JP2974582B2 - Method for producing fiber-reinforced thermoplastic resin foam - Google Patents
Method for producing fiber-reinforced thermoplastic resin foamInfo
- Publication number
- JP2974582B2 JP2974582B2 JP6276652A JP27665294A JP2974582B2 JP 2974582 B2 JP2974582 B2 JP 2974582B2 JP 6276652 A JP6276652 A JP 6276652A JP 27665294 A JP27665294 A JP 27665294A JP 2974582 B2 JP2974582 B2 JP 2974582B2
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic resin
- fiber
- hollow body
- reinforced thermoplastic
- foaming
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Laminated Bodies (AREA)
- Moulding By Coating Moulds (AREA)
- Molding Of Porous Articles (AREA)
Description
【産業上の利用分野】本発明は、熱可塑性樹脂発泡体で
構成される芯材層と、繊維強化熱可塑性樹脂シートで構
成される表皮層とからなる繊維強化熱可塑性樹脂発泡体
の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a process for producing a fiber-reinforced thermoplastic resin foam comprising a core layer composed of a thermoplastic resin foam and a skin layer composed of a fiber-reinforced thermoplastic resin sheet. About.
【0001】[0001]
【従来の技術】長尺の横断面異形形状の成形体であって
その内部を発泡層とするものは、剛性に優れた成形体と
して建材その他の分野で、天然木材と同様に又はその代
替品として使用されている。かかる用途にあっては、剛
性を高めるため、芯材層を熱可塑性樹脂発泡体で構成
し、表皮層を繊維強化熱硬化性樹脂複合体で構成してな
る成形体が用いられている。2. Description of the Related Art A molded article having a long cross-sectionally irregular shape and having a foamed layer inside is used as a molded article having excellent rigidity in construction materials and other fields in the same manner as natural wood or as an alternative thereto. Has been used as In such an application, in order to increase rigidity, a molded article having a core material layer formed of a thermoplastic resin foam and a skin layer formed of a fiber-reinforced thermosetting resin composite is used.
【0002】特開平4−339635号公報には、機械
的強度及び軽量性に優れた複合体を連続的に製造するた
めに、合成樹脂発泡体を連続的に一方向に移送しつつそ
の外面に熱硬化性樹脂を含浸させた連続繊維を供給し、
加熱して引抜成形する製造方法が開示されている。しか
しながら、この方法では、横断面異形形状の発泡成形体
を予め用意しておく必要があり、また、引抜成形を行う
ために低粘度樹脂を用いることから表皮層の厚みむらや
機械的強度に不均一な箇所が発生しやすく、かつ、金型
内部での変形、賦形が困難である等の問題点があった。Japanese Patent Application Laid-Open No. 4-339635 discloses that in order to continuously produce a composite having excellent mechanical strength and light weight, a synthetic resin foam is continuously transferred in one direction while being transferred to the outer surface thereof. Supply continuous fiber impregnated with thermosetting resin,
A production method of drawing by heating is disclosed. However, in this method, it is necessary to prepare a foamed molded article having an irregular cross-sectional shape in advance, and since a low-viscosity resin is used for performing the pultrusion molding, the thickness unevenness of the skin layer and the mechanical strength are not sufficient. There have been problems such as that uniform portions are easily generated, and that deformation and shaping inside the mold are difficult.
【0003】[0003]
【発明が解決しようとする課題】本発明は、上記に鑑
み、表皮層が繊維強化熱可塑性樹脂、芯材層が発泡体で
ある繊維強化熱可塑性樹脂発泡体を製造するにあたっ
て、表皮層の厚みむらが少なく、曲げ強度等の機械的強
度に優れた、繊維強化熱可塑性樹脂発泡体の製造方法を
提供することを目的とする。SUMMARY OF THE INVENTION In view of the above, it is an object of the present invention to produce a fiber-reinforced thermoplastic resin foam in which the skin layer is a fiber-reinforced thermoplastic resin and the core material layer is a foam. An object of the present invention is to provide a method for producing a fiber-reinforced thermoplastic resin foam having less unevenness and excellent mechanical strength such as bending strength.
【0004】[0004]
【課題を解決するための手段】先ず、請求項1〜7に記
載の発明について説明する。First, the invention according to claims 1 to 7 will be described.
【0005】請求項1に記載の発明は、1枚又は複数枚
の繊維質シートを連続的に中空状に賦形する工程、中空
状体の内面に、発泡性樹脂組成物を発泡させながら供給
し、中空状体を発泡圧により所望形状に賦形する工程を
包含することを特徴とする。[0005] The invention according to claim 1 is a step of continuously forming one or a plurality of fibrous sheets into a hollow shape, and supplying the foamable resin composition to the inner surface of the hollow body while foaming the foamable resin composition. And a step of shaping the hollow body into a desired shape by foaming pressure.
【0006】請求項2に記載の発明は、1枚又は複数枚
の繊維質シートを連続的に中空状体に賦形する工程、中
空状体の内面に、発泡性樹脂組成物を供給し、発泡性樹
脂組成物を発泡剤の発泡温度以上に加熱し、中空状体を
発泡圧により所望形状に賦形する工程を包含することを
特徴とする。According to a second aspect of the present invention, there is provided a step of continuously forming one or a plurality of fibrous sheets into a hollow body, supplying a foamable resin composition to an inner surface of the hollow body, The method includes heating the foamable resin composition to a temperature equal to or higher than the foaming temperature of the foaming agent, and shaping the hollow body into a desired shape by foaming pressure.
【0007】請求項3に記載の発明は、1枚又は複数枚
の繊維強化熱可塑性樹脂シートを連続的に中空状体に賦
形する工程、中空状体を所定横断面形状に空気圧成形す
る工程、及び、中空状体の内面に、熱可塑性樹脂及び発
泡剤を含有する発泡性樹脂組成物を発泡させながら供給
し、中空状体を発泡圧により所望形状に賦形する工程を
包含することを特徴とする。According to a third aspect of the present invention, there is provided a step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets into a hollow body, and a step of pneumatically forming the hollow body into a predetermined cross-sectional shape. And a step of supplying a foamable resin composition containing a thermoplastic resin and a foaming agent to the inner surface of the hollow body while foaming the foamed body, and forming the hollow body into a desired shape by foaming pressure. Features.
【0008】請求項4に記載の発明は、1枚又は複数枚
の繊維強化熱可塑性樹脂シートを連続的に中空状体に賦
形する工程、中空状体を所定横断面形状に空気圧成形す
る工程、及び、空気圧成形された中空状体の内面に、熱
可塑性樹脂及び発泡剤を含有する発泡性樹脂組成物を供
給し、発泡性樹脂組成物を発泡剤の発泡温度以上に加熱
し、中空状体を発泡圧により所望形状に賦形する工程を
包含することを特徴とする。According to a fourth aspect of the present invention, there is provided a step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets into a hollow body, and a step of pneumatically forming the hollow body into a predetermined cross-sectional shape. And, on the inner surface of the pneumatically formed hollow body, a foamable resin composition containing a thermoplastic resin and a foaming agent is supplied, and the foamable resin composition is heated to a foaming temperature or higher of the foaming agent, and the hollow A step of shaping the body into a desired shape by foaming pressure.
【0009】請求項5に記載の発明は、1枚又は複数枚
の繊維強化熱可塑性樹脂層及び発泡性樹脂組成物層から
なる複合シートを、繊維強化熱可塑性樹脂層が外面とな
るように連続的に中空状体に賦形する工程、中空状体を
所定横断面形状に空気圧成形する工程、及び、発泡性樹
脂組成物層を発泡させ、中空状体を発泡圧により所望形
状に賦形する工程を包含することを特徴とする。According to a fifth aspect of the present invention, a composite sheet comprising one or a plurality of fiber-reinforced thermoplastic resin layers and a foamable resin composition layer is continuously formed such that the fiber-reinforced thermoplastic resin layer becomes an outer surface. Forming the hollow body into a hollow body, pneumatically forming the hollow body into a predetermined cross-sectional shape, and foaming the foamable resin composition layer, and shaping the hollow body into a desired shape by the foaming pressure. It is characterized by including a step.
【0010】請求項6に記載の発明は、1枚又は複数枚
の、連続繊維が多数配向した繊維強化熱可塑性樹脂シー
トを、連続繊維が長手方向となるように連続的に中空状
体に賦形する工程、中空状体を金型内に供給する工程、
中空状体の内面に、熱可塑性樹脂及び発泡剤を含有する
発泡性樹脂組成物を発泡させながら供給し、中空状体を
引き抜きつつ、中空状体を発泡圧により所望形状に賦形
する工程を包含することを特徴とする。請求項7に記載
の発明は、1枚又は複数枚の、連続繊維が多数配向した
繊維強化熱可塑性樹脂シートを、連続繊維が長手方向と
なるように連続的に中空状体に賦形する工程、中空状体
を金型内に供給する工程、中空状体の内面に、熱可塑性
樹脂及び発泡剤を含有する発泡性樹脂組成物を供給し、
発泡性樹脂組成物を発泡剤の発泡温度以上に加熱し、中
空状体を引き抜きつつ、中空状体を発泡圧により所望形
状に賦形する工程を包含することを特徴とする。本発明
において、繊維強化熱可塑性樹脂シートに用いられる熱
可塑性樹脂は、特に限定されず、例えば、ポリ塩化ビニ
ル、塩素化ポリ塩化ビニル、塩化ビニル−酢酸ビニル共
重合体、塩化ビニル−アクリル酸共重合体、ポリメチル
メタクリレート、ポリエチレン、ポリプロピレン、ポリ
スチレン、ポリアミド、ポリカーボネート、ポリフェニ
レンサルファイド、ポリスルホン、ポリエーテルエーテ
ルケトン等の他、熱可塑性エラストマー等が挙げられ、
賦形工程において、繊維強化熱可塑性樹脂シートが伸長
される場合があり、かかる場合は、伸長性に富んだ熱可
塑性樹脂を用いるのが好ましく、伸長性を向上させるた
めに適度の架橋処理を施してもよい。[0010] According to a sixth aspect of the present invention, one or a plurality of fiber-reinforced thermoplastic resin sheets in which a large number of continuous fibers are oriented are continuously applied to a hollow body so that the continuous fibers extend in the longitudinal direction. Forming, supplying the hollow body into the mold,
On the inner surface of the hollow body, a foaming resin composition containing a thermoplastic resin and a foaming agent is supplied while foaming, and while the hollow body is pulled out, the step of shaping the hollow body into a desired shape by foaming pressure is performed. It is characterized by including. The invention according to claim 7 is a step of continuously forming one or more fiber-reinforced thermoplastic resin sheets in which a large number of continuous fibers are oriented into a hollow body such that the continuous fibers are in the longitudinal direction. Step of supplying a hollow body into a mold, on the inner surface of the hollow body, supplying a foamable resin composition containing a thermoplastic resin and a foaming agent,
The method includes heating the foamable resin composition to a temperature equal to or higher than the foaming temperature of the foaming agent, and forming the hollow body into a desired shape by foaming pressure while extracting the hollow body. Oite the present invention <br/>, the thermoplastic resin used in the fiber-reinforced thermoplastic resin sheet is not particularly limited, for example, polyvinyl chloride, chlorinated polyvinyl chloride, vinyl chloride - vinyl acetate copolymer, Vinyl chloride-acrylic acid copolymer, polymethyl methacrylate, polyethylene, polypropylene, polystyrene, polyamide, polycarbonate, polyphenylene sulfide, polysulfone, polyether ether ketone, and the like, as well as thermoplastic elastomers,
In the shaping step, the fiber-reinforced thermoplastic resin sheet may be stretched. In such a case, it is preferable to use a thermoplastic resin having a high stretchability, and a moderate cross-linking treatment is performed to improve the stretchability. You may.
【0011】溶融粘度が、1×105 〜1×107 ポイ
ズの熱可塑性樹脂を用いることは、表皮層に厚みむらが
生じにくくなるので、好適である。なお、本発明におい
て、溶融粘度とは、高化式フローテスターを用い、熱融
着可能な温度においてφ1mm×L10mmのノズルか
ら150kg/cm2 の条件で押出したときの見かけの
粘度をいう。The use of a thermoplastic resin having a melt viscosity of 1 × 10 5 to 1 × 10 7 poise is preferable because uneven thickness of the skin layer hardly occurs. In the present invention, the melt viscosity refers to an apparent viscosity when extruded from a nozzle of φ1 mm × L10 mm under a condition of 150 kg / cm 2 at a temperature at which heat fusion is possible using a Koka type flow tester.
【0012】上記熱可塑性樹脂は、単独で使用されても
併用されてもよく、熱安定剤、可塑剤、滑剤、酸化防止
剤、紫外線吸収剤、顔料、無機充填剤、補強短繊維等の
添加剤、充填剤、加工助剤、改質剤等が添加されてもよ
い。The above-mentioned thermoplastic resins may be used alone or in combination. Addition of heat stabilizers, plasticizers, lubricants, antioxidants, ultraviolet absorbers, pigments, inorganic fillers, reinforcing short fibers, etc. Agents, fillers, processing aids, modifiers and the like may be added.
【0013】上記繊維強化熱可塑性樹脂シートに用いら
れる繊維としては、例えば、ガラス繊維、炭素繊維、金
属繊維等の無機繊維;アラミド繊維、ビニロン等の合成
繊維;絹、綿、麻等の天然繊維等の、補強繊維として使
用可能なすべての繊維を使用することができる。The fibers used in the fiber-reinforced thermoplastic resin sheet include, for example, inorganic fibers such as glass fiber, carbon fiber and metal fiber; synthetic fibers such as aramid fiber and vinylon; and natural fibers such as silk, cotton and hemp. All fibers that can be used as reinforcing fibers can be used.
【0014】上記繊維は、得られる繊維強化熱可塑性樹
脂シートの耐衝撃性を維持しつつ表面円滑性を損なわな
いためには、直径1〜100μm、長さ10mm以上の
長繊維又は連続繊維を用いるのがよい。繊維強化熱可塑
性樹脂シート内部での繊維形態としては、特に限定され
ず、例えば、長繊維がランダム配向したマット状;又は
連続繊維よりなるロービング状、ストランド状、クロス
状;連続繊維フィラメント1本1本が開繊した状態で複
合体の長手方向に引き揃えられた状態のもの、又はこれ
ら繊維状態を複数組み合わせたもの等が挙げられる。In order to maintain the impact resistance of the obtained fiber-reinforced thermoplastic resin sheet and not to impair the surface smoothness, a long fiber or continuous fiber having a diameter of 1 to 100 μm and a length of 10 mm or more is used. Is good. The form of the fiber inside the fiber reinforced thermoplastic resin sheet is not particularly limited, and may be, for example, a mat shape in which long fibers are randomly oriented; or a roving shape, a strand shape, or a cross shape made of continuous fibers; Examples include a state in which the book is spread and aligned in the longitudinal direction of the composite, a state in which a plurality of these fiber states are combined, and the like.
【0015】本発明で使用される繊維強化熱可塑性樹脂
シートは、特に限定されず、例えば、以下のようにして
製造される。一方向に引き揃えられて配された繊維形態
を有する繊維強化熱可塑性樹シートを得ようとするとき
には、流動槽の槽内に粉体状熱可塑性樹脂を入れ、槽底
に設けた多孔板から空気を噴出させることにより流動化
状態として、その中にガイドロールにより誘導された繊
維束を複数本通過させ、熱可塑性樹脂付着又は/及び侵
入繊維束とし、その後加熱ロールを通過させることによ
り繊維に熱可塑性樹脂を含浸させ、冷却ロールを通過さ
せて所望の繊維強化熱可塑性樹脂シートを得る。又、繊
維がランダムな状態で配されている繊維強化熱可塑性樹
脂シートを得ようとするときには、上記の如くして得ら
れた熱可塑性樹脂付着又は/及び侵入繊維束を、ロータ
リーカッターで細断し、下部無端ベルト上へ落下させて
集積し、上下部無端ベルトで挟みつつ加圧して加熱炉内
を通過させ、細断された繊維に熱可塑性樹脂を含浸さ
せ、その後冷却ガイドロールを通過させて、所望の繊維
強化熱可塑性樹脂シートを得る。The fiber-reinforced thermoplastic resin sheet used in the present invention is not particularly limited, and is manufactured, for example, as follows. When trying to obtain a fiber-reinforced thermoplastic tree sheet having a fiber form arranged and aligned in one direction, put the powdery thermoplastic resin in the tank of the fluidized tank, from the perforated plate provided in the tank bottom A plurality of fiber bundles guided by guide rolls are passed through in a fluidized state by jetting air, and a thermoplastic resin adhered or / and penetrated fiber bundle is formed. It is impregnated with a thermoplastic resin and passed through a cooling roll to obtain a desired fiber-reinforced thermoplastic resin sheet. When it is intended to obtain a fiber-reinforced thermoplastic resin sheet in which fibers are randomly arranged, the thermoplastic resin-adhered or / and penetrating fiber bundle obtained as described above is shredded with a rotary cutter. Then, it is dropped and accumulated on the lower endless belt, pressed and sandwiched by the upper and lower endless belts, passed through the heating furnace, impregnated with the chopped fibers with the thermoplastic resin, and then passed through the cooling guide roll. Thus, a desired fiber-reinforced thermoplastic resin sheet is obtained.
【0016】又、溶融粘度の低い熱可塑性樹脂を使用す
る場合は、溶融状態にある熱可塑性樹脂に繊維を浸漬さ
せて熱可塑性樹脂シートを製造することも可能である。
かかる場合、繊維強化熱可塑性樹脂シートを製造後、熱
可塑性樹脂を架橋することが好ましい。When a thermoplastic resin having a low melt viscosity is used, it is also possible to produce a thermoplastic resin sheet by immersing fibers in a thermoplastic resin in a molten state.
