These non-condensable gases permeate the separation molding layer and / or other surface layer forming materials together with the liquid molding resin system, and a part of them penetrates through the material to form the surface layer of the molded article, so that it is particularly preferable for molding. When the cycle is shortened, this process is also accelerated, so that the gas is left behind and tends to remain as a void in the molded product or the surface layer portion. Voids in molded parts and surface layers To prevent this, make sure that the mixture contains as little non-condensable gas as possible when preparing the mixture, or temporarily put the mixture under reduced pressure before feeding it to the mold. It is desirable to supply air to the mold after degassing by, for example.

【0029】型内のコアを形成すべき部分へ供給された
混合物は、液状成形樹脂システムの反応が始まり、この
反応熱による発熱又はこれと型の所定領域からの伝熱と
により十分高い温度まで加熱されることで、液状成形樹
脂システムが流動性を保っている状態で発泡性樹脂の膨
張が起こる。
The mixture supplied to the portion of the mold where the core is to be formed is heated to a sufficiently high temperature due to the reaction of the liquid molding resin system, heat generated by the reaction, or heat transfer from a predetermined region of the mold. The heating causes expansion of the foamable resin while the liquid molding resin system maintains fluidity.

【0030】発泡性樹脂の膨張圧力で分離層及び/又は
その他の表面形成材料が型の内壁面に押し付けられ、該
内壁面に沿った外形を形成させると同時に、液状成形樹
脂システムが分離層及び/又はその他の表層部形成材料
に浸透し、その一部は該材料を通り抜け、成形品の表面
層を形成する。樹脂の過剰分は型の貯り部分に集める
か、ベントから抜き出される。
The expansion pressure of the expandable resin causes the separation layer and / or other surface forming material to be pressed against the inner wall surface of the mold to form an outer contour along the inner wall surface, while the liquid molding resin system forms the separation layer and It penetrates into the other surface layer forming material, and a part of it penetrates the material to form the surface layer of the molded article. Excess resin is either collected in the mold reservoir or withdrawn from the vent.

【0031】かくして、同時並行的に液状成形樹脂シス
テムの硬化が進み、充分硬化した段階で、型を開いて、
得られた発泡コアを含む複合成形品を型から取り出す。
Thus, the curing of the liquid molding resin system progresses in parallel at the same time, and at the stage of sufficient curing, the mold is opened,
The composite molded article containing the obtained foam core is taken out of the mold.

【0032】成形品が適当に冷えていない場合、得られ
た複合成形品を型から取り出す際に変形することがあ
り、これを防ぐために、型の所定領域を液状成形樹脂シ
ステムの熱変形温度以下に下げてから型から取り出す必
要がある。
If the molded product is not properly cooled, it may be deformed when the resulting composite molded product is taken out of the mold. In order to prevent this, a predetermined region of the mold is kept below the heat deformation temperature of the liquid molding resin system. It is necessary to lower it to and remove it from the mold.

【0033】成形サイクル中にこの型の所定領域の温度
を上げ下げする操作は極力少なくすることが好ましく、
本発明方法では、発泡性樹脂、液状成形樹脂システムの
混合物をマイクロ波加熱する温度条件を選ぶことによ
り、液状成形樹脂システムの反応熱による発熱だけで型
の所定領域の温度を一定にして成形することができる。
It is preferable to minimize the operation of raising and lowering the temperature of the predetermined region of the mold during the molding cycle.
In the method of the present invention, the temperature of a predetermined region of the mold is kept constant only by the heat generated by the reaction heat of the liquid molding resin system by selecting the temperature condition for microwave heating the mixture of the foaming resin and the liquid molding resin system. be able to.