In such a case, it is preferable to crosslink the thermoplastic resin after producing the fiber-reinforced thermoplastic resin sheet.
【0017】中空状体に空気圧成形を施す場合は、中空
状体の気密性を向上させ賦形性を向上させるため、上記
製造方法において予め繊維束間に熱可塑性樹脂を含浸さ
せたり、得られた繊維強化熱可塑性樹脂シートに表面処
理を施し、繊維と熱可塑性樹脂との密着性を向上させる
ことが好ましい。なお、繊維強化熱可塑性樹脂シート
は、単層であっても、繊維強化熱可塑性樹シートが複数
積層されたものであってもよい。In the case where the hollow body is subjected to pneumatic molding, in order to improve the airtightness of the hollow body and improve the shaping property, a thermoplastic resin is previously impregnated between the fiber bundles or obtained in the above-mentioned production method. It is preferable that the fiber-reinforced thermoplastic resin sheet is subjected to a surface treatment to improve the adhesion between the fiber and the thermoplastic resin. The fiber reinforced thermoplastic resin sheet may be a single layer or a laminate of a plurality of fiber reinforced thermoplastic resin sheets.
【0018】繊維強化熱可塑性樹脂シートの厚みは特に
限定されないが、薄くなると、補強効果がなく、厚くな
ると、賦形が困難となるので、厚み0.1〜10mmが
好ましい。繊維強化熱可塑性樹脂シート中の繊維量は、
少なくなると、充分な補強効果、成形安定性を得ること
ができず、又、多くなると、熱可塑性樹脂が含浸できず
融着が困難となり、却って補強効果が低下し、若しくは
空気圧成形を施す場合気密性が低下し中空状体の賦形が
不十分となるので、5〜70体積%が好ましく、10〜
50体積%がより好ましい。The thickness of the fiber reinforced thermoplastic resin sheet is not particularly limited. However, if the thickness is small, there is no reinforcing effect, and if the thickness is large, shaping becomes difficult. Therefore, the thickness is preferably 0.1 to 10 mm. The amount of fibers in the fiber reinforced thermoplastic resin sheet is
If the amount is too small, sufficient reinforcing effect and molding stability cannot be obtained.If the amount is too large, the thermoplastic resin cannot be impregnated and fusion becomes difficult. 5 to 70% by volume is preferable because the shapeability of the hollow body becomes insufficient due to a decrease in the property.
50% by volume is more preferred.
【0019】上記繊維強化熱可塑性樹脂シートは、中空
状体とされ、空気圧成形又は/及び発泡圧により賦形さ
れる。その際、外部から金型等の規制体により中空状体
が規制される場合があり、規制体と繊維強化熱可塑性樹
脂シート間で摩擦力が発生する。従って、摩擦力に抗し
ながら引抜きつつ成形する際、繊維強化熱可塑性樹脂シ
ートの切断等を防止するため、繊維強化熱可塑性樹脂シ
ートの繊維形態は、繊維強化熱可塑性樹脂シートの長手
方向に連続繊維が引き揃えられたものであるのが好まし
い。なお、繊維強化熱可塑性樹脂シートを積層し、複層
で用いる場合は、そのうちの少なくとも一層が上記形態
であれば足りる。The above fiber-reinforced thermoplastic resin sheet is formed into a hollow body, and is formed by pneumatic molding or / and foaming pressure. At that time, the hollow body may be regulated from outside by a regulating body such as a mold, and a frictional force is generated between the regulating body and the fiber-reinforced thermoplastic resin sheet. Therefore, when forming while drawing while resisting frictional force, the fiber form of the fiber reinforced thermoplastic resin sheet is continuous in the longitudinal direction of the fiber reinforced thermoplastic resin sheet in order to prevent the fiber reinforced thermoplastic resin sheet from being cut or the like. Preferably, the fibers are aligned. In the case of laminating fiber-reinforced thermoplastic resin sheets and using them in multiple layers, it is sufficient that at least one of them has the above-mentioned form.
【0020】上記繊維強化熱可塑性樹脂シートからなる
繊維強化熱可塑性樹脂層の一面に発泡性樹脂組成物層が
積層された複合シートを、繊維強化熱可塑性樹脂シート
の代わりに用いることは、得られる繊維強化熱可塑性樹
脂発泡体の表面層と芯材層との界面に発泡性樹脂組成物
から発生したガスが進入し、得られる繊維強化熱可塑性
樹脂発泡体の表面層と芯材層間にボイドが生じるのを防
止することができ、表面層と芯材層の融着性の優れた繊
維強化熱可塑性樹脂発泡体を得ることができ好適であ
る。発泡性樹脂組成物層は、下記に述べる、未発泡のま
ま中空体内面に供給される、発泡性樹脂組成物と同様の
ものからなる。繊維強化熱可塑性樹脂シートの場合と同
様に、複合シートは、単層で用いられても、複合シート
が複数積層されたものであってもよい。The use of a composite sheet in which a foamable resin composition layer is laminated on one side of a fiber-reinforced thermoplastic resin layer composed of the above-mentioned fiber-reinforced thermoplastic resin sheet, instead of the fiber-reinforced thermoplastic resin sheet, can be obtained. Gas generated from the foamable resin composition enters the interface between the surface layer of the fiber reinforced thermoplastic resin foam and the core material layer, and voids are formed between the surface layer of the obtained fiber reinforced thermoplastic resin foam and the core material layer. This is preferable because it is possible to obtain a fiber-reinforced thermoplastic resin foam having excellent fusion between the surface layer and the core material layer. The foamable resin composition layer is the same as the foamable resin composition described below, which is supplied to the inner surface of the hollow body without being foamed. As in the case of the fiber reinforced thermoplastic resin sheet, the composite sheet may be used as a single layer or a laminate of a plurality of composite sheets.
【0021】複合シートの製造方法は特に限定されず、
例えば、上記方法で得られた繊維強化熱可塑性樹脂シー
トの一面に、予め製造された発泡性樹脂組成物シートを
加熱融着させることにより、複合シートを製造する方
法;上記方法で得られた繊維強化熱可塑性樹脂シートの
一面に、未発泡の発泡性樹脂組成物をシート状に押出積
層し、複合シートを製造する方法等が挙げられる。The method for producing the composite sheet is not particularly limited.
For example, a method for producing a composite sheet by heat-sealing a foamable resin composition sheet produced in advance on one surface of the fiber-reinforced thermoplastic resin sheet obtained by the above method; a fiber obtained by the above method A method of extruding and laminating an unfoamed foamable resin composition on one surface of a reinforced thermoplastic resin sheet to form a composite sheet, or the like, may be used.
【0022】上記繊維強化熱可塑性樹脂シートの代わり
に繊維質シートを用いてもよい。繊維質シートを用いる
と、発泡性樹脂組成物を発泡させ中空状体をその発泡圧
により賦形する際、繊維質シートに発泡性樹脂組成物を
含浸させることができ、予め繊維強化熱可塑性樹脂シー
ト等を製造しておく必要がないので、工程を省くことが
でき、好適である。A fibrous sheet may be used instead of the above fiber-reinforced thermoplastic resin sheet. When the fibrous sheet is used, when the foamable resin composition is foamed and the hollow body is shaped by the foaming pressure, the fibrous sheet can be impregnated with the foamable resin composition, and the fiber reinforced thermoplastic resin can be used in advance. Since there is no need to manufacture a sheet or the like, the steps can be omitted, which is preferable.
【0023】繊維質シートに用いられる繊維としては、
発泡性樹脂組成物を構成する熱可塑性樹脂の溶融温度
や、発泡性樹脂組成物の発泡温度で溶融しないものであ
れば、特に限定されず、例えば、ガラス繊維、炭素繊
維、シリコン・チタン・炭素繊維、ボロン繊維、金属繊
維、アラミド繊維、ポリエステル繊維、ポリアミド繊維
等が挙げられる。The fibers used in the fibrous sheet include:
It is not particularly limited as long as it does not melt at the melting temperature of the thermoplastic resin constituting the foamable resin composition or at the foaming temperature of the foamable resin composition. For example, glass fiber, carbon fiber, silicon / titanium / carbon Fiber, boron fiber, metal fiber, aramid fiber, polyester fiber, polyamide fiber and the like.
【0024】繊維質シートに用いられる繊維のモノフィ
ラメント径は、小さくなると、補強効果が低下し、又、
大きくなると、軽量性を損なわない様に、目付重量は一
定の値とされるため、単位面積当たりの繊維の本数が減
少し、樹脂と繊維の接触面積が低下し、得られる繊維強
化熱可塑性樹脂発泡体の表面層の強度が低下するので、
1〜50μmが好ましく、更に3〜23μmが好まし
い。When the monofilament diameter of the fiber used in the fibrous sheet is reduced, the reinforcing effect is reduced, and
As the weight increases, the weight per unit area is reduced so that the weight per unit area is reduced so as not to impair the lightness, the contact area between the resin and the fiber decreases, and the obtained fiber reinforced thermoplastic resin As the strength of the foam surface layer decreases,
It is preferably from 1 to 50 μm, more preferably from 3 to 23 μm.
【0025】繊維質シートとは、繊維を堆積又は絡み合
わせてシート状にしたものをいい、好ましくは、コンテ
ィニュアスマット、スワルマット、チョップドストラン
ドマット、繊維クロス等の、長繊維又は連続繊維が少量
の結着剤で結着されたものが好ましい。The fibrous sheet refers to a sheet formed by depositing or entangled fibers, and is preferably a small amount of long fibers or continuous fibers such as continuous mat, swirl mat, chopped strand mat, and fiber cloth. Those bound with a binder are preferred.
【0026】繊維質シートの空隙率は、小さくなると、
発泡性樹脂組成物の発泡による、繊維質シートへの樹脂
の含浸が少なくなり、表面層と芯材層が剥離しやすくな
り、又、大きくなると、繊維による補強効果が低下する
ので、5〜15容積%であるのが好ましい。When the porosity of the fibrous sheet decreases,
The impregnation of the resin into the fibrous sheet due to the foaming of the foamable resin composition is reduced, and the surface layer and the core material layer are easily peeled off. It is preferably volume%.
【0027】なお、中空体が賦形される際、中空体が全
体的に又は部分的に延伸される場合がある。かかる場
合、延伸によって中空体に亀裂又は薄肉化が生じ、得ら
れる繊維強化熱可塑性樹脂発泡体の表面層に部分的に剛
性の低下した部分が生じる場合がある。これを防止する
ため、上記繊維強化熱可塑性樹脂シート又は繊維質シー
トを用いる場合には中空体の外面又は内面に、複合シー
トを用いる場合には中空体の外面に、延伸性に優れた熱
可塑性樹脂層を積層してもよい。特に、外面に上記熱可
塑性樹脂層を積層することは、上記効果の他に、得られ
る繊維強化熱可塑性樹脂発泡体の表面層の平滑性が向上
し、好適である。When the hollow body is shaped, the hollow body may be stretched completely or partially. In such a case, the hollow body may be cracked or thinned by the stretching, and a part of the surface layer of the obtained fiber-reinforced thermoplastic resin foam may have a partially reduced rigidity. To prevent this, when using the above fiber-reinforced thermoplastic resin sheet or fibrous sheet, on the outer surface or inner surface of the hollow body, and when using a composite sheet, on the outer surface of the hollow body, a thermoplastic material having excellent stretchability. A resin layer may be laminated. In particular, it is preferable to laminate the thermoplastic resin layer on the outer surface, in addition to the effects described above, because the smoothness of the surface layer of the obtained fiber-reinforced thermoplastic resin foam is improved.
【0028】又、中空状体に空気圧成形を施す場合は、
上記の如く熱可塑性樹脂層を積層することは、中空状体
の気密性を向上させ中空状体の賦形性を向上させる効果
もあり好ましい。When the hollow body is subjected to pneumatic molding,
Laminating the thermoplastic resin layer as described above is preferable because it has the effect of improving the airtightness of the hollow body and improving the shapeability of the hollow body.
【0029】繊維強化熱可塑性樹脂シート、複合シート
及び繊維質シートを中空状体に賦形する方法は、特に限
定されず、例えば、実施例において後述する金型を用い
る方法の他に、合成樹脂、金属製のシューやロール等で
徐々に曲げていく方法が挙げられる。中空状に賦形する
際には、繊維強化熱可塑性樹脂シート、複合シート又は
繊維質シートの割れや裂けを防ぐため、遠赤外線ヒータ
ーや熱風ブロアーで加熱し、熱可塑性樹脂を軟化状態と
しながら賦形を行うのが好ましい。The method of shaping the fiber-reinforced thermoplastic resin sheet, the composite sheet and the fibrous sheet into a hollow body is not particularly limited. For example, in addition to a method using a mold described later in Examples, a synthetic resin And a method of bending gradually with a metal shoe or roll. When forming into a hollow shape, in order to prevent the fiber-reinforced thermoplastic resin sheet, composite sheet or fibrous sheet from cracking or tearing, it is heated with a far-infrared heater or hot air blower to form the thermoplastic resin while softening it. Preferably, shaping is performed.
【0030】なお、本発明でいう「中空状体」とは、端
部同士を突き合わせ又は重なり合わさって賦形されてい
るものの他、端部同士に若干の隙間を生じている場合も
含まれる。The term "hollow body" as used in the present invention includes not only those formed by abutting or overlapping the ends but also forming a slight gap between the ends.
【0031】中空状体に空気圧成形を施す場合、繊維強
化熱可塑性樹脂シート又は複合シートに用いられる熱可
塑性樹脂として高溶融粘度のものが用いられ、中空状体
に賦形する過程で端部同士が熱可塑性樹脂の溶融により
一体化されている場合は、端部同士が突き合わされて中
空状体に賦形されている場合であっても、空気圧成形に
よる賦形性が低下しないので問題ないが、そうでない場
合は、中空状体の気密性を向上させ、賦形性を向上させ
るため、中空状体は端部同士を重なり合わせ賦形された
ものとするのが好ましい。When a hollow body is subjected to pneumatic molding, a thermoplastic resin having a high melt viscosity is used as a fiber-reinforced thermoplastic resin sheet or a composite sheet. In the case where is integrated by melting of the thermoplastic resin, even if the ends are abutted and shaped into a hollow body, there is no problem because the shapeability by pneumatic molding does not decrease. Otherwise, in order to improve the airtightness of the hollow body and improve the shapeability, it is preferable that the hollow body is formed by overlapping the ends thereof.
【0032】又、繊維強化熱可塑性樹脂シート、複合シ
ート及び繊維質シートを中空状体に賦形する際、複数枚
の繊維強化熱可塑性樹脂シート等を用い、各々の端部同
士を突き合わせ又は重ね合わせて、中空状体に賦形して
もよい。When shaping the fiber-reinforced thermoplastic resin sheet, composite sheet, and fibrous sheet into a hollow body, a plurality of fiber-reinforced thermoplastic resin sheets or the like are used to abut or overlap each end. In addition, it may be shaped into a hollow body.
【0033】特に、空気圧成形又は発泡圧による賦形に
より、所望横断面形状の全周が中空状体の全周に比して
大きくなる場合、複数枚の繊維強化熱可塑性樹脂シート
等の端部同士を、賦形過程で延伸する部分に相当する部
分に延伸する分だけ重ね合わせて中空状体に賦形するこ
とは、延伸する際重ね合わせた部分がずれ、又、各々の
繊維強化熱可塑性樹脂シートがわずかづづ延伸すること
により、1枚の繊維強化熱可塑性樹脂シート等で中空状
体とした場合に比して、各々の繊維強化熱可塑性樹脂シ
ートの延伸度が少なくなる。In particular, when the entire circumference of the desired cross-sectional shape becomes larger than the entire circumference of the hollow body by pneumatic molding or shaping by foaming pressure, the end portions of a plurality of fiber-reinforced thermoplastic resin sheets or the like are used. To form a hollow body by overlapping each other by an amount corresponding to the portion corresponding to the portion to be stretched in the shaping process, the overlapped portion is displaced when stretching, and each fiber-reinforced thermoplastic By stretching the resin sheet little by little, the degree of stretching of each fiber-reinforced thermoplastic resin sheet becomes smaller than when a hollow body is formed by a single fiber-reinforced thermoplastic resin sheet or the like.
【0034】従って、複数枚の繊維強化熱可塑性樹脂シ
ート等を端部同士を重ね合わせて、中空状体に賦形する
ことは、表皮層の薄肉化を緩和させ、得られる繊維強化
熱可塑性樹脂発泡体の剛性の低下を防止することができ
ると共に、中空状体の賦形過程において中空状体が部分
的に大きく延伸され、得られる表皮層に部分的な薄肉化
が生じるのを防止することができ、全体的に同一の剛性
を有する繊維強化熱可塑性樹脂発泡体を得ることができ
好適である。Accordingly, by forming a plurality of fiber-reinforced thermoplastic resin sheets or the like into a hollow body by overlapping the end portions thereof, the thickness of the skin layer is reduced, and the obtained fiber-reinforced thermoplastic resin sheet is formed. It is possible to prevent the rigidity of the foam from lowering, and to prevent the hollow body from being partially stretched greatly in the process of shaping the hollow body, so that the obtained skin layer is partially thinned. It is possible to obtain a fiber-reinforced thermoplastic resin foam having the same rigidity as a whole, which is preferable.
【0035】請求項1、2、6、7に記載の発明は、上
記の如く得られた中空状体を、発泡圧により所望形状に
賦形することを特徴とし、請求項3、4に記載の発明
は、上記の如く得られた中空状体を、空気圧成形及び発
泡圧により所望形状に賦形することを特徴とし、請求項
5に記載の発明は、上記の如く得られた中空状体を、空
気圧成形及び発泡性樹脂組成物の発泡による発泡圧によ
り所望形状に賦形することを特徴とするものである。な
お、空気圧成形とは、真空成形の他、圧空成形も含ま
れ、ここに「空気」とは、所謂「大気」の他、窒素ガス
等のガスも含まれることはいうまでもない。[0035] The invention according to claim 1, 2, 6, 7 is a hollow body obtained as described above, characterized in that to shape into a desired shape by foaming pressure, according to claim 3, 4 The present invention is characterized in that the hollow body obtained as described above is shaped into a desired shape by pneumatic molding and foaming pressure.
The invention described in 5 is characterized in that the hollow body obtained as described above is shaped into a desired shape by air pressure molding and foaming pressure due to foaming of the foamable resin composition. The pneumatic forming includes not only vacuum forming but also pneumatic forming. Needless to say, “air” includes not only so-called “atmosphere” but also a gas such as nitrogen gas.
【0036】請求項3〜5に記載の発明の如く、発泡性
樹脂組成物の発泡圧による賦形と共に、中空状体を空気
圧成形しておくことは、発泡圧による賦形だけの場合に
比して、複雑な横断面形状を得たい場合、特に正確な横
断面形状を有する繊維強化熱可塑性樹脂発泡体を得るこ
とができ、好適である。As described in the third to fifth aspects of the present invention, forming the hollow body by air pressure together with the shaping of the expandable resin composition by the foaming pressure is more efficient than forming by the foaming pressure alone. Thus, when it is desired to obtain a complicated cross-sectional shape, a fiber-reinforced thermoplastic resin foam having a particularly accurate cross-sectional shape can be obtained, which is preferable.
【0037】本発明で使用される発泡性樹脂組成物は、
熱可塑性樹脂及び発泡剤を含有する。上記熱可塑性樹脂
としては、発泡可能なすべての熱可塑性樹脂が挙げら
れ、例えば、ポリ塩化ビニル、塩素化ポリ塩化ビニル、
ポリエチレン、ポリプロピレン、ポリスチレン、ポリア
ミド、ポリカーボネート、ポリフェニレンサルファイ
ド、ポリスルホン、ポリエーテルエーテルケトン等が挙
げられるが、成形温度領域において、繊維強化熱可塑性
樹脂シートに使用される上記熱可塑性樹脂に比べて相対
的に粘度の低い流動性の良い樹脂を用いることは、発泡
むらを防ぎ、得られる繊維強化熱可塑性樹脂発泡体の表
皮層の厚みの均一性を向上させる点で好ましい。The foamable resin composition used in the present invention comprises:
Contains a thermoplastic resin and a foaming agent. Examples of the thermoplastic resin include all foamable thermoplastic resins, for example, polyvinyl chloride, chlorinated polyvinyl chloride,
Polyethylene, polypropylene, polystyrene, polyamide, polycarbonate, polyphenylene sulfide, polysulfone, polyetheretherketone, and the like, but in the molding temperature range, relative to the thermoplastic resin used for the fiber-reinforced thermoplastic resin sheet. It is preferable to use a resin having a low viscosity and a good flowability in order to prevent uneven foaming and to improve the uniformity of the thickness of the skin layer of the obtained fiber-reinforced thermoplastic resin foam.
【0038】なお、表皮層となる繊維強化熱可塑性樹脂
シート等に用いられる熱可塑性樹脂と、発泡性樹脂組成
物に用いられる熱可塑性樹脂は、同一である必要は無
く、両者を溶融様態(熱融着可能な状態)になるまで加
熱し、圧着した際、冷却後に融着した界面が容易に剥離
しない状態となるものであれば、両者の組み合わせは、
特に限定されない。The thermoplastic resin used for the fiber-reinforced thermoplastic resin sheet or the like serving as the skin layer does not need to be the same as the thermoplastic resin used for the foamable resin composition. was heated to fusible state), when the crimp as long as a state of the interface after the cohesion after cooling is not easily peeled off, the combination of both,
There is no particular limitation.
【0039】但し、繊維質シートを用いた場合、発泡性
熱可塑性樹脂に用いられる熱可塑性樹脂の溶融粘度は、
高くなると、繊維質シート間に樹脂を含浸させることが
困難となり、又、低くなると、得られる発泡体の気泡が
均一微細とならないため、6000〜30000ポイズ
の範囲が好ましい。However, when a fibrous sheet is used, the melt viscosity of the thermoplastic resin used for the expandable thermoplastic resin is as follows:
If it is too high, it becomes difficult to impregnate the resin between the fibrous sheets, and if it is too low, the resulting foam does not have uniform and fine cells, so the range of 6,000 to 30,000 poise is preferable.
【0040】なお、発泡性樹脂組成物に用いられる熱可
塑性樹脂は、単独又は複数の混合物として用いられても
よく、また、発泡性樹脂組成物の発泡性を損なわない範
囲内で、熱安定剤、可塑剤、滑剤、酸化防止剤、紫外線
吸収剤、顔料、無機充填材、補強繊維等の添加剤、充填
材、加工助剤、改質剤等が加えられていてもよい。リサ
イクルの点から、廃プラスチック、木質材料、木粉、シ
ート・モールディング・コンパウンド(SMC)粉砕粉
等が好ましい。The thermoplastic resin used in the foamable resin composition may be used alone or as a mixture of a plurality of thermoplastic resins. The heat stabilizer may be used within a range that does not impair the foamability of the foamable resin composition. Plasticizers, lubricants, antioxidants, ultraviolet absorbers, pigments, inorganic fillers, additives such as reinforcing fibers, fillers, processing aids, modifiers, and the like may be added. From the viewpoint of recycling, waste plastic, woody material, wood flour, ground powder of sheet molding compound (SMC) and the like are preferable.
【0041】補強繊維を添加する場合、少なくなると、
補強効果がなく、又、多くなると、均一に発泡させるこ
とが困難となり、却って、補強効果が低下するので、発
泡性樹脂組成物中、5〜60体積%が好ましく、20〜
30体積%が更に好ましい。In the case where the reinforcing fibers are added,
There is no reinforcing effect, and when it increases, it becomes difficult to foam uniformly, and on the contrary, the reinforcing effect is reduced.
30% by volume is more preferred.
【0042】また、発泡性を改善するために架橋処理が
施されてもよい。上記架橋処理方法は、特に限定され
ず、例えば、可視光線、紫外線、α線、β線、γ線、X
線又は電子線等の活性エネルギー線の照射により架橋す
る方法、有機過酸化物を添加し分解し架橋する方法、架
橋性シラン変性熱可塑性樹脂を添加し水処理することに
より架橋する方法等が挙げられる。Further, a cross-linking treatment may be performed to improve the foamability. The crosslinking treatment method is not particularly limited, for example, visible light, ultraviolet light, α-ray, β-ray, γ-ray, X
A method of crosslinking by irradiation with an active energy ray such as a beam or an electron beam, a method of adding an organic peroxide to decompose and crosslink, a method of adding a crosslinkable silane-modified thermoplastic resin and performing a water treatment to perform crosslinking. Can be
【0043】電子線により架橋する熱可塑性樹脂として
は、例えば、ポリエチレン、ポリプロピレン、ポリスチ
レン等のα−水素を持った熱可塑性樹脂等が挙げられ、
また可視光線、紫外線により架橋する熱可塑性樹脂とし
ては、必要により光重合開始剤(光増感剤)を含有した
熱可塑性樹脂等が挙げられ、光重合開始剤としては、例
えば、ベンゾインアルキルエーテル系、アセトフェノン
系、ベンゾフェノン系、チオキサントン系等が挙げられ
る。Examples of the thermoplastic resin crosslinked by an electron beam include thermoplastic resins having α-hydrogen such as polyethylene, polypropylene and polystyrene.
Examples of the thermoplastic resin that can be crosslinked by visible light and ultraviolet light include a thermoplastic resin containing a photopolymerization initiator (photosensitizer) if necessary. Examples of the photopolymerization initiator include benzoin alkyl ether-based Acetophenone type, benzophenone type, thioxanthone type and the like.
【0044】又、有機過酸化物としては、特に限定され
ず、例えば、イソブチルパーオキサイド、ジクミルパー
オキサイド、2,5−ジメチル−2,5−ジ(t−ブチ
ルパーオキシ)ヘキセン、1,3−ビス(t−ブチルパ
ーオキシイソプロピル)ベンゼン、t−ブチルクミルパ
ーオキサイド、ジ−t−ブチルパーオキサイド等が挙げ
られる。この際、有機過酸化物の添加によって、一般
に、熱可塑性樹脂そのものが開裂しやすくなるが、所望
程度に架橋が進行しない場合には、適宜、トリアリルシ
アヌレート、ジアリルフタレート等の架橋助剤を添加し
てもよい。The organic peroxide is not particularly restricted but includes, for example, isobutyl peroxide, dicumyl peroxide, 2,5-dimethyl-2,5-di (t-butylperoxy) hexene, 3-bis (t-butylperoxyisopropyl) benzene, t-butylcumyl peroxide, di-t-butyl peroxide and the like. At this time, the addition of the organic peroxide generally causes the thermoplastic resin itself to be easily cleaved.However, when the crosslinking does not proceed to a desired degree, a crosslinking auxiliary such as triallyl cyanurate or diallyl phthalate is appropriately added. It may be added.
【0045】上記発泡剤は、特に限定されず、分解して
ガスを発生する分解型発泡剤、気化によりガスを発生す
る物理型発泡剤の他、気体でも良く、分解型発泡剤とし
ては、例えば、アゾジカルボンアミド、アゾビスイソブ
チロニトリル、N,N′−ジニトロペンタメチレンテト
ラミン、p,p′−オキシビスベンゼンスルホニルヒド
ラジド、アゾジカルボン酸バリウム、トリヒドラジノト
リアジン、5−フェニルテトラゾール等が挙げられる。The foaming agent is not particularly limited, and may be a decomposable foaming agent that decomposes to generate gas, a physical foaming agent that generates gas by vaporization, or a gas. Azodicarbonamide, azobisisobutyronitrile, N, N'-dinitropentamethylenetetramine, p, p'-oxybisbenzenesulfonylhydrazide, barium azodicarboxylate, trihydrazinotriazine, 5-phenyltetrazole and the like. Can be
【0046】物理型発泡剤としては、例えば、イソペン
タン、ヘプタン、シクロヘキサン等の脂肪族炭化水素、
トリクロロトリフルオロエタン、ジクロロテトラフルオ
ロエタン等のふっ化脂肪族炭化水素等が挙げられる。気
体としては、例えば、空気、窒素、ヘリウム等が挙げら
れる。上記発泡剤は、多量に加えて得られる発泡体の発
泡倍率が高くなると、得られる芯材層を構成する発泡体
の剛性が低下するので、発泡倍率が30倍以下が好まし
く、かかる範囲内となるように配合するのが好ましい。
具体的には、分解型発泡剤及び物理型発泡剤の場合は、
発泡剤の種類にもよるが、熱可塑性樹脂100重量部に
対して1〜20重量部が好ましい。Examples of the physical foaming agent include aliphatic hydrocarbons such as isopentane, heptane and cyclohexane;
Fluorinated aliphatic hydrocarbons such as trichlorotrifluoroethane and dichlorotetrafluoroethane are exemplified. Examples of the gas include air, nitrogen, and helium. The above foaming agent, when the foaming ratio of the foam obtained by adding a large amount increases, the rigidity of the foam constituting the obtained core material layer decreases, the foaming ratio is preferably 30 times or less, and within this range It is preferable to mix them.
Specifically, in the case of a decomposition type foaming agent and a physical type foaming agent,
Although it depends on the type of the foaming agent, the amount is preferably 1 to 20 parts by weight based on 100 parts by weight of the thermoplastic resin.
【0047】本発明において、複合シートを用いずに、
繊維強化熱可塑性樹脂又は繊維質シートを用いた場合
は、発泡性樹脂組成物を供給する必要があるが、発泡性
樹脂組成物の中空状体内面への供給は、発泡させながら
供給しても、未発泡のまま供給してもよい。In the present invention, without using a composite sheet,
When using a fiber-reinforced thermoplastic resin or a fibrous sheet, it is necessary to supply a foamable resin composition, but the supply of the foamable resin composition to the hollow body surface may be performed while foaming. Alternatively, it may be supplied without foaming.
【0048】発泡性樹脂組成物を発泡させながら供給す
る方法としては、例えば、熱可塑性樹脂に発泡剤を、発
泡剤の発泡温度以下の温度で、混練又は含浸させること
により発泡性樹脂組成物を得た後、押出機に供給し発泡
剤の発泡温度以上に加熱し、発泡させつつ供給する方
法;熱可塑性樹脂を押出機に供給、溶融混練し、溶融状
態となった熱可塑性樹脂に、押出機途中から物理型発泡
剤又は気体を供給し、発泡させつつ供給する方法等が挙
げられる。なお、本発明において、発泡温度とは、分解
型発泡剤の場合はその分解温度を、物理型発泡剤の場合
はその沸点をいう。なお、分解温度とは、半減期が3分
となる温度をいう。但し、発泡温度において、発泡性樹
脂組成物が発泡可能な状態にあるのはいうまでもないAs a method of supplying the foamable resin composition while foaming the foamable resin composition, for example, a foaming agent is kneaded or impregnated at a temperature not higher than the foaming temperature of the foaming agent with the thermoplastic resin. After it is obtained, it is supplied to an extruder and heated to a temperature higher than the foaming temperature of the foaming agent, and supplied while being foamed. A method in which a physical foaming agent or gas is supplied in the middle of the machine, and supplied while foaming is performed. In the present invention, the term "foaming temperature" refers to the decomposition temperature of a decomposable foaming agent and the boiling point of a physical foaming agent. Note that the decomposition temperature refers to a temperature at which the half life is 3 minutes. However, needless to say, at the foaming temperature, the foamable resin composition is in a foamable state.
【0049】次に、発泡性樹脂組成物を未発泡のまま供
給する方法としては、例えば、熱可塑性樹脂に発泡剤
を、発泡剤の発泡温度以下の温度で、混練又は含浸させ
ることにより発泡性樹脂組成物を得、これを、ペレット
状、シート状、ロッド状、パイプ状等所望の形状で供給
する方法が挙げられる。Next, as a method of supplying the foamable resin composition in an unfoamed state, for example, the foaming agent is kneaded or impregnated with a thermoplastic resin at a temperature lower than the foaming temperature of the foaming agent. A method of obtaining a resin composition and supplying the resin composition in a desired shape such as a pellet, a sheet, a rod, a pipe, or the like can be given.
【0050】発泡性樹脂組成物は、発泡した際、中空状
体内部が充満するだけの量を供給する必要はない。中空
状体は金型等の規制体に規制されることにより所望形状
に賦形されるのであるが、該規制体に押し当てられるだ
けの発泡圧が得られるだけの量を添加すればよく、例え
ば、金型コアを金型冷却部位まで延長し発泡を規制し
て、最終成形体随所に空隙部分を成形させてもよいし、
発泡性樹脂組成物の供給量又は中空状体の引取速度を変
化させることにより、得られる繊維強化熱可塑性樹脂発
泡体の芯材層中に、発泡性樹脂組成物が発泡充満した部
位と非充満部位を任意に成形させてもよい。本発明にお
いて、発泡圧とは、発泡性樹脂組成物のみにより生じる
発泡圧のみならず、発泡性樹脂組成物のみの発泡圧のみ
では、中空状体を規制体に押しつけるだけの圧が得られ
ない場合は、別途内部へ圧力をかけるが、かかる場合
は、その圧力を付加した圧力をいう。内部に別途圧力を
かける場合は、規制体内部を通じて空気配管を施し、中
空状体内部に気体を供給できる規制体構造とすることが
好ましい。When the foamable resin composition is foamed, it is not necessary to supply an amount sufficient to fill the inside of the hollow body. The hollow body is shaped into a desired shape by being regulated by a regulating body such as a mold, but it is sufficient to add an amount sufficient to obtain a foaming pressure enough to be pressed against the regulating body, For example, the mold core may be extended to the mold cooling portion to restrict foaming, and a void portion may be formed everywhere in the final molded body,
By changing the supply amount of the foamable resin composition or the take-up speed of the hollow body, the core material layer of the obtained fiber-reinforced thermoplastic resin foam has a foam-filled portion and a non-filled portion of the foamable resin composition. The site may be arbitrarily shaped. In the present invention, the foaming pressure means not only the foaming pressure generated by the foamable resin composition alone, but also the foaming pressure of the foamable resin composition alone does not provide a pressure enough to press the hollow body against the regulating body. In such a case, pressure is separately applied to the inside. In such a case, the pressure refers to the pressure added. When pressure is separately applied to the inside, it is preferable that an air pipe is provided through the inside of the restricting body so that a gas is supplied to the inside of the hollow body.
【0051】中空状体内面に供給された未発泡の発泡性
樹脂組成物を発泡させる方法としては、特に限定されな
いが、例えば、中空状体内部又は/及び外部から熱風を
吹き込む方法が挙げられる。なお、発泡させつつ発泡性
樹脂組成物を供給する際も必要に応じて、中空状体を加
熱してもよい。The method of foaming the unfoamed foamable resin composition supplied to the inner surface of the hollow body is not particularly limited, and examples thereof include a method of blowing hot air from inside and / or outside the hollow body. When supplying the foamable resin composition while foaming, the hollow body may be heated as necessary.