【0034】上述の如く、本発明の方法は、成形後の発
泡コアとなる部分に、少なくとも発泡性樹脂、液状成形
樹脂システムを含む混合物を供給する条件をできるだけ
厳密に管理することで効率的に成形を進める手段とし
て、(イ)型内へ供給する混合物を構成する液状成形樹
脂システムのうち、液状成形樹脂とその硬化剤、又はウ
レタン樹脂システムのような場合イソシアネートとポリ
オールのように混合により反応を開始するものを、供給
直前まで混合しないでおき、型へ供給する直前の段階で
混合すること、(ロ)混合物を型への供給直前にマイク
ロ波を使って室温以上でかつ発泡性樹脂が体積膨張を生
じる以下の温度に急速に加熱して型に供給すること、を
実施する点を主な特徴としている。これらによって、成
形に要する時間を大幅に短縮することができるばかりで
なく、良好な品質の複合成形品が効率的に製造される。
As described above, the method of the present invention is efficiently controlled by strictly controlling the conditions for supplying the mixture containing at least the foamable resin and the liquid molding resin system to the portion to be the foamed core after molding. (A) As a means of promoting molding, among liquid molding resin systems that make up the mixture to be fed into the mold, liquid molding resins and their curing agents, or in the case of urethane resin systems, react by mixing like isocyanate and polyol What is started is left unmixed until just before feeding, and mixed at the stage immediately before feeding to the mold. (B) Using a microwave just before feeding the mixture to the mold at room temperature or above The main feature is that the material is rapidly heated to the following temperature at which volume expansion occurs and is supplied to the mold. By these, not only the time required for molding can be greatly shortened, but also a good quality composite molded product can be efficiently produced.

【0035】[0035]

【発明の効果】以上の如く、本発明方法では、大幅な成
形サイクリの短縮を達成することができ、しかも、良好
な品質の複合成形品が得られるので、工業的に極めて有
用である。
As described above, according to the method of the present invention, the molding cycle can be greatly shortened, and a composite molded article of good quality can be obtained, which is industrially very useful.

【0036】本発明方法により得られる複合成形品は軽
量で強靭なため、例えばカヌーパドル、マスト、方向
舵、ウインドサーフィン安定用フィン(スケグ)、人力
水中翼挺、スキー(板、ポール)、ホッケースティッ
ク、野球用バット、スポークのない車輪、自転車のフレ
ーム、スケートボードなどのスポーツ用品分野、自動車
(乗用車、バス、トラック)などの外板用材料、スポイ
ラー、ドライブシャフト、内外装品、鉄道車輌のドアや
構造部材などの車両分野、熱交換器の鏡板、エアコン・
コンプレッサーブレード、攪拌翼、電気絶縁材サポート
ビーム、フィッティング類などの産業分野、車椅子(ハ
イドリム、側パネル)、X線投影用テーブル、義手・義
足などの医療器具分野、及びプロペラ、座席、家具、コ
ントロールサーフェス、二次構造材、衛生放送用アンテ
ナのリフレクタなどの広い分野に有効である。
Since the composite molded article obtained by the method of the present invention is lightweight and tough, for example, canoe paddles, masts, rudders, windsurfing fins (skegs), human hydrofoil, skis (boards, poles), hockey sticks. , Baseball bats, non-spoke wheels, bicycle frames, skateboards and other sporting goods fields, automobile (passenger cars, buses, trucks) and other outer skin materials, spoilers, drive shafts, interior and exterior products, railroad vehicle doors Fields such as automobiles and structural members, end plates of heat exchangers, air conditioners,
Industrial fields such as compressor blades, stirring blades, electrical insulation support beams, fittings, wheelchairs (hydrim, side panels), X-ray projection tables, medical equipment fields such as artificial hands and artificial legs, and propellers, seats, furniture, controls It is effective in a wide range of fields such as surfaces, secondary structural materials, and reflectors for satellite broadcasting antennas.

【0037】[0037]

【実施例】以下、本発明を実施例により詳細に説明する
が、これらは本発明を説明するためのものであって、こ
れらの実施例により本発明が限定されるものではない。
なお、例中の「部」は特にことわりのない限り重量部を
表わす。
EXAMPLES The present invention will now be described in detail with reference to examples, but these are for explaining the present invention and the present invention is not limited to these examples.
In addition, "part" in an example represents a weight part unless there is particular notice.