【0052】発泡性樹脂組成物を発泡させ、その発泡圧
により、中空状体を所望形状に賦形するのであるが、所
望形状に賦形する方法としては、特に限定されず、例え
ば、中空状体を、断面形状が所望形状を有する金型等の
規制体に供給し、発泡圧により繊維強化熱可塑性樹脂シ
ート等を規制体に押しつけて所望形状に賦形する方法の
他、最終繊維強化熱可塑性樹脂発泡体の所望形状によっ
ては規制体による規制は行わず、発泡圧により中空状体
を賦形する方法等が挙げられる。The foamable resin composition is foamed, and the hollow body is shaped into a desired shape by the foaming pressure. The method for shaping the hollow body into a desired shape is not particularly limited. In addition to the method of supplying the body to a regulating body such as a mold having a desired cross-sectional shape and pressing a fiber-reinforced thermoplastic resin sheet or the like against the regulating body by foaming pressure to form a desired shape, Depending on the desired shape of the plastic resin foam, the regulation by the regulating body is not performed, and a method of shaping the hollow body by the foaming pressure may be used.
【0053】内部芯材層の発泡倍率は、30倍を超える
と発泡層自体が応力を保持できなくなり却って剛性が低
下するので、通常は30倍以下とされるが、補強繊維と
の組み合わせによって最適な倍率を適宜選択することが
でき、好ましくは1.5〜5倍とされる。When the foaming ratio of the inner core material layer exceeds 30 times, the foamed layer itself cannot hold the stress and the stiffness is lowered rather than 30 times. The magnification can be appropriately selected, and is preferably 1.5 to 5 times.
【0054】繊維質シートを用いた場合は、発泡性樹脂
組成物を発泡させながら繊維間に含浸させるのである
が、高発泡倍率の芯材層を得るために、発泡性樹脂組成
物を構成する熱可塑性樹脂に高粘度のものを用いた場
合、熱可塑性樹脂が繊維間に含浸し難いことがあるが、
このような場合には、中空状体を規制する規制体の断面
形状を漸次小さくし、繊維間に溶融熱可塑性樹脂が含浸
しやすいようにする方法が好ましい。具体的には、例え
ば、繊維質シートを連続的に中空状体に賦形した後、中
空状体内面に発泡性樹脂組成物を供給し、発泡性樹脂組
成物を金型内で発泡させるとともに、繊維質シートを内
面方向に絞り込み、発泡性樹脂組成物を構成する熱可塑
性樹脂が繊維質シートに含浸しやすくすることが挙げら
れる。When a fibrous sheet is used, the foamable resin composition is impregnated between the fibers while foaming. In order to obtain a core material layer having a high expansion ratio, the foamable resin composition is formed. When using a high viscosity thermoplastic resin, the thermoplastic resin may be difficult to impregnate between the fibers,
In such a case, it is preferable to use a method in which the cross-sectional shape of the regulating body that regulates the hollow body is gradually reduced so that the molten thermoplastic resin is easily impregnated between the fibers. Specifically, for example, after continuously forming the fibrous sheet into a hollow body, supplying the foamable resin composition to the hollow body surface, and foaming the foamable resin composition in the mold And squeezing the fibrous sheet in the inner surface direction to facilitate the impregnation of the fibrous sheet with the thermoplastic resin constituting the foamable resin composition.
【0055】次に、請求項8に記載の発明について説明
する。請求項8に記載の発明は、1枚又は幅方向におい
て一部相互に重ねられる複数枚の繊維強化熱可塑性樹脂
シートを連続的に中空状に賦形する工程、中空状体内
に、繊維を主成分とするマット状物中に発泡性樹脂組成
物が含浸せしめられてなる、複合発泡性シートを供給
し、中空状体と一体化する工程、及び、複合発泡性シー
トと一体化された中空状体を空気圧成形すると共に、発
泡性樹脂組成物を発泡剤の発泡温度以上に加熱すること
により、中空状体における複合発泡性シートの厚みを拡
張する工程を包含することを特徴とする。Next, the invention according to claim 8 will be described. The invention according to claim 8 is a step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets partially overlapped in the width direction into a hollow shape. A step of supplying a composite foamable sheet in which a foamable resin composition is impregnated in a mat-like substance as a component, and integrating the composite foamable sheet with a hollow body; The thickness of the composite foamable sheet in the hollow body is increased by pneumatically molding the body and heating the foamable resin composition to a temperature equal to or higher than the foaming temperature of the foaming agent.
The method is characterized by including a step of stretching.
【0056】本発明で用いられる繊維強化熱可塑性樹脂
シートは、上記で述べたものと同様のものが用いられ
る。1枚又は幅方向において一部相互に重ねられる複数
枚の繊維強化熱可塑性樹脂シートを連続的に中空状に賦
形する方法、得られた中空状体の形態は、上記で述べら
れたものと同様である。As the fiber reinforced thermoplastic resin sheet used in the present invention, the same one as described above is used. A method for continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets partially overlapped in the width direction into a hollow shape, the form of the obtained hollow body is the same as that described above. The same is true.
【0057】本発明で用いられる複合発泡性シートは、
上記繊維質シートに発泡性樹脂組成物が含浸せしめられ
てなるものである。なお、複合発泡性シートに用いられ
る繊維質シートは、繊維強化熱可塑性樹脂発泡体を構成
する表面層に用いられる場合に比して、若干結着剤が多
い場合がある。上記繊維質シートは、特に限定されず、
例えば、スワルマット、コンティニュアスマット、チョ
ップドストランドマット等が挙げられる。The composite foamable sheet used in the present invention comprises:
The fibrous sheet is impregnated with a foamable resin composition. The fibrous sheet used for the composite foamable sheet may have a slightly larger amount of a binder than that used for the surface layer constituting the fiber-reinforced thermoplastic resin foam. The fibrous sheet is not particularly limited,
For example, a swirl mat, a continuous mat, a chopped strand mat and the like can be mentioned.
【0058】マット状物を構成する繊維の長さは、短く
なると、繊維同士の交絡がなくなり、マット状物が形状
を維持できなくなり、又、長くなると、厚み拡張時、一
方向への優先的な繊維の配向が困難となるので、5〜1
00mmが好ましい。When the length of the fibers constituting the mat-like material is short, the fibers are not entangled with each other, and the shape of the mat-like material cannot be maintained. Since it becomes difficult to orient various fibers,
00 mm is preferred.
【0059】マット状物を構成する繊維の直径は、細く
なると、補強効果が低下し、又、太くなると、マット状
物に形成しにくくなるので、1〜50μmが好ましく、
更に、7〜23μmが好ましい。The diameter of the fibers constituting the mat-like material is preferably from 1 to 50 μm, since the thinner the fiber, the lower the reinforcing effect, and the larger the diameter, the more difficult it is to form the mat-like material.
Further, it is preferably from 7 to 23 μm.
【0060】上記発泡性樹脂組成物は、上述したものと
同様のものが用いられる。上記複合発泡性シートの製造
方法は、特に限定されず、例えば、溶融状態の発泡性樹
脂組成物を、発泡温度より低い温度で、マット状物に供
給した後、加圧することにより、マット状物内部に含浸
させ、複合発泡性シートを製造する方法;粉体状発泡性
樹脂組成物を、振動やエアーによりマット状物内部に供
給した後、発泡温度より低い温度で、更にマット状物に
溶融含浸させて製造する方法が挙げられる。The same foaming resin composition as described above is used. The method for producing the composite foamable sheet is not particularly limited. For example, the foamable resin composition in a molten state is supplied to the mat-like material at a temperature lower than the foaming temperature, and then the matte-like material is pressed. A method for producing a composite foamable sheet by impregnating the inside; supplying the powdery foamable resin composition to the inside of the mat-like material by vibration or air, and then melting the mat-like material at a temperature lower than the foaming temperature. And a method of producing by impregnation.
【0061】本発明では、中空状体内に複合発泡性シー
トを供給し、中空状体と複合発泡性シートを一体化する
のであるが、一体化する方法は、特に限定されず、例え
ば、内部に複合発泡性シートが供給された中空状体を、
入口部横断面より出口部横断面がテーパ状に小さくなる
金型に供給し、金型を、中空状体に用いられる熱可塑性
樹脂又は複合発泡性シートに用いられる熱可塑性樹脂の
融点以上、且つ分解型発泡剤の発泡温度より低い温度に
保持し、一体化する方法;中空状体に用いられる熱可塑
性樹脂又は複合発泡性シートに用いられる熱可塑性樹脂
の融点以上、且つ分解型発泡剤の発泡温度より低い温度
に保持された外部規制体により、外部から中空状体を押
圧することにより一体化する方法等が挙げられる。In the present invention, the composite foamable sheet is supplied into the hollow body, and the hollow body and the composite foamable sheet are integrated. The method of integration is not particularly limited. The hollow body supplied with the composite foamable sheet,
The outlet cross section is supplied to a mold whose taper shape is smaller than the inlet cross section, and the mold is at least the melting point of the thermoplastic resin used for the hollow body or the thermoplastic resin used for the composite foamable sheet, and A method of maintaining and lowering the foaming temperature of the decomposable foaming agent at a temperature lower than the melting temperature of the thermoplastic resin used for the hollow body or the thermoplastic resin used for the composite foamable sheet and foaming the decomposable foaming agent. A method in which a hollow body is pressed from the outside with an external regulating body kept at a temperature lower than the temperature to integrate the hollow body with the outside regulating body, and the like.
【0062】その後、複合発泡性シートと一体化された
中空状体を、空気圧成形し、発泡性樹脂組成物を発泡剤
の発泡温度以上に加熱すると共に、中空状体における複
合発泡性シートの厚みを拡張するのであるが、空気圧成
形、発泡温度以上に加熱する方法は、上記で述べたと同
様に行われる。[0062] Then, a hollow body which is integrated with the composite foamable sheet, with pneumatically molding, heating the foamable resin composition or foaming temperature of the foaming agent, double the hollow body
To expand the thickness of the composite foamable sheet, the method of pneumatic molding and heating to a temperature higher than the foaming temperature is performed in the same manner as described above.
【0063】上記複合発泡性シートの厚みを拡張する方
法は、特に限定されず、例えば、空気圧成形及び発泡圧
により、中空状体の少なくとも一方向の厚みが拡がれば
よく、例えば、中空状体の断面積よりも広い断面積を有
する空気圧成形可能な金型に複合シートと一体化した中
空状体を供給し、空気圧成形及び発泡により、複合発泡
性シートの厚みを拡張する方法が挙げられる。シートの
厚みを拡張する際、中空状体における複合発泡性シート
の厚み方向へのみ優先的に拡張させることは、得られる
繊維強化熱可塑性樹脂発泡体中、特定方向に繊維が優先
的に配向し、圧縮強度が向上し、好適である。The method for expanding the thickness of the composite foamable sheet is not particularly limited. For example, the thickness of the hollow body may be increased in at least one direction by pneumatic molding and foaming pressure. The hollow body integrated with the composite sheet is supplied to a pneumatically moldable mold having a cross-sectional area larger than the cross-sectional area of the body, and the composite foam is formed by pneumatic molding and foaming.
There is a method of expanding the thickness of the conductive sheet . Sheet
When expanding thickness, composite foamable sheet in hollow body
It is preferred that the fibers are preferentially expanded only in the thickness direction because the fibers are preferentially oriented in a specific direction in the obtained fiber-reinforced thermoplastic resin foam, and the compressive strength is improved.
【0064】得られる内部芯材層の発泡倍率は、上記と
同様の理由で、通常30以下、好ましくは、1.5〜5
倍とされる。The expansion ratio of the obtained inner core layer is usually 30 or less, preferably 1.5 to 5 for the same reason as described above.
Doubled.
【0065】[0065]
【作用】本発明の繊維強化熱可塑性樹脂発泡体の製造方
法は、表皮層として、繊維強化熱可塑性樹脂シート等を
使用し、該繊維強化熱可塑性樹脂シート等を中空状体に
賦形し、その内面に発泡性樹脂組成物を供給、発泡さ
せ、その発泡圧により、中空状体を賦形するものであ
る。従って、予め成形された発泡体を用意する必要もな
く、又、発泡圧により中空状体を賦形するものであるた
め、中空状体からなる表皮層の厚みむらが発生しにく
い。According to the method for producing a fiber-reinforced thermoplastic resin foam of the present invention, a fiber-reinforced thermoplastic resin sheet or the like is used as a skin layer, and the fiber-reinforced thermoplastic resin sheet or the like is shaped into a hollow body. The foamable resin composition is supplied to the inner surface and foamed, and the hollow body is shaped by the foaming pressure. Therefore, there is no need to prepare a preformed foam, and since the hollow body is shaped by the foaming pressure, thickness unevenness of the skin layer made of the hollow body hardly occurs.
【0066】表皮層及び芯材層には熱可塑性樹脂を用
い、発泡圧により賦形しているので、製造過程において
所望形状に賦形することが可能であり、複雑な断面形状
を有する繊維強化熱可塑性樹脂発泡体を得ることができ
る。Since a thermoplastic resin is used for the skin layer and the core material layer and is formed by foaming pressure, it can be formed into a desired shape in the manufacturing process, and fiber reinforced having a complicated cross-sectional shape can be formed. A thermoplastic foam can be obtained.
【0067】しかも、発泡性樹脂組成物が発泡する発泡
圧により、溶融状態にある発泡途上の樹脂が、中空状体
を内部から均一な力で押すことにより、表面層と芯材層
が融着一体化したものであるため、表面層と芯材層の界
面において部分的に融着の弱い部分が存在せず、剛性等
の品質の均一な繊維強化熱可塑性樹脂発泡体を得ること
ができる。Furthermore, the foaming resin foaming pressure causes the foaming resin in the molten state to push the hollow body from the inside with a uniform force, so that the surface layer and the core material layer are fused. Since they are integrated, there is no partially weakly fused portion at the interface between the surface layer and the core material layer, and a fiber-reinforced thermoplastic resin foam having uniform quality such as rigidity can be obtained.
【0068】賦形過程で中空状体の延伸を伴う場合、複
数の繊維強化熱可塑性樹脂シート等を、延伸する部分に
対応する様に端部同士を重ね合わせて中空状体に賦形す
ることは、各々の繊維強化熱可塑性樹脂シート間の重な
り部分がずれ、又各々の繊維強化熱可塑性樹脂シートが
わずかづつ延伸することにより、得られる表皮層の薄肉
化を緩和させ、又、表皮層に部分的に大きく薄肉化した
箇所が生ずるのを防止することができる。又、複合シー
トを用いると、表皮層と芯材層との界面に、発泡性樹脂
組成物から生じたガスが残存して、得られる繊維強化熱
可塑性樹脂発泡体の表面層と芯材層との間にボイドが発
生するのを、防止することができる。When the hollow body is stretched during the shaping process, a plurality of fiber-reinforced thermoplastic resin sheets or the like are formed into a hollow body by overlapping the ends so as to correspond to the stretched portion. The overlapping portion between each fiber reinforced thermoplastic resin sheet is shifted, and each fiber reinforced thermoplastic resin sheet is stretched little by little, so that the obtained skin layer can be thinned, and It is possible to prevent the occurrence of a partially large and thin portion. When a composite sheet is used, gas generated from the foamable resin composition remains at the interface between the skin layer and the core material layer, and the surface layer and the core material layer of the obtained fiber-reinforced thermoplastic resin foam. It is possible to prevent voids from being generated between them.
【0069】又、繊維質シートを用いると、発泡性樹脂
組成物が発泡して、繊維質シートの繊維間に樹脂が含浸
するので、予め繊維強化熱可塑性樹脂シート等を製造す
る必要がないので、工程を省くことができる。When a fibrous sheet is used, the foamable resin composition foams and the resin is impregnated between the fibers of the fibrous sheet. Therefore, it is not necessary to manufacture a fiber-reinforced thermoplastic resin sheet or the like in advance. , The process can be omitted.
【0070】中空状体を発泡圧又は/及び空気圧成形に
より賦形することにより、発泡圧だけでは得られなかっ
た、複雑な横断面形状を有する繊維強化熱可塑性樹脂発
泡体を、正確に得ることができる。By forming the hollow body by foaming pressure and / or pneumatic molding, it is possible to accurately obtain a fiber-reinforced thermoplastic resin foam having a complicated cross-sectional shape, which cannot be obtained by foaming pressure alone. Can be.
【0071】繊維強化熱可塑性樹脂シートとして連続繊
維が多数配向したものを用いて、連続繊維が長手方向と
なるように中空状体に賦形することにより、中空状体を
引き抜きつつ、繊維強化熱可塑性樹脂発泡体を製造する
ことができる。中空状体内に複合発泡性シートを供給、
一体化した後、空気圧成形すると共に、発泡させ、発泡
性シートの厚みを拡張させることにより、中空状体内に
供給された複合発泡性シートを構成する繊維が、発泡性
シートの厚み方向に優先的に配向するので、圧縮強度が
向上する。By using a fiber reinforced thermoplastic resin sheet having a large number of continuous fibers oriented and shaping the continuous fibers into a hollow body so as to be in the longitudinal direction, the fiber reinforced thermoplastic resin sheet is drawn out while the hollow body is pulled out. A plastic foam can be manufactured. Supply composite foamable sheet into hollow body,
After integration, pneumatic molding, foaming, foaming
By expanding the thickness of the porous sheet, the fibers constituting the composite foamed sheet supplied into the hollow body become foamable.
Since the sheet is preferentially oriented in the thickness direction of the sheet , the compressive strength is improved.
【実施例】以下に本発明の実施例を記載して本発明を更
に詳しく説明するが、本発明はこれら実施例に限定され
るものではない。なお、図面において、「前」とは、右
方向をいう。EXAMPLES The present invention will be described in more detail with reference to examples of the present invention, but the present invention is not limited to these examples. In the drawings, "front" means rightward.
【0072】(実施例1) 繊維強化熱可塑性樹脂シートを、下記の方法により製造
した。図1に示したように、直径23μmのフィラメン
トより構成されるロービング状のガラス繊維束1(44
00tex)を、24本づつ上下2段に配すると共に、
ポリ塩化ビニル(溶融粘度2.4×105 ポイズ)10
0重量部、錫系熱安定剤1重量部、ポリエチレンWAX
0.5重量部からなる、粒子径約80μmの粉体状樹脂
組成物2が、矢印の方向より圧送されるエアーにより流
動化されている流動槽3中を通過させて、ガラス繊維束
1のフィラメントに粉体状樹脂組成物2を付着させた
後、約200℃に加熱された加熱炉4を通過させること
により加熱、加圧し、樹脂組成物2を溶融、含浸させ
て、厚み1.2mmの繊維強化熱可塑性樹脂シート5を
得た。またガラス繊維束1が流動槽3を通過した後、上
下のガラス繊維束1の間にネット状のガラス繊維6を挟
んだ。繊維強化熱可塑性樹脂シート5中のガラス繊維の
含有率は、30体積%であった。Example 1 A fiber-reinforced thermoplastic resin sheet was produced by the following method. As shown in FIG. 1, a roving-like glass fiber bundle 1 (44) composed of a filament having a diameter of 23 μm.
00tex) are arranged in two rows of 24 pieces each,
Polyvinyl chloride (melt viscosity 2.4 × 10 5 poise) 10
0 parts by weight, 1 part by weight of tin heat stabilizer, polyethylene wax
A powdery resin composition 2 having a particle diameter of about 80 μm consisting of 0.5 parts by weight is passed through a fluidized tank 3 fluidized by air fed from the direction of the arrow to form a glass fiber bundle 1. After the powdery resin composition 2 is adhered to the filament, the resin composition 2 is heated and pressed by passing through a heating furnace 4 heated to about 200 ° C. to melt and impregnate the resin composition 2 to a thickness of 1.2 mm. Thus, a fiber-reinforced thermoplastic resin sheet 5 was obtained. After the glass fiber bundle 1 passed through the fluidizing tank 3, the net-like glass fiber 6 was sandwiched between the upper and lower glass fiber bundles 1. The content of glass fibers in the fiber-reinforced thermoplastic resin sheet 5 was 30% by volume.
【0073】図2に示した繊維強化熱可塑性樹脂シート
の製造装置は、上記の如くして製造された、幅=91m
m、厚み=1.2mmの繊維強化熱可塑性樹脂シート5
が巻回されている巻戻しロール6と、発泡性樹脂組成物
押出用の押出機7と、その前方にまで配置され、先端部
が前向き直角に折曲げられかつその中央部に環状空孔が
設けられた、シート5を円形に賦形することのできる金
型8と、金型8の後端部に固定され、前方に突き出した
垂直断面形状が円形の内コア9と、金型8の前方に断熱
材10、加熱金型11、断熱材12及び冷却金型13を
配し、その前方に引取機14を備えているものである。
加熱金型11の垂直断面形状は、直径29mmの円形で
ある。11よりも前方の断熱材12及び冷却金型13も
同様の断面形状を有している。The apparatus for manufacturing a fiber-reinforced thermoplastic resin sheet shown in FIG. 2 has a width of 91 m manufactured as described above.
m, thickness = 1.2 mm, fiber reinforced thermoplastic resin sheet 5
Roll 6 around which is wound, an extruder 7 for extruding the foamable resin composition, and disposed in front of the rewind roll 6, the front end portion is bent at a right angle forward, and an annular hole is formed in the center portion thereof. A mold 8 provided for forming the sheet 5 into a circular shape, an inner core 9 fixed to the rear end of the mold 8 and projecting forward and having a circular vertical cross section, A heat insulating material 10, a heating mold 11, a heat insulating material 12, and a cooling mold 13 are disposed in front of the apparatus, and a take-off machine 14 is provided in front of the heat insulating material 10, the heating mold 11, and the cooling mold 13.
The vertical sectional shape of the heating mold 11 is a circle having a diameter of 29 mm. The heat insulating material 12 and the cooling mold 13 in front of 11 also have the same cross-sectional shape.
【0074】金型8の後方には繊維強化熱可塑性樹脂シ
ート5を挿入できるU字形の隙間が設けられており、隙
間より繊維強化熱可塑性樹脂シート5を挿入し、金型8
内部でシートをU字形から、シート5の両端部を重ね合
わせずに突き合わせ、外径29.0mm、厚み1.2m
mの中空状体に連続的に賦形し、中空状体に賦形した繊
維強化熱可塑性樹脂シート5の内側に、ポリ塩化ビニル
100重量部、錫系熱安定剤2.5重量部、滑剤0.5
重量部、アクリル加工助剤8重量部、CaCO3 5重量
部、ジオクチルフタレート2重量部、重炭酸ナトリウム
(発泡温度175℃)3.5重量部からなる発泡性樹脂
組成物15を、予め162℃以下の樹脂温度にて、スク
リュー径30mmの2軸押出機にて混練ペレット化した
ものを用い、スクリュー径40mmの単軸押出機(L/
D=30、圧縮比2.5)より樹脂温度200℃にて押
出し積層すると同時に発泡を開始させ、加熱金型11に
より樹脂温度を200℃に保持し発泡を完了させた後、
冷却金型13にて、外層表面温度を60℃にまで冷却
し、芯材層の発泡倍率約3.2倍、断面形状が直径29
mmの円形である、繊維強化熱可塑性樹脂発泡体16を
連続的に成形速度1.5m/minにて成形した。A U-shaped gap in which the fiber-reinforced thermoplastic resin sheet 5 can be inserted is provided behind the mold 8, and the fiber-reinforced thermoplastic resin sheet 5 is inserted through the gap, and the mold 8 is inserted.
Inside, the sheet is abutted from the U-shape without overlapping the both ends of the sheet 5, the outer diameter is 29.0 mm, and the thickness is 1.2 m.
m, and 100 parts by weight of polyvinyl chloride, 2.5 parts by weight of a tin-based heat stabilizer, and a lubricant inside a fiber-reinforced thermoplastic resin sheet 5 formed continuously into a hollow body of m. 0.5
A foamable resin composition 15 consisting of 3 parts by weight, 8 parts by weight of an acrylic processing aid, 5 parts by weight of CaCO3, 2 parts by weight of dioctyl phthalate, and 3.5 parts by weight of sodium bicarbonate (foaming temperature: 175 ° C.) At a resin temperature of 30 kDa, a single screw extruder with a screw diameter of 40 mm (L /
D = 30, compression ratio 2.5), extruded and laminated at a resin temperature of 200 ° C. and started foaming at the same time.
In the cooling mold 13, the outer layer surface temperature is cooled to 60 ° C., and the foaming ratio of the core material layer is about 3.2 times, and the cross-sectional shape is 29 in diameter.
The fiber-reinforced thermoplastic resin foam 16 having a circular shape of mm was continuously molded at a molding speed of 1.5 m / min.
【0075】得られた繊維強化熱可塑性樹脂発泡体16
の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚みの
最大値、最小値及びCV値を以下の方法により測定し、
その結果を表1に示した。The obtained fiber reinforced thermoplastic resin foam 16
The flexural strength, flexural modulus and compressive strength, the maximum value, minimum value and CV value of the thickness of the surface layer were measured by the following methods,
The results are shown in Table 1.
【0076】(曲げ強度、曲げ弾性率) JIS K7221に従って測定した。 (圧縮強度) JIS G3448における偏平試験において、平板の
距離が2/3の高さまで圧縮した時の加重を、その時点
において平板と試験片が接触する面積で除した値を圧縮
強度とした。 (表面層の最大値、最小値) 得られた繊維強化熱可塑性樹脂発泡体から無作為に、1
0か所切り出し、それを更に10分割し、各々の表面層
の厚みを測定し、その最大値及び最小値を採った。 (CV値) 上記測定から、標準偏差及び平均値を求め、下記式によ
りCV値を求めた。CV値=100×標準偏差/平均値 (実施例2) ガラス繊維束1間に、ネット状のガラス繊維6を挟まな
かったこと以外は、実施例1と略同様にして、繊維強化
熱可塑性樹脂シート5を製造した。繊維強化熱可塑性樹
脂シート5中、ガラス繊維の含有量は、50体積%であ
った。実施例1で用いられた製造装置の金型11におい
て、入口断面形状が直径29mmの円形、出口形状が2
7×27mmの矩形となっており、金型内部断面形状
が、漸次入口形状から出口形状へと変化している以外
は、実施例1で用いられた製造装置を用いて、実施例1
と同様にして、芯材層の発泡倍率2.8倍、断面形状が
27×27mmの矩形である、繊維強化熱可塑性樹脂発
泡体16を連続的に成形速度1.2m/minにて成形
した。得られた繊維強化熱可塑性樹脂発泡体16の曲げ
強度及び曲げ弾性率、表面層の厚みの最大値、最小値及
びCV値を実施例1と同様の方法により、又繊維強化熱
可塑性樹脂発泡体16の圧縮強度を下記の方法により測
定し、その結果を表1に示した。 (圧縮強度) JIS K7208に従って測定した。(Bending strength and flexural modulus) Measured according to JIS K7221. (Compression strength) In the flatness test according to JIS G3448, the value obtained by dividing the load when the distance of the flat plate was compressed to a height of 2/3 by the area where the flat plate and the test piece were in contact at that time was defined as the compressive strength. (Maximum value, minimum value of surface layer) From the obtained fiber-reinforced thermoplastic resin foam, 1
0 portions were cut out, further divided into 10 portions, the thickness of each surface layer was measured, and the maximum value and the minimum value were taken. (CV value) From the above measurements, the standard deviation and average value were determined, and the CV value was determined by the following equation. CV value = 100 × standard deviation / average value (Example 2) A fiber-reinforced thermoplastic resin was prepared in substantially the same manner as in Example 1 except that the glass fibers 6 in a net shape were not sandwiched between the glass fiber bundles 1. Sheet 5 was produced. The content of glass fibers in the fiber-reinforced thermoplastic resin sheet 5 was 50% by volume. In the mold 11 of the manufacturing apparatus used in Example 1, the inlet cross-sectional shape was a circular shape having a diameter of 29 mm, and the outlet shape was 2 mm.
Example 1 was performed using the manufacturing apparatus used in Example 1 except that the shape was a 7 × 27 mm rectangle, and the internal shape of the mold gradually changed from the inlet shape to the outlet shape.
In the same manner as described above, a fiber-reinforced thermoplastic resin foam 16 having a core material layer having a foaming ratio of 2.8 times and a cross-sectional shape of 27 × 27 mm was continuously molded at a molding speed of 1.2 m / min. . The flexural strength and flexural modulus, the maximum value, the minimum value and the CV value of the thickness of the surface layer of the obtained fiber-reinforced thermoplastic resin foam 16 were measured in the same manner as in Example 1, and the fiber-reinforced thermoplastic resin foam was used. 16 was measured by the following method, and the results are shown in Table 1. (Compressive strength) Measured according to JIS K7208.
【0077】(実施例3) 繊維強化樹脂シートを、予め製造した3枚の繊維強化熱
可塑性樹脂予備シートを。加熱、加圧し一体化して得
た。繊維強化熱可塑性樹脂予備シートの製造には、図3
に示した製造装置を用いた。流動槽17と、流動槽17
の後方に、平行して配置された複数の巻き戻しロール1
8と、各流動槽装置の前方に配置された引き取り駆動ロ
ール19(場合によっては、引取駆動ロール19、1
9)と、引取駆動ロール19の前にこれと対峙せしめら
れたロータリー・カッター20と、所定間隔をおいて対
向せしめられた上下無端ベルト21、22と、両無端ベ
ルト21、22の対向移送部に対して配された加熱炉2
3、厚み調整機28及び上下冷却ガイド・ロール24と
を備えており、下無端ベルト22の後方には送り込み部
22bが設けられ、送り込み部22bは、ロータリー・
カッター20の下方に位置せしめられていた。(Example 3) Three fiber reinforced thermoplastic resin spare sheets which were produced in advance from a fiber reinforced resin sheet were used. Heating, pressurizing and integrating were obtained. For the production of the fiber reinforced thermoplastic resin spare sheet, FIG.
Was used. Fluidized vessel 17 and fluidized vessel 17
Behind, a plurality of rewinding rolls 1 arranged in parallel
8 and take-up drive rolls 19 (in some cases, take-up drive rolls 19, 1
9), a rotary cutter 20 opposed to the take-up drive roll 19 and opposed thereto, upper and lower endless belts 21 and 22 opposed to each other at a predetermined interval, and an opposing transfer portion of both endless belts 21 and 22. Heating furnace 2 arranged for
3, a thickness adjuster 28 and a vertical cooling guide roll 24, and a feed portion 22b is provided behind the lower endless belt 22, and the feed portion 22b is
It was located below the cutter 20.
【0078】両無端ベルト21、22は、モーターで上
下各複数のプーリー27のうち上下各1つを駆動するこ
とにより、連続して同方向へほぼ同速度で移動するよう
になされているものであった。また上無端ベルト21の
移送部21aの後部は、後上向きに傾斜せしめられてお
り、上下移送部21a、22aの間隙が後方に向かって
広がっている。上下無端ベルト21、22は、高強度で
耐熱性のある、スチールで形成されていた。加熱炉23
は熱風循環式のものが用いられ、これの中を上下無端ベ
ルト21、22の上下移送部21a、22aが通過して
いた。The two endless belts 21 and 22 are configured to move continuously in the same direction at substantially the same speed by driving one of the upper and lower pulleys 27 by a motor. there were. The rear part of the transfer section 21a of the upper endless belt 21 is inclined rearward and upward, and the gap between the upper and lower transfer sections 21a and 22a is widened rearward. The upper and lower endless belts 21 and 22 were formed of steel having high strength and heat resistance. Heating furnace 23
The hot air circulation type was used, and the upper and lower transfer portions 21a and 22a of the upper and lower endless belts 21 and 22 passed through this.
【0079】上記装置において、巻き戻しロール18よ
り巻き戻されたロービング状ガラス繊維束よりなる強化
繊維束25A(繊維の直径17μm)15本を流動槽装
置17に導き、流動状態となった、冷凍粉砕した高密度
ポリエチレン(溶融粘度1.1×105 ポイズ)粒子2
6を開繊しながら通過させ、樹脂と強化繊維の割合を
3:2(容積比)となるように樹脂を付着させた。樹脂
付着繊維束25Bをロータリー・カッター20によりそ
れぞれ37.5mmに切断し、切断樹脂付着繊維束25
Cを上下無端ベルト21、22の間隙への送り込み部2
2b上に落下させて集積し、切断樹脂付着繊維束集積物
25Dを、移動する両無端ベルト21、22で挟みなが
ら厚み方向に加圧して熱風が循環している加熱炉23中
を通過させた。引き続いて、溶融状態にある樹脂と強化
繊維束の混合物を加圧しつつ冷却し、熱可塑性樹脂に長
さ37.5mmの強化繊維がランダムな状態で配されて
いる厚み0.5mmの繊維強化熱可塑性樹脂予備シート
25Eを得た。繊維強化熱可塑性樹脂予備シート25E
中、ガラス繊維の含有量は、40体積%であった。又、
粉体状樹脂組成物として、粒子径80μmの高密度ポリ
エチレンを用い、厚さが0.3mmとなるように調整し
た以外は、実施例2と同様にして、繊維強化熱可塑性樹
脂予備シート25Fを得た。繊維強化熱可塑性樹脂予備
シート25Eを、2枚の繊維強化熱可塑性樹脂予備シー
ト25Fで挟み、一体化させ、厚さ1.2mmの繊維強
化熱可塑性樹脂シート5を得た。In the above apparatus, fifteen reinforcing fiber bundles 25A (having a fiber diameter of 17 μm) made of roving glass fiber bundles unwound from the unwinding roll 18 are guided to the fluidizing tank device 17, where the freezing state is achieved. Ground high-density polyethylene (melt viscosity 1.1 × 10 5 poise) particles 2
6 was allowed to pass through the fiber while being opened, and the resin was adhered so that the ratio of the resin to the reinforcing fibers was 3: 2 (volume ratio). The resin-attached fiber bundle 25B is cut into 37.5 mm by the rotary cutter 20, and the cut resin-attached fiber bundle 25B is cut.
C feeding section 2 into the gap between upper and lower endless belts 21 and 22
2b, the cut resin-attached fiber bundle stack 25D was pressed in the thickness direction while being sandwiched between the moving endless belts 21 and 22, and passed through a heating furnace 23 in which hot air was circulating. . Subsequently, the mixture of the resin and the reinforcing fiber bundle in the molten state is cooled while being pressurized, and the reinforcing fiber having a length of 37.5 mm is randomly distributed in the thermoplastic resin. A plastic resin spare sheet 25E was obtained. Fiber reinforced thermoplastic resin spare sheet 25E
Medium, the content of glass fiber was 40% by volume. or,
The same procedure as in Example 2 was repeated except that high-density polyethylene having a particle diameter of 80 μm was used as the powdery resin composition and the thickness was adjusted to 0.3 mm. Obtained. The fiber-reinforced thermoplastic resin preliminary sheet 25E was sandwiched between two fiber-reinforced thermoplastic resin preliminary sheets 25F and integrated to obtain a fiber-reinforced thermoplastic resin sheet 5 having a thickness of 1.2 mm.