【0038】[0038]

【実施例1】液状成形樹脂システムとして、エポキシ樹
脂を準備した。すなわち、油化シェル社製の「エピコー
ト828」とイソホロンジアミン(硬化剤「エピキュア
T」)である。
Example 1 An epoxy resin was prepared as a liquid molding resin system. That is, “Epicoat 828” and isophoronediamine (curing agent “Epicure T”) manufactured by Yuka Shell Co., Ltd.

【0039】補強繊維材料として、ガラスマット(旭フ
ァイバークラス社製8609―300)を入手した。そ
の目付けは約300g/m2 である。また、分離層とし
てユニセル社製のポリエステルを主とした不織布「ユニ
セルBT605W」を入手した。
A glass mat (8609-300 manufactured by Asahi Fiber Class Co., Ltd.) was obtained as a reinforcing fiber material. The basis weight is about 300 g / m 2 . In addition, a non-woven fabric "UNICEL BT605W" mainly made of polyester manufactured by Unicell was obtained as a separation layer.

【0040】発泡性樹脂として松本油脂製薬社製の「マ
ツモトマイクロスフェアーF―82D」を入手した。こ
れは105℃で発泡膨張する樹脂粒子である。更に第三
成分として旭硝子社製「シリカバルーンQ―CEL」を
入手した。
As the expandable resin, "Matsumoto Microsphere F-82D" manufactured by Matsumoto Yushi-Seiyaku Co., Ltd. was obtained. These are resin particles that expand and expand at 105 ° C. Furthermore, "Silica Balloon Q-CEL" manufactured by Asahi Glass Co., Ltd. was obtained as a third component.

【0041】そして、「エピコート828」100部、
イソホロンジアミン24部、発泡性樹脂40部及びシリ
カバルーン15部を、後述の如く混合加熱しスラリー状
混合物Aを調製した。
Then, 100 parts of "Epicote 828",
24 parts of isophorone diamine, 40 parts of expandable resin and 15 parts of silica balloon were mixed and heated as described below to prepare a slurry mixture A.

【0042】すなわち、まず、「エピコート828」、
発泡性樹脂、シリカバルーンを予め定量後混合した。こ
の混合液体をスラリー状液体Bとする。一方、イソホロ
ンジアミンは別にしておき、これを液体Cとする。これ
らの液体B、液体Cを図1に示す混合加熱装置に供給
し、ギアポンプで計量した液体B、液体Cをそれぞれ供
給口3及び供給口4からダイナミック混合部5へ供給す
る。両液体はダイナミック混合部5内でスピンドル1に
より混合され、排出管6へ混合物Aが排出される。排出
管6はマイクロ波照射部2内に導かれており、混合物A
は管内を流動中に直接マイクロ波で加熱して、所定温度
の混合物Aとした。
That is, first, "Epicoat 828",
The foaming resin and silica balloon were mixed in advance after quantitative determination. This mixed liquid is referred to as a slurry liquid B. On the other hand, the isophoronediamine is separately set, and this is liquid C. These liquids B and C are supplied to the mixing and heating device shown in FIG. 1, and the liquids B and C measured by the gear pump are supplied to the dynamic mixing section 5 from the supply ports 3 and 4, respectively. Both liquids are mixed by the spindle 1 in the dynamic mixing section 5, and the mixture A is discharged to the discharge pipe 6. The discharge pipe 6 is guided to the inside of the microwave irradiation unit 2, and the mixture A
Was heated directly in the tube by microwave while flowing to obtain a mixture A having a predetermined temperature.

【0043】一方、加熱冷却ができるように熱媒体を通
せるジャケットを持った上下1対の内寸法が幅210m
m、長さ300mm、厚み10mmの金型を準備した。
On the other hand, a pair of upper and lower inner dimensions having a jacket through which a heat medium can pass for heating and cooling has a width of 210 m.
A mold having m, a length of 300 mm and a thickness of 10 mm was prepared.