【0080】高密度ポリエチレン100重量部、ホモプ
ロピレン100重量部、シラン架橋性ポリプロピレン樹
脂30重量部、アゾジカルボンアミド(発泡温度190
℃)5重量部、ガラス繊維(フィラメント直径14μ
m、繊維長2mm)10重量部を、スクリュー径30m
mの二軸押出機に供給し、175℃にて溶融混練後、ペ
レット化し、このペレットを、100℃の熱水に1時間
浸漬した後、乾燥させ、発泡性樹脂組成物を得た。100 parts by weight of high-density polyethylene, 100 parts by weight of homopropylene, 30 parts by weight of a silane crosslinkable polypropylene resin, azodicarbonamide (foaming temperature: 190
° C) 5 parts by weight, glass fiber (filament diameter 14μ)
m, fiber length 2 mm) 10 parts by weight, screw diameter 30 m
m, and the mixture was melt-kneaded at 175 ° C., pelletized, immersed in hot water at 100 ° C. for 1 hour, and dried to obtain a foamable resin composition.
【0081】図2において、上記ペレットをスクリュー
直径40mmの単軸押出機(L/D=30、圧縮比2.
5)に供給、165℃で溶融混練し、未発泡のまま、押
出積層後、205℃に温度制御された加熱金型11にて
加熱し、発泡を開始させ、発泡樹脂が中空状体内面に充
満後に、冷却金型13に導入し、表面を60℃にまで冷
却させ、又、図示されていないが、金型コア9内部に金
型コア9後方より通気孔を設け、金型コア9の先端付近
に形成される空間の圧力を1.3kg/cm2に調節
し、加熱金型11及び冷却金型13のうち、中空状体が
接触する面はテトラフルオロエチレンで覆い、成形速度
を1.8m/minとした以外は、実施例2と同様にし
て、芯材層の発泡倍率2.9倍、断面形状が27×27
mmの矩形である、繊維強化熱可塑性樹脂発泡体16を
得た。In FIG. 2, the above pellets were extruded from a single screw extruder having a screw diameter of 40 mm (L / D = 30, compression ratio 2.
5) melt-kneaded at 165 ° C., extruded and laminated in an unfoamed state, and then heated by a heating mold 11 temperature-controlled at 205 ° C. to start foaming, and the foamed resin is deposited on the hollow body surface. After filling, the mixture is introduced into a cooling mold 13 and the surface is cooled to 60 ° C. Further, although not shown, a ventilation hole is provided inside the mold core 9 from the rear of the mold core 9 to form the mold core 9. The pressure of the space formed near the tip was adjusted to 1.3 kg / cm 2, and the surface of the heating mold 11 and the cooling mold 13 that contacted the hollow body was covered with tetrafluoroethylene, and the molding speed was increased to 1. Except for 8 m / min, in the same manner as in Example 2, the expansion ratio of the core material layer was 2.9 times, and the cross-sectional shape was 27 × 27.
Thus, a fiber-reinforced thermoplastic resin foam 16 having a rectangular shape of mm was obtained.
【0082】得られた繊維強化熱可塑性樹脂発泡体16
の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚みの
最大値、最小値及びCV値を実施例2と同様の方法によ
り測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 16
The flexural strength, flexural modulus and compressive strength, and the maximum, minimum and CV values of the thickness of the surface layer were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0083】(実施例4) 熱可塑性樹脂として、平均粒径100μmの冷凍粉砕さ
れたポリプロピレン(溶融粘度1.6×105 )を用い
た以外は、実施例2と同様にして、繊維強化熱可塑性樹
脂シートを製造して、これを、29Aとした。繊維強化
熱可塑性樹脂シート29A中、ガラス繊維の含有量は4
0体積%であった。図4(イ)に示した繊維強化熱可塑
性樹脂発泡体の製造装置は、繊維強化熱可塑性樹脂シー
ト29Aが巻回されている巻戻しロール29、その前方
に配置され、先端部が前向きに折曲げられた、シート2
9Aを矩形に賦形することのできる内層発泡性樹脂組成
物供給装置30、繊維強化熱可塑性樹脂シート29Aの
端部同士を押圧するロール31、断面形状が幅50×厚
み25mmの長方形からやや大きめの幅60×厚み30
mmの長方形であって、図4(ロ)に示すような、両下
角欠けた形状に緩やかに変化する賦形金型32、賦形金
型32を包囲する、賦形金型32を加熱するハンドヒー
ター40、その前方に断熱材33、冷却金型34を配
し、その前方に引取機35を備えているものであった。
供給装置30は、発泡性樹脂組成物供給路37、通気孔
38と、図示しないが、その前方にエアーだけを通じる
ことができるメッシュを有していた。更に、シート端部
の重なり部分を加熱する熱風加熱装置36を設けられ、
又、図示していないが、供給装置30にシートを囲繞し
矩形に賦形するためのガイドロールが配されていた。Example 4 A fiber-reinforced thermoplastic resin was prepared in the same manner as in Example 2 except that a frozen and pulverized polypropylene having an average particle size of 100 μm (melt viscosity: 1.6 × 10 5) was used as the thermoplastic resin. A resin sheet was manufactured and this was designated as 29A. In the fiber-reinforced thermoplastic resin sheet 29A, the content of glass fiber is 4
It was 0% by volume. The apparatus for manufacturing a fiber-reinforced thermoplastic resin foam shown in FIG. 4A is provided with a rewinding roll 29 around which a fiber-reinforced thermoplastic resin sheet 29A is wound, and is disposed in front of the rewinding roll 29, and has a front end folded forward. Bent, sheet 2
An inner layer foamable resin composition supply device 30 capable of shaping 9A into a rectangle, a roll 31 pressing the end portions of the fiber-reinforced thermoplastic resin sheet 29A, a cross-sectional shape slightly larger than a rectangle having a width of 50 × 25 mm in thickness. Width 60 x thickness 30
As shown in FIG. 4 (b), the shaping mold 32 which gradually changes to a shape lacking both lower corners and which surrounds the shaping mold 32 is heated. A hand heater 40, a heat insulating material 33 and a cooling mold 34 are disposed in front of the hand heater 40, and a take-off device 35 is provided in front of the hand heater 40.
The supply device 30 had a foamable resin composition supply passage 37, a vent hole 38, and a mesh (not shown) that could allow only air to pass in front of it. Further, a hot air heating device 36 for heating the overlapping portion of the sheet end is provided,
Although not shown, the supply device 30 is provided with a guide roll for surrounding the sheet and shaping the sheet into a rectangle.
【0084】上記で得られた繊維強化熱可塑性樹脂シー
ト29Aを、連続的に矩形形状に賦形し、重ね合わせ部
を150℃の熱風加熱装置36により加熱した後、ロー
ル31により密着させ、中空状体に賦形した。この中空
状体を連続的に引き取り、賦形金型32に引き込むと同
時に、発泡性樹脂組成物供給路37を通じて、発泡性樹
脂組成物39(高密度ポリエチレン100重量部、ホモ
ポリプロピレン100重量部、シラン架橋性ポリプロピ
レン30重量部、アゾジカルボンアミド(発泡温度19
0℃)を、実施例3と同様にして、ペレット化したも
の)を、樹脂温180℃で未発泡のまま、中空状体の内
面に供給し、バンドヒーター40により賦形金型32を
205℃に加熱し、該金型32内部、特に断面形状が緩
やかに変化する部分において発泡樹脂組成物の発泡が開
始するように、引き取り速度を調節しつつ発泡性樹脂組
成物を発泡させた。発泡樹脂は、繊維強化熱可塑性樹脂
シート29Aを幅方向に延伸させると同時に、発泡圧に
より金型32内面に押し当て賦形した。これを引き取
り、水温5℃の冷却水が循環する冷却金型34に引き込
み、表面層が約40℃になるまで冷却することにより、
成形速度は0.5m/minで、芯材層の発泡倍率が
2.85倍である、繊維強化熱可塑性樹脂発泡体41を
連続的に得た。The fiber-reinforced thermoplastic resin sheet 29A obtained above is continuously shaped into a rectangular shape, and the overlapped portion is heated by a hot air heating device 36 at 150 ° C. It was shaped into a shape. The hollow body is continuously taken out and drawn into the shaping mold 32, and at the same time, the foamable resin composition 39 (100 parts by weight of high-density polyethylene, 100 parts by weight of homopolypropylene, 30 parts by weight of silane crosslinkable polypropylene, azodicarbonamide (foaming temperature 19
(0 ° C.) in the same manner as in Example 3, and pelletized) is supplied to the inner surface of the hollow body while the resin temperature is 180 ° C., while not foaming. The foamable resin composition was foamed while controlling the take-up speed so that the foaming resin composition began to foam at the inside of the mold 32, particularly at a portion where the cross-sectional shape gradually changed. The foamed resin was formed by stretching the fiber-reinforced thermoplastic resin sheet 29A in the width direction and pressing the foamed resin against the inner surface of the mold 32 by foaming pressure. This is taken and taken into a cooling mold 34 in which cooling water having a water temperature of 5 ° C. circulates, and cooled until the surface layer reaches about 40 ° C.
A molding speed was 0.5 m / min, and a fiber-reinforced thermoplastic resin foam 41 having a foaming ratio of the core material layer of 2.85 times was continuously obtained.
【0085】得られた繊維強化熱可塑性樹脂発泡体41
の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚みの
最大値、最小値及びCV値を実施例2と同様の方法によ
り測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 41
The flexural strength, flexural modulus and compressive strength, and the maximum, minimum and CV values of the thickness of the surface layer were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0086】(実施例5) 粉体状樹脂組成物として、ポリプロピレン(溶融粘度
1.6×105 ポイズ)を用いた以外は、実施例1と同
様にして、繊維強化熱可塑性樹脂シートを得て、これを
42Bとした。更に、高密度ポリエチレン100重量
部、シラン架橋性ポリプロピレン樹脂15重量部、アゾ
ジカルボンアミド(発泡温度190℃)5重量部、ガラ
ス繊維(フィラメント直径14、繊維長5mm)10重
量部を、スクリュー径30mmの二軸押出機に供給し、
170℃の温度で溶融加熱後、上記繊維強化熱可塑性樹
脂シート42Bに厚み1mmのシート状で押出積層し、
繊維強化熱可塑性樹脂層42Bの一面に発泡性樹脂組成
物層42Cが積層された、厚み2mm、幅204mmの
複合シート42Aを得、得られた複合シートを100℃
の熱水に1時間浸漬後、乾燥させた。得られた複合シー
ト42Aの一端部には、図5(ニ)の如く、幅20mm
の発泡性樹脂組成物層が積層されていないものであっ
た。Example 5 A fiber-reinforced thermoplastic resin sheet was obtained in the same manner as in Example 1, except that polypropylene (melt viscosity: 1.6 × 10 5 poise) was used as the powdery resin composition. This was designated as 42B. Further, 100 parts by weight of high-density polyethylene, 15 parts by weight of silane crosslinkable polypropylene resin, 5 parts by weight of azodicarbonamide (foaming temperature 190 ° C.), 10 parts by weight of glass fiber (filament diameter 14, fiber length 5 mm), screw diameter 30 mm To the twin screw extruder,
After being melted and heated at a temperature of 170 ° C., the fiber-reinforced thermoplastic resin sheet 42B is extrusion-laminated in a sheet shape having a thickness of 1 mm,
A composite sheet 42A having a thickness of 2 mm and a width of 204 mm, in which a foamable resin composition layer 42C is laminated on one surface of a fiber-reinforced thermoplastic resin layer 42B, is obtained.
Immersed in hot water for 1 hour and dried. At one end of the obtained composite sheet 42A, as shown in FIG.
No foamable resin composition layer was laminated.
【0087】実施例5において用いられた製造装置を図
5(イ)に示す。製造装置は、上記で得られた複合シー
ト42Aが巻回されている巻戻しロール42aと、その
先端部が前向き直角に折り曲げられ、且つその内部に吸
気孔46、排気孔47が設けられた、複合シート42A
を中空状に賦形することのできる金型43と、その周囲
に金型43に沿って、複合シート42Aを中空状に賦形
するためのガイドロール54と、複合シート42Aの端
部同士を重ね合わせた部分を加熱するための加熱装置4
5と、加熱装置45により加熱した重ね合わせ部分を圧
着する加圧ロール44と、入口断面形状が、図5(ロ)
に示すような楕円形をしており、前方になるにつれ、漸
次変化し、出口形状が図5(ハ)に示すような断面形状
となる、加熱金型48と、ヒーター49と、図5(ハ)
に示す断面形状を有する、断熱材50、冷却金型51及
び引取機53とを有するものである。FIG. 5A shows the manufacturing apparatus used in the fifth embodiment. The manufacturing apparatus has a rewind roll 42a around which the composite sheet 42A obtained above is wound, and a front end portion thereof is bent forward and at a right angle, and an intake hole 46 and an exhaust hole 47 are provided therein. Composite sheet 42A
Can be formed into a hollow shape, a guide roll 54 for forming the composite sheet 42A into a hollow shape along the die 43 around the die 43, and the ends of the composite sheet 42A are connected to each other. Heating device 4 for heating the superposed part
5, a pressure roll 44 for pressing the overlapped portion heated by the heating device 45, and an inlet cross-sectional shape shown in FIG.
The heating mold 48, the heater 49, and the heating die 48 shown in FIG. 5 (c) have an elliptical shape as shown in FIG. C)
A heat insulating material 50, a cooling mold 51, and a take-off machine 53 having a cross-sectional shape shown in FIG.
【0088】複合シート42Aを、金型43及びガイド
ロール54により、図5(ニ)に示すように、発泡性樹
脂組成物層が内側となり且つ発泡性樹脂組成物層が積層
されていない部分が重ね合わせ部となるように中空状に
賦形後、重ね合わせ部を加熱装置45で190℃に加熱
し、加圧ロール44により圧着した。更に、得られた中
空状体を、200℃に加熱された金型48に供給すると
共に、吸気孔46より225℃の熱風を中空状体内部に
吸引すると共に、排気孔47より排気を行い、発泡性樹
脂組成物層を発泡させ、発泡が完了した後、冷却金型5
1により外層表面温度を60℃にまで冷却し、芯材層の
発泡倍率が4.7倍である、繊維強化熱可塑性樹脂発泡
体52を成形速度1.2m/minにて成形した。得ら
れた繊維強化熱可塑性樹脂発泡体52の曲げ強度、曲げ
弾性率及び圧縮強度、表面層の厚みの最大値、最小値及
びCV値を実施例2と同様の方法により測定し、その結
果を表1に示した。As shown in FIG. 5 (d), the composite sheet 42A is separated by the mold 43 and the guide roll 54 into a portion where the foamable resin composition layer is inside and the foamable resin composition layer is not laminated. After shaping into a hollow shape so as to form an overlapping portion, the overlapping portion was heated to 190 ° C. by a heating device 45 and pressed by a pressure roll 44. Further, the obtained hollow body is supplied to a mold 48 heated to 200 ° C., and at the same time, 225 ° C. hot air is sucked into the hollow body through the intake hole 46 and exhausted through the exhaust hole 47. After the foaming resin composition layer is foamed and the foaming is completed, the cooling mold 5
The surface temperature of the outer layer was cooled to 60 ° C. according to 1 and a fiber-reinforced thermoplastic resin foam 52 having a core material layer expansion ratio of 4.7 times was molded at a molding speed of 1.2 m / min. The bending strength, bending elastic modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 52, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were obtained. The results are shown in Table 1.
【0089】(実施例6) 繊維質シートとして、モノフィラメント径9μmの連続
ガラス繊維束をランダムに配向させてエポキシ樹脂系結
着剤で保持したコンティニュアスマット(目付重量45
0g/m2 、幅94.2mm、)を用いた。繊維強化熱
可塑性樹脂発泡体の製造装置は図6に示したように、繊
維質シート繰り出し機55、発泡性樹脂組成物押出用押
出機56、発泡性樹脂組成物押出用金型57、加熱冷却
金型58、引き取り機59よりなる。発泡性樹脂組成物
押出用金型57は、U字形の繊維質シート挿入部60か
ら発泡性樹脂組成物流路62の出口にわたって繊維質シ
ート61を通過させると、発泡性樹脂組成物押出用金型
57内部で徐々に筒状に賦形され、端部と端部が突き合
わされて完全な筒状となる構造になっており、繊維質シ
ート61が完全な筒状にならない部分で発泡性樹脂組成
物押出用押出機56と連結されている。Example 6 As a fibrous sheet, a continuous mat (basis weight 45) in which a continuous glass fiber bundle having a monofilament diameter of 9 μm was randomly oriented and held with an epoxy resin binder was used.
0 g / m @ 2, width 94.2 mm). As shown in FIG. 6, the apparatus for producing a fiber-reinforced thermoplastic resin foam includes a fibrous sheet feeder 55, an extruder 56 for extruding an expandable resin composition, a mold 57 for extruding an expandable resin composition, heating and cooling. It comprises a mold 58 and a take-up machine 59. When the fibrous sheet 61 passes from the U-shaped fibrous sheet insertion section 60 to the outlet of the foamable resin composition flow path 62, the foamable resin composition extrusion mold 57 is 57 is gradually formed into a tubular shape, and the end portion is abutted against each other to form a complete tubular shape. The portion where the fibrous sheet 61 does not become a complete tubular shape is a foamable resin composition. It is connected to an extruder 56 for extruding a product.
【0090】発泡性樹脂組成物流路62は、押出機56
と発泡性樹脂組成物押出用金型57の連結部から繊維質
シート61が完全に筒状になる部分まで設けられてお
り、筒状となった繊維質シート61の内面側に直径5m
mのストランド状で発泡性樹脂組成物を押出せる構造に
なっている。The flow path 62 of the foamable resin composition is
And a portion from which the fibrous sheet 61 is completely cylindrical to the portion where the fibrous sheet 61 is completely cylindrical.