【0044】キャビティ内壁面の温度を80℃に保った
金型内に、上述の補強繊維材料と分離層を敷き、その上
に上述の如く混合加熱した表1に示す温度の混合物Aを
速やかに供給した。
The above-mentioned reinforcing fiber material and the separation layer were laid in a mold in which the temperature of the inner wall surface of the cavity was kept at 80 ° C., and the mixture A having the temperature shown in Table 1 and mixed and heated as described above was immediately added thereto. Supplied.

【0045】ついで、直ちにその上に分離層、補強繊維
材料をこの順序で載せるよう金型に納め、金型を閉じ
た。
Then, the separating layer and the reinforcing fiber material were immediately placed on the mold in this order, and the mold was closed.

【0046】金型を閉じてそのままの状態で2分間経過
した時に金型ジャケットと金型内の中心部温度が100
℃に達したので、直ちに冷却のため30℃の冷却用の熱
媒体を通して冷却した。冷却後、金型内の中心部温度が
60℃に達した時点で成形品を取り出した。
When the mold is closed and the condition is maintained for 2 minutes, the temperature of the center of the mold jacket and the mold is 100.
Since the temperature reached to 0 ° C, it was immediately cooled by passing through a heating medium for cooling at 30 ° C. After cooling, the molded product was taken out when the center temperature in the mold reached 60 ° C.

【0047】[0047]

【実施例2】成形時に金型を次の条件で積極的に加熱す
る以外は実施例1と全く同様にして実験を行った。すな
わち、本例では、金型を閉じると直ちに150℃の熱媒
を金型ジャケットに通して加熱し、金型内の中心部温度
が100℃に達してから、直ちに冷却のため30℃の冷
却用の熱媒体に切り替えた。そして、冷却後、金型内の
中心部温度が60℃に達した時点で成形品を取り出し
た。
Example 2 An experiment was conducted in exactly the same manner as in Example 1 except that the mold was positively heated under the following conditions during molding. That is, in this example, as soon as the mold is closed, a heating medium of 150 ° C. is passed through the mold jacket to heat the mold, and the temperature of the central portion in the mold reaches 100 ° C. I switched to the heat medium for. After cooling, the molded product was taken out when the temperature of the central portion in the mold reached 60 ° C.

【0048】[0048]

【比較例1】比較のため、実施例1において、混合物A
の加熱を行わずに該混合物Aを室温(25℃)で金型内
へ供給する以外は実施例2と全く同様にして成形品を製
造した。
Comparative Example 1 For comparison, in Example 1, the mixture A was used.
A molded article was produced in exactly the same manner as in Example 2 except that the mixture A was fed into the mold at room temperature (25 ° C.) without heating.

【0049】これらの各実験における成形条件、成形所
要時間等を、表1にまとめて示す。
The molding conditions and the required molding time in each of these experiments are shown in Table 1.

【0050】[0050]

【表1】 [Table 1]

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

【図1】本発明方法で使用する混合加熱装置の一例を示
す簡略化した断面図。
FIG. 1 is a simplified sectional view showing an example of a mixing and heating apparatus used in the method of the present invention.

【符号の説明】[Explanation of symbols]

1 スピンドル 2 マイクロ波照射装置 3 供給口 4 供給口 5 ダイナミック混合部 6 排出路 7 マイクロ波発信部 1 Spindle 2 Microwave Irradiation Device 3 Supply Port 4 Supply Port 5 Dynamic Mixing Section 6 Discharge Path 7 Microwave Transmission Section

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 少なくとも液状成形樹脂システムにより
所定の形状に成形された繊維強化樹脂層からなる表層部
及び発泡コアからなる芯部を有する複合成形品を製造す
るに当たり、(a)成形用の型内に、表層部成形用の材
料を設置すること、(b)型内の成形後の発泡コアとな
る部分に、少なくとも発泡性樹脂及び液状成形樹脂シス
テムを含む混合物を供給し、かつ、その際、少なくとも
混合により反応する成分は型に供給する直前に混合し、
該混合物を室温以上でかつ発泡性樹脂粒子が体積膨張を
生じる以下の温度にマイクロ波によって加熱した後、型
内へ供給すること、(c)型を閉じた後、型の所定領域
を十分高い温度まで加熱すること及び/又は上記液状成
形樹脂システムの反応熱による温度上昇により、コア部
に位置する発泡性樹脂を加熱発泡させて体積膨張を生じ
させ、これにより表層部形成用の材料を型の内壁面に対
して押し付けること、(d)その状態で液状成形樹脂シ
ステムを硬化させること、そして、(e)得られた複合
成形品を型から取り出すこと、を特徴とする複合成形品
の製造方法。
1. A mold for molding (a) for producing a composite molded article having at least a surface layer portion made of a fiber reinforced resin layer molded into a predetermined shape by a liquid molding resin system and a core portion made of a foamed core. And (b) supplying a mixture containing at least a foamable resin and a liquid molding resin system to a portion which becomes a foam core after molding in the mold, and at that time, , At least the components that react by mixing are mixed just before feeding to the mold,
The mixture is heated to a temperature not lower than room temperature and at a temperature not higher than that at which the expandable resin particles cause volume expansion by microwave, and then supplied into a mold, (c) after closing the mold, a predetermined region of the mold is sufficiently high. By heating to a temperature and / or temperature rise due to the reaction heat of the liquid molding resin system, the expandable resin located in the core part is heated and foamed to cause volume expansion, whereby the material for forming the surface layer part is molded. Manufacturing of a composite molded article, characterized by pressing against the inner wall surface of (5), (d) curing the liquid molding resin system in that state, and (e) removing the obtained composite molded article from the mold. Method.
JP5010785A 1993-01-26 1993-01-26 Manufacture of composite molded piece Pending JPH06218830A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5010785A JPH06218830A (en) 1993-01-26 1993-01-26 Manufacture of composite molded piece

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5010785A JPH06218830A (en) 1993-01-26 1993-01-26 Manufacture of composite molded piece

Publications (1)

Publication Number Publication Date
JPH06218830A true JPH06218830A (en) 1994-08-09

Family

ID=11759995

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5010785A Pending JPH06218830A (en) 1993-01-26 1993-01-26 Manufacture of composite molded piece

Country Status (1)

Country Link
JP (1) JPH06218830A (en)

Cited By (4)

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JP2021098375A (en) * 2016-12-01 2021-07-01 アディダス アーゲー Method of manufacturing plastic component, plastic component, and shoe
US11938697B2 (en) 2016-05-24 2024-03-26 Adidas Ag Method and apparatus for automatically manufacturing shoe soles
US11945184B2 (en) 2013-02-13 2024-04-02 Adidas Ag Methods for manufacturing cushioning elements for sports apparel
US11964445B2 (en) 2016-05-24 2024-04-23 Adidas Ag Method for the manufacture of a shoe sole, shoe sole, and shoe with pre-manufactured TPU article

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11945184B2 (en) 2013-02-13 2024-04-02 Adidas Ag Methods for manufacturing cushioning elements for sports apparel
US11938697B2 (en) 2016-05-24 2024-03-26 Adidas Ag Method and apparatus for automatically manufacturing shoe soles
US11964445B2 (en) 2016-05-24 2024-04-23 Adidas Ag Method for the manufacture of a shoe sole, shoe sole, and shoe with pre-manufactured TPU article
JP2021098375A (en) * 2016-12-01 2021-07-01 アディダス アーゲー Method of manufacturing plastic component, plastic component, and shoe
JP2022093335A (en) * 2016-12-01 2022-06-23 アディダス アーゲー Method of manufacturing plastic component, plastic component, and shoe

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