The structure is such that the foamable resin composition can be extruded in a strand shape of m.
【0091】加熱冷却金型58は金型断面状が製品形状
となっており、ヒーターによる加熱と、通水による冷却
が可能である。発泡性樹脂組成物押出用金型57の発泡
性樹脂組成物押出部分の断面形状及び加熱冷却金型58
の断面形状は、直径30mmの円とした。The heating / cooling mold 58 has a product sectional shape, and can be heated by a heater and cooled by passing water. Sectional Shape of Extruded Portion of Foamable Resin Composition of Mold 57 for Foamable Resin Composition Extrusion and Heating / Cooling Mold 58
Was a circle having a diameter of 30 mm.
【0092】180℃に温度調節した発泡性樹脂組成物
押出用金型57に繊維質シート挿入部から繊維質シート
61を挿入し、金型内で中空状体とした後、発泡性樹脂
組成物(ポリ塩化ビニル100重量部、錫系熱安定剤
2.5重量部、滑剤1重量部、アクリル加工助剤12重
量部、CaCO3 2重量部、ジオクチルフタレート2重
量部、重炭酸ナトリウム(発泡温度175℃)5重量部
を、スーパーミキサーで温度100℃になるまで攪拌、
混合したもの)を、発泡性樹脂組成物押出用押出機56
から、金型57の流路62を経て、185℃で発泡させ
ながら、中空状体内面に供給した。The fibrous sheet 61 is inserted from the fibrous sheet insertion portion into the foaming resin composition extrusion die 57 adjusted to a temperature of 180 ° C. to form a hollow body in the die. (100 parts by weight of polyvinyl chloride, 2.5 parts by weight of a tin-based heat stabilizer, 1 part by weight of a lubricant, 12 parts by weight of an acrylic processing aid, 2 parts by weight of CaCO3, 2 parts by weight of dioctyl phthalate, sodium bicarbonate (foaming temperature: 175 5 ° C.) with a supermixer until the temperature reaches 100 ° C.
Extruder 56 for extruding a foamable resin composition.
After that, the mixture was supplied to the hollow inner surface while foaming at 185 ° C. through the flow path 62 of the mold 57.
【0093】発泡性樹脂組成物押出後、発泡性樹脂組成
物押出用金型57に連結した加熱冷却金型58に導入
し、180℃に加熱した加熱部で発泡を継続させながら
コンティニュアスマットに、発泡したポリ塩化ビニルを
含浸させつつ発泡圧で押圧し、10℃に冷却した冷却部
で表面温度が70℃になるまで冷却し、繊維強化熱可塑
性樹脂発泡体59Aを得た。得られた繊維強化熱可塑性
樹脂発泡体は、加熱冷却金型面で押し当てられ高密度と
なったガラス繊維含有ポリ塩化ビニルからなる表面層の
内側に、ポリ塩化ビニル発泡体からなる芯材層を有する
2層構造であり、芯材層の発泡倍率は、3.55倍であ
った。After extruding the foamable resin composition, the foamed resin composition is introduced into a heating / cooling mold 58 connected to a mold 57 for extruding the foamable resin composition, and is formed into a continuous mat while continuing foaming in a heating section heated to 180 ° C. The foamed polyvinyl chloride was impregnated and pressed by a foaming pressure, and cooled to a surface temperature of 70 ° C. in a cooling unit cooled to 10 ° C. to obtain a fiber-reinforced thermoplastic resin foam 59A. The obtained fiber-reinforced thermoplastic resin foam is pressed against the heating / cooling mold surface and becomes a high-density glass fiber-containing polyvinyl chloride inside a surface layer made of a polyvinyl chloride foam core material layer. And the expansion ratio of the core material layer was 3.55 times.
【0094】得られた繊維強化熱可塑性樹脂発泡体59
Aの曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚み
の最大値、最小値及びCV値を実施例1と同様の方法に
より測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 59
The flexural strength, flexural modulus and compressive strength of A, and the maximum, minimum and CV values of the thickness of the surface layer were measured in the same manner as in Example 1, and the results are shown in Table 1.
【0095】(実施例7) 繊維質シート64は、実施例5と同じものを用いた。用
いた製造過程を図7に示した。発泡性樹脂組成物押出用
金型63は、実施例5で同じ構造である。樹脂押出孔6
5の出口部分での繊維質シート賦形路の断面形状は、周
長109.9mmの円形であり、樹脂押出孔65の部分
から発泡性樹脂組成物押出用金型63に接続されている
加熱冷却金型66にかけて、周長92.4mmの円形に
まで絞り込まれ、断面形状が周長92.4mmの円形で
ある、加熱冷却金型66へ導かれる。(Example 7) The same fibrous sheet 64 as in Example 5 was used. The manufacturing process used is shown in FIG. The foaming resin composition extrusion die 63 has the same structure as that of the fifth embodiment. Resin extrusion hole 6
The cross-sectional shape of the fibrous sheet forming path at the exit portion of No. 5 is a circle with a circumference of 109.9 mm, and the heating is connected to the foaming resin composition extrusion die 63 from the resin extrusion hole 65. It is narrowed down to a circular shape having a peripheral length of 92.4 mm by the cooling die 66, and is guided to a heating / cooling die 66 having a circular shape having a peripheral length of 92.4 mm.
【0096】発泡性樹脂組成物として、ポリ塩化ビニル
100重量部、錫系熱安定剤2.5重量部、滑剤0.6
重量部、アクリル加工助剤3重量部、CaCO3 5重量
部、ジオクチルフタレート1重量部、重炭酸ナトリウム
(発泡温度175℃)5重量部を、スーパーミキサーで
温度100℃になるまで攪拌、混合したものものを用
い、製造装置として、上記装置を用いた他、温度条件等
は実施例6と同様にして繊維強化熱可塑性樹脂発泡体6
7を得た。加熱冷却金型66に押し当てられ高密度とな
ったガラス繊維含有ポリ塩化ビニルからなる表面層内側
に、ポリ塩化ビニル発泡体からなる芯材層を有する2層
構造であり、芯材層の発泡倍率は、3.73倍であっ
た。As a foamable resin composition, 100 parts by weight of polyvinyl chloride, 2.5 parts by weight of a tin-based heat stabilizer, 0.6 parts by weight of a lubricant
Parts by weight, 3 parts by weight of an acrylic processing aid, 5 parts by weight of CaCO3, 1 part by weight of dioctyl phthalate, and 5 parts by weight of sodium bicarbonate (foaming temperature: 175 ° C) were stirred and mixed by a super mixer until the temperature reached 100 ° C. The fiber reinforced thermoplastic resin foam 6 was manufactured in the same manner as in Example 6 except that the above apparatus was used as the manufacturing apparatus.
7 was obtained. It has a two-layer structure having a core layer made of polyvinyl chloride foam inside a surface layer made of glass fiber-containing polyvinyl chloride pressed against the heating and cooling mold 66 and having a high density. Magnification was 3.73 times.
【0097】得られた繊維強化熱可塑性樹脂発泡体67
の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚みの
最大値、最小値及びCV値を実施例1と同様の方法によ
り測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 67
The flexural strength, flexural modulus and compressive strength, and the maximum, minimum, and CV values of the thickness of the surface layer were measured in the same manner as in Example 1. The results are shown in Table 1.
【0098】(実施例8) 発泡性樹脂組成物を、発泡性樹脂組成物押出用押出機か
ら165℃で未発泡のまま、中空状体内面に供給し、加
熱冷却金型の加熱部の温度を、190℃とし、発泡性樹
脂組成物を発泡させた以外は、実施例6と同様にして、
繊維強化熱可塑性樹脂発泡体59Aを得た。加熱冷却金
型に押し当てられ高密度となったガラス繊維含有ポリ塩
化ビニルからなる表面層内側に、ポリ塩化ビニル発泡体
からなる芯材層を有する2層構造であり、芯材層の発泡
倍率は2.10倍であった。Example 8 A foamable resin composition was supplied from a foamable resin composition extruder to a hollow body surface at 165 ° C. while not foaming, and the temperature of a heating section of a heating and cooling mold was changed. Was set to 190 ° C., and except that the foamable resin composition was foamed, in the same manner as in Example 6,
A fiber-reinforced thermoplastic resin foam 59A was obtained. It has a two-layer structure having a core layer made of polyvinyl chloride foam inside a surface layer made of glass fiber-containing polyvinyl chloride pressed against a heating and cooling mold and having a high density. Was 2.10 times.
【0099】得られた繊維強化熱可塑性樹脂発泡体59
Aの曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚み
の最大値、最小値及びCV値を実施例1と同様の方法に
より測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 59
The flexural strength, flexural modulus and compressive strength of A, and the maximum, minimum and CV values of the thickness of the surface layer were measured in the same manner as in Example 1, and the results are shown in Table 1.
【0100】(実施例9) 発泡性樹脂組成物を、発泡性樹脂組成物押出用押出機か
ら162℃で未発泡のまま、中空状体内面に供給し、加
熱冷却金型の加熱部の温度を、190℃とし、発泡性樹
脂組成物を発泡させた以外は、実施例7と同様にして、
繊維強化熱可塑性樹脂発泡体67を得た。加熱冷却金型
に押し当てられ高密度となったガラス繊維含有ポリ塩化
ビニルからなる表面層内側に、ポリ塩化ビニル発泡体か
らなる芯材層を有する2層構造であり、芯材層の発泡倍
率は2.0倍であった。Example 9 A foamable resin composition was supplied from a foamable resin composition extrusion extruder to a hollow body surface at 162 ° C. while being not foamed. Was set to 190 ° C., and except that the foamable resin composition was foamed,
A fiber reinforced thermoplastic resin foam 67 was obtained. It has a two-layer structure having a core layer made of polyvinyl chloride foam inside a surface layer made of glass fiber-containing polyvinyl chloride pressed against a heating and cooling mold and having a high density. Was 2.0 times.
【0101】得られた繊維強化熱可塑性樹脂発泡体67
の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚みの
最大値、最小値及びCV値を実施例1と同様の方法によ
り測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 67
The flexural strength, flexural modulus and compressive strength, and the maximum, minimum, and CV values of the thickness of the surface layer were measured in the same manner as in Example 1. The results are shown in Table 1.
【0102】(実施例10) 粉体状樹脂組成物として、ポリ塩化ビニル100重量
部、錫系熱安定剤1重量部、ポリエチレンWAX0.7
重量部からなるものを用いた以外は、実施例1と同様に
して、繊維強化熱可塑性樹脂シート128を得た。図1
8(イ)に示す製造装置を用いて、維強化熱可塑性樹脂
発泡体を製造した。製造装置は、繊維強化熱可塑性樹脂
シート128が巻回された巻き戻しロール129と、そ
の前方に、横断面形状が図18(ロ)、図18(ハ)に
示すような形状を有し、且つ内部に繊維強化熱可塑性樹
脂シートの通ることができる貫通孔を有する、スリット
部材130、131と、繊維強化熱可塑性樹脂シート1
28の端部同士が重なり合った部分を、加熱する加熱ロ
ール143と、その前には、先端が直角前向きに折れ曲
がり、且つ金型142と押出機132の先端部間に隙間
を有するように配置された、発泡性樹脂組成物を供給す
る押出機132と、繊維強化熱可塑性樹脂シート128
を円形に賦形することができる金型142、145と、
金型142、145間には、横断面形状が図18(ニ)
に示す形状を有し、且つ内部に繊維強化熱可塑性樹脂シ
ート128の通ることができる貫通孔を有するスリット
部材133と、金型145の前方には、横断面形状が図
18(ホ)に示す形状を有し、且つ内部に繊維強化熱可
塑性樹脂シート128の通ることができる貫通孔を有す
るスリット部材134と、更に、スリット部材134の
前方には、入口断面形状が円形であり、漸次変化し、出
口断面形状が幅12×厚さ90mmの矩形である、金型
146と、繊維強化熱可塑性樹脂シート128の端部同
士が重なり合った他方を加熱する加熱ロール135と、
金型146と断熱材141を介して設置された、加熱金
型139及び140からなり、入口断面形状が幅12×
厚さ90mmの矩形であり、漸次変化し、出口断面形状
が図18(ヘ)に示す横断面形状である加熱金型136
と、その前方には、更に、断熱材137を介して、加熱
金型136の出口断面形状に対応した、横断面形状を有
する冷却金型138と、引取機144とを有するもので
ある。Example 10 As a powdery resin composition, 100 parts by weight of polyvinyl chloride, 1 part by weight of a tin-based heat stabilizer, polyethylene WAX 0.7
A fiber-reinforced thermoplastic resin sheet 128 was obtained in the same manner as in Example 1 except that a part consisting of parts by weight was used. FIG.
8 (a), a fiber reinforced thermoplastic resin foam was produced. The manufacturing apparatus has a rewinding roll 129 on which a fiber-reinforced thermoplastic resin sheet 128 is wound, and a cross section in front of the rewinding roll 129 having a shape as shown in FIGS. And slit members 130 and 131 having a through hole through which the fiber-reinforced thermoplastic resin sheet can pass, and the fiber-reinforced thermoplastic resin sheet 1
The heating roll 143 that heats the portion where the ends of the 28 overlap each other is disposed in front of the heating roll 143 so that the tip is bent forward at a right angle and a gap is provided between the mold 142 and the tip of the extruder 132. An extruder 132 for supplying the foamable resin composition; and a fiber-reinforced thermoplastic resin sheet 128.
Molds 142 and 145 that can shape the
The cross-sectional shape between the molds 142 and 145 is shown in FIG.
18 and a slit member 133 having a through hole through which the fiber-reinforced thermoplastic resin sheet 128 can pass, and a cross-sectional shape in front of the mold 145 is shown in FIG. A slit member 134 having a shape and having a through hole through which the fiber reinforced thermoplastic resin sheet 128 can pass, and further, in front of the slit member 134, the entrance cross-sectional shape is circular, and gradually changes. A mold 146 having an outlet cross-sectional shape of a rectangle having a width of 12 × a thickness of 90 mm, and a heating roll 135 for heating the other end of the fiber-reinforced thermoplastic resin sheet 128 in which the ends overlap each other;
It consists of heating molds 139 and 140 installed via a mold 146 and a heat insulating material 141, and the cross-sectional shape of the inlet is 12 ×
The heating mold 136 has a rectangular shape with a thickness of 90 mm, changes gradually, and has a cross-sectional exit shape shown in FIG.
In front of it, a cooling mold 138 having a cross-sectional shape corresponding to the exit cross-sectional shape of the heating mold 136 and a take-off device 144 are further provided via a heat insulating material 137.
【0103】得られた繊維強化熱可塑性樹脂シート12
8を、巻き戻しロール129より巻き戻しつつ、これを
スリット部材130、131の貫通孔に通し、スリット
部材130、131により、繊維強化熱可塑性樹脂シー
ト128の一端部を重ね合わせ、重ね合わせた部分を、
加熱ロール143で200℃に加熱し、融着させた。更
に、一端部が融着された繊維強化熱可塑性樹脂シート1
28を、150℃に保持された金型142に挿入し、ス
リット部材133、134及び、175℃に保持された
金型145、146、更には、200℃に保持された加
熱ロール135により、断面形状が幅90×厚さ12m
mの矩形である中空状体に賦形した。ポリ塩化ビニル1
00重量部、錫系熱安定剤2.5重量部、滑剤0.5重
量部、アクリル加工助剤8重量部、CaCO3 3.5重
量部、ジオクチルフタレート2重量部、重炭酸ナトリウ
ム(発泡温度175℃)2.1重量部からなる発泡性樹
脂組成物を、押出機132に供給し、樹脂温度180℃
で発泡させながら、中空状体内部に供給した。加熱金型
136を180℃に保持しつつ、発泡圧により中空状体
を賦形し、発泡を完了させ、冷却金型138により、表
皮層を60℃に冷却し、芯材層の発泡倍率が2.5倍で
ある、繊維強化熱可塑性樹脂発泡体147を成形速度
1.5m/minで成形した。得られた繊維強化熱可塑
性樹脂発泡体147の曲げ強度、曲げ弾性率及び圧縮強
度、表面層の厚みの最大値、最小値及びCV値を実施例
2と同様の方法により測定し、その結果を表1に示し
た。The obtained fiber reinforced thermoplastic resin sheet 12
8 is rewound from the rewind roll 129, passed through the through holes of the slit members 130, 131, and the slit members 130, 131 overlap one end of the fiber-reinforced thermoplastic resin sheet 128, and the overlapped portion To
The mixture was heated to 200 ° C. with a heating roll 143 and fused. Further, a fiber-reinforced thermoplastic resin sheet 1 having one end fused thereto.
28 is inserted into a mold 142 maintained at 150 ° C., and cross-sections are formed by slit members 133 and 134, molds 145 and 146 maintained at 175 ° C., and a heating roll 135 maintained at 200 ° C. Shape is width 90 x thickness 12m
m was shaped into a rectangular hollow body. Polyvinyl chloride 1
00 parts by weight, tin-based heat stabilizer 2.5 parts by weight, lubricant 0.5 parts by weight, acrylic processing aid 8 parts by weight, CaCO3 3.5 parts by weight, dioctyl phthalate 2 parts by weight, sodium bicarbonate (foaming temperature 175 C.) A foamable resin composition consisting of 2.1 parts by weight was supplied to an extruder 132 and a resin temperature of 180 ° C.
While being foamed in the above, the inside of the hollow body was supplied. While maintaining the heating mold 136 at 180 ° C., the hollow body is shaped by the foaming pressure to complete the foaming, and the skin layer is cooled to 60 ° C. by the cooling mold 138, and the foaming ratio of the core material layer is reduced. A 2.5 times, fiber reinforced thermoplastic resin foam 147 was molded at a molding speed of 1.5 m / min. The bending strength, bending elastic modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 147, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were measured. The results are shown in Table 1.
【0104】(実施例11) 粉体状熱可塑性樹脂として、平均粒径100μmのポリ
プロピレンを用いた以外は、実施例10と同様にして、
ガラス繊維が40容量%である、繊維強化熱可塑性樹脂
シート128を得たこと、金型142と押出機132の
先端部分との間隙をなくすと共に、押出機先端部分の中
央部にコア部材を備え、加熱ロール135、143の温
度を150℃に保持したこと、発泡性樹脂組成物(高密
度ポリエチレン100重量部、ホモポリプロピレン10
0重量部、シラン架橋性ポリプロピレン40重量部、ア
ゾジカルボンアミド(発泡温度190℃)5重量部を、
直径30mmの二軸押出機に供給し、170℃の温度で
溶融混練し、幅80mm、厚み3mmのシート状に押出
した後、該シートを100℃の熱水に1時間浸漬後、乾
燥させたもの)を、120℃で中空状体内面に供給した
こと、加熱金型139を210℃に、加熱金型140を
200℃に保持したこと、冷却金型138により表皮層
を40℃に冷却したこと、成形速度を0.5m/min
としたこと以外は、実施例10を同様にして、繊維強化
熱可塑性樹脂発泡体147を得た。得られた繊維強化熱
可塑性樹脂発泡体147の曲げ強度、曲げ弾性率及び圧
縮強度、表面層の厚みの最大値、最小値及びCV値を実
施例2と同様の方法により測定し、その結果を表1に示
した。Example 11 The procedure of Example 10 was repeated, except that polypropylene having an average particle size of 100 μm was used as the powdery thermoplastic resin.
A fiber-reinforced thermoplastic resin sheet 128 having 40% by volume of glass fiber was obtained, a gap between the mold 142 and the tip of the extruder 132 was eliminated, and a core member was provided at the center of the tip of the extruder. The temperature of the heating rolls 135 and 143 was maintained at 150 ° C., and the foamable resin composition (100 parts by weight of high-density polyethylene,
0 parts by weight, 40 parts by weight of silane crosslinkable polypropylene, 5 parts by weight of azodicarbonamide (foaming temperature 190 ° C.)
The mixture was supplied to a twin screw extruder having a diameter of 30 mm, melt-kneaded at a temperature of 170 ° C., extruded into a sheet having a width of 80 mm and a thickness of 3 mm, immersed in hot water at 100 ° C. for 1 hour, and dried. ) At 120 ° C., the heating mold 139 was maintained at 210 ° C., the heating mold 140 was maintained at 200 ° C., and the skin layer was cooled to 40 ° C. by the cooling mold 138. That the molding speed is 0.5 m / min
A fiber-reinforced thermoplastic resin foam 147 was obtained in the same manner as in Example 10 except that the above conditions were satisfied. The bending strength, bending elastic modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 147, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were measured. The results are shown in Table 1.
【0105】(実施例12) 幅110mmであって、両端部10mmに発泡性樹脂組
成物層が積層されていない部分を有するように調整した
こと以外は、実施例5と同様にして、複合シート42A
を得た。得られた2枚の複合シート42Aを用い、図1
9に示すように中空状体に賦形したこと以外は、実施例
5と同様にして、繊維強化熱可塑性樹脂発泡体52を得
た。得られた繊維強化熱可塑性樹脂発泡体52の曲げ強
度、曲げ弾性率及び圧縮強度、表面層の厚みの最大値、
最小値及びCV値を実施例2と同様の方法により測定
し、その結果を表1に示した。(Example 12) A composite sheet was prepared in the same manner as in Example 5, except that the width was 110 mm and both ends were adjusted so that the foamable resin composition layer was not laminated at 10 mm. 42A
I got Using the obtained two composite sheets 42A, FIG.
A fiber-reinforced thermoplastic resin foam 52 was obtained in the same manner as in Example 5, except that the hollow body was shaped as shown in FIG. Flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 52, the maximum value of the thickness of the surface layer,
The minimum value and CV value were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0106】(実施例13) 繊維強化熱可塑性樹脂シート128の代わりに、幅11
0mmの2枚の実施例6で用いられた繊維質シートを用
い、図20に示すように中空状体に賦形したこと以外
は、実施例10と同様にして、繊維強化熱可塑性樹脂発
泡体147を得た。得られた繊維強化熱可塑性樹脂発泡
体52の曲げ強度、曲げ弾性率及び圧縮強度、表面層の
厚みの最大値、最小値及びCV値を実施例2と同様の方
法により測定し、その結果を表1に示した。(Example 13) Instead of the fiber-reinforced thermoplastic resin sheet 128, the width 11
A fiber-reinforced thermoplastic resin foam was produced in the same manner as in Example 10 except that two 0 mm-sized fibrous sheets used in Example 6 were formed into a hollow body as shown in FIG. 147 was obtained. The bending strength, bending elastic modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 52, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were obtained. The results are shown in Table 1.
【0107】(実施例14) 発泡性樹脂組成物を、樹脂温度165℃で未発泡のまま
中空状体に供給したこと、加熱金型の温度を195℃と
し、発泡を開始させ、発泡圧により中空状体を賦形した
こと以外は、実施例13と同様にして、繊維強化熱可塑
性樹脂発泡体52を得た。得られた繊維強化熱可塑性樹
脂発泡体52の曲げ強度、曲げ弾性率及び圧縮強度、表
面層の厚みの最大値、最小値及びCV値を実施例2と同
様の方法により測定し、その結果を表1に示した。 (実施例15) 粉体状樹脂組成物として、酢酸−塩化ビニル共重合体
(溶融粘度1.7×105 ポイズ)100重量部、錫系
安定剤2重量部、ポリエチレンWAX0.5重量部から
なるものを用い、加熱炉の温度を210℃とした以外
は、実施例1と同様にして、厚み1.2mm、幅91m
m、ガラス繊維含有率30体積%の繊維強化熱可塑性樹
シート5を得た。(Example 14) The foaming resin composition was supplied to the hollow body in a non-foamed state at a resin temperature of 165 ° C, the temperature of a heating mold was set to 195 ° C, foaming was started, and the foaming pressure was changed. A fiber-reinforced thermoplastic resin foam 52 was obtained in the same manner as in Example 13 except that the hollow body was shaped. The bending strength, bending elastic modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 52, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were obtained. The results are shown in Table 1. (Example 15) A powdery resin composition was composed of 100 parts by weight of an acetic acid-vinyl chloride copolymer (melt viscosity 1.7 × 10 5 poises), 2 parts by weight of a tin-based stabilizer, and 0.5 parts by weight of polyethylene WAX. 1.2 mm in thickness and 91 m in width in the same manner as in Example 1 except that the temperature of the heating furnace was set to 210 ° C.
m, a fiber-reinforced thermoplastic resin sheet 5 having a glass fiber content of 30% by volume.
【0108】繊維強化熱可塑性樹脂シート5は、巻取機
によりコイル状に巻き取られるが、そのまま図10に示
す繊維強化熱可塑性樹脂発泡体製造装置の巻き戻しロー
ル81に移し替えられる。繊維強化熱可塑性樹脂発泡体
製造装置は、巻き戻しロール81と、その前方に配置せ
られかつ一側方の、塩素化ポリ塩化ビニル100重量
部、ジオクチル錫メルカプト系熱安定剤2重量部、グリ
セリンモノステアレート滑剤2重量部、ポリエチレンW
AX1重量部、ポリメチルメタアクリレート加工助剤5
重量部、CaCO3 5重量部、重炭酸ナトリウム(発泡
温度175℃)2.5重量部からなる、発泡性樹脂組成
物の押出機82と連結せられた賦形金型83と、賦形金
型83内の後端部に固定され、同金型83より前方に突
き出した横断面円形の内コア84と、賦形金型83の前
方に、後から順に配置せられた加熱真空成形装置85、
加熱金型86、断熱材87及び冷却金型88および引取
機89を備えている。The fiber reinforced thermoplastic resin sheet 5 is wound into a coil shape by a winder, but is transferred as it is to a rewind roll 81 of a fiber reinforced thermoplastic resin foam manufacturing apparatus shown in FIG. The fiber reinforced thermoplastic resin foam manufacturing apparatus includes a rewind roll 81, 100 parts by weight of chlorinated polyvinyl chloride, 2 parts by weight of dioctyltin mercapto-based heat stabilizer disposed in front of and on one side thereof, glycerin 2 parts by weight of monostearate lubricant, polyethylene W
AX1 part by weight, polymethyl methacrylate processing aid 5
A shaping mold 83 connected to an extruder 82 of a foamable resin composition, the shaping mold comprising 5 parts by weight, 5 parts by weight of CaCO 3, and 2.5 parts by weight of sodium bicarbonate (foaming temperature: 175 ° C.); An inner core 84 having a circular cross section that is fixed to the rear end of the inside of the die 83 and protrudes forward from the same die 83; and a heating vacuum forming device 85 that is arranged in front of the shaping die 83 in order from the rear.
A heating mold 86, a heat insulating material 87, a cooling mold 88, and a take-off machine 89 are provided.
【0109】賦形金型83は、U字状の入口と、真円の
環状出口とを有しており、入口から出口にかけて、U字
状に変形されて賦形金型83に挿入された繊維強化熱可
塑性樹脂シート5の両縁を徐々に接近させて最後に両縁
を突き合わせ、外径が29mm、厚み1.2mmの完全
な真円中空状体となすような通路が形成されている。押
出機82は、前記シート5が完全に中空状になる手前の
位置で賦形金型83の内コア84と連結せられている。
内コア84は賦形金型83の前面より突出している。内
コア84には、横断面円環状の発泡性樹脂組成物通路9
0が形成せられているが、これは内コア84の突出部8
4aにおいて、真空成形装置85の内周面に向かってラ
ッパ状に広がって開口している。押出機82には、直径
40mmの単軸押出機が用いられている。真空成形金型
85の内面は、入口側で賦形装置83の出口外径と同じ
円形となっているが、出口側で18mm×40mmの矩
形となっている。そして、出口から入口にかけて内面が
円形から次第に矩形になるようにかつその周長が次第に
大きくなっていっている。加熱金型86および冷却金型
88の内面は、ともに真空成形装置85の出口形状に合
致している。The shaping die 83 has a U-shaped inlet and a circular outlet, and is deformed into a U-shape from the inlet to the outlet and inserted into the shaping die 83. The two edges of the fiber-reinforced thermoplastic resin sheet 5 are gradually approached to each other and finally the two edges are abutted to form a completely circular hollow body having an outer diameter of 29 mm and a thickness of 1.2 mm. . The extruder 82 is connected to the inner core 84 of the shaping die 83 at a position before the sheet 5 becomes completely hollow.
The inner core 84 protrudes from the front surface of the shaping die 83. The inner core 84 has an annular foamable resin composition passage 9 having an annular cross section.
0 is formed, which corresponds to the protrusion 8 of the inner core 84.
In FIG. 4 a, it opens in a trumpet shape toward the inner peripheral surface of the vacuum forming device 85. As the extruder 82, a single screw extruder having a diameter of 40 mm is used. The inner surface of the vacuum molding die 85 has the same circular shape as the outer diameter of the outlet of the shaping device 83 on the inlet side, but has a rectangular shape of 18 mm × 40 mm on the outlet side. And, from the outlet to the inlet, the inner surface becomes gradually rectangular from a circular shape, and the circumferential length thereof becomes gradually larger. The inner surfaces of the heating mold 86 and the cooling mold 88 both conform to the outlet shape of the vacuum forming device 85.
【0110】上記装置において、巻き戻しロール81か
ら巻き戻された繊維強化熱可塑性樹脂シート5をU形に
折り曲げて賦形金型83に挿入し、同金型83内で17
0℃に加熱しながら連続的に中空状に賦形することによ
り中空状体91となし、この中空状体91を180℃に
加熱された真空成形装置85内に導入し、減圧力600
mmHgで真空成形装置85の内面に吸引して所定形状
に賦形しつつその内面に発泡性樹脂組成物を押出機82
より樹脂温度190℃で押出して積層すると同時に発泡
を開始させ、ついで、発泡させつつ加熱金型86に導入
し、樹脂温度を180℃に保持して発泡を完了させた
後、冷却金型88により外層表面温度を60℃にまで冷
却し、発泡倍率3.8倍の芯材層92と表皮層93とよ
りなる18mm×40mmの横断面矩形の繊維強化熱可
塑性樹脂発泡体94を連続的に得た。成形速度を1.0
m/minとした。In the above apparatus, the fiber-reinforced thermoplastic resin sheet 5 unwound from the unwinding roll 81 is bent into a U-shape, inserted into the shaping mold 83, and inserted into the shaping mold 83.
The hollow body 91 is continuously formed into a hollow shape while being heated to 0 ° C. to form a hollow body 91. The hollow body 91 is introduced into a vacuum forming apparatus 85 heated to 180 ° C.
The foamable resin composition is sucked into the inner surface of the vacuum forming device 85 at a pressure of mmHg and shaped into a predetermined shape while the extruder 82
The resin is extruded at a resin temperature of 190 ° C., the foaming is started at the same time as the lamination, and then the foaming is introduced into a heating mold 86 while the foaming is completed while the resin temperature is kept at 180 ° C. The outer layer surface temperature was cooled to 60 ° C. to continuously obtain an 18 mm × 40 mm fiber-reinforced thermoplastic resin foam 94 having a rectangular cross section of 18 mm × 40 mm comprising a core layer 92 having a foaming ratio of 3.8 and a skin layer 93. Was. Molding speed 1.0
m / min.
【0111】得られた繊維強化熱可塑性樹脂発泡体94
の曲げ強度、曲げ弾性率及び圧縮強度、表面層93の厚
みの最大値、最小値及びCV値を実施例2と同様の方法
により測定し、その結果を表1に示した。The obtained fiber-reinforced thermoplastic resin foam 94
The bending strength, flexural modulus and compressive strength, and the maximum, minimum and CV values of the thickness of the surface layer 93 were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0112】(実施例16) 発泡性樹脂組成物として、高密度ポリエチレン100重
量部、ホモポリプロピレン100重量部、シラン架橋性
ポリプロピレン40重量部、アゾジカルボンアミド(発
泡温度190℃)5重量部を、直径30mmの二軸押出
機に供給し、170℃にて、溶融混練し、幅80mm、
厚み3mmのシート状にし、このシートを100℃の熱
水に1時間浸漬した後、乾燥したものを用いたこと、発
泡性樹脂組成物を押出機82より樹脂温度170℃で未
発泡のまま押出し、加熱金型86を220℃に保持し
て、発泡性樹脂組成物を発泡させたこと以外は、実施例
15と同様にして、発泡倍率3.2倍の芯材層92と表
皮層93とよりなる18mm×40mmの横断面矩形の
繊維強化熱可塑性樹脂発泡体94を連続的に得た。得ら
れた繊維強化熱可塑性樹脂発泡体94の曲げ強度、曲げ
弾性率及び圧縮強度、表面層93の厚みの最大値、最小
値及びCV値を実施例2と同様の方法により測定し、そ
の結果を表1に示した。Example 16 As a foamable resin composition, 100 parts by weight of high-density polyethylene, 100 parts by weight of homopolypropylene, 40 parts by weight of silane crosslinkable polypropylene, and 5 parts by weight of azodicarbonamide (foaming temperature: 190 ° C.) It is supplied to a twin screw extruder having a diameter of 30 mm, and is melt-kneaded at 170 ° C.
A sheet having a thickness of 3 mm was immersed in hot water at 100 ° C. for 1 hour, and then dried. The foamable resin composition was extruded from an extruder 82 at a resin temperature of 170 ° C. without foaming. In the same manner as in Example 15, except that the foaming resin composition was foamed while the heating mold 86 was maintained at 220 ° C., the core material layer 92 and the skin layer 93 having a foaming ratio of 3.2 were formed. A 18 mm × 40 mm fiber-reinforced thermoplastic resin foam 94 having a rectangular cross section was continuously obtained. The bending strength, bending elastic modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 94, the maximum value, the minimum value and the CV value of the thickness of the surface layer 93 were measured by the same methods as in Example 2, and the results were as follows. Are shown in Table 1.
【0113】(実施例17) 粉体状樹脂組成物として、ポリプロピレン(溶融粘度
1.2×105 ポイズ)を用い、加熱炉の温度を210
℃とした以外は、実施例15と同様にして、厚み1m
m、幅91mm、ガラス繊維含有率40体積%の繊維強
化熱可塑性樹シート5を得た。更に、高密度ポリエチレ
ン100重量部、シラン架橋性ポリプロピレン15重量
部、アゾジカルボンアミド(発泡温度190℃)5重量
部、ガラス繊維(フィラメント直径φ14、繊維長5m
m)10重量部からなる発泡性樹脂組成物を直径30m
mの2軸押出機により樹脂温度を170℃以下に維持し
ながら押出し、厚み1mmの発泡性樹脂組成物シートを
得、これと上記繊維強化熱可塑性樹脂シート5とを17
0℃で積層熱融着させ、一端部に発泡性熱可塑性樹脂シ
ートの積層していない部分を10mm長さ設け、1mm
の発泡性熱可塑性樹脂層および1mmの繊維強化熱可塑
性樹脂層を有する幅110mmの複合シート99を得
た。Example 17 Polypropylene (melt viscosity: 1.2 × 10 5 poises) was used as the powdery resin composition, and the temperature of the heating furnace was set to 210.
1 m in the same manner as in Example 15 except that
m, a width of 91 mm, and a fiber reinforced thermoplastic resin sheet 5 having a glass fiber content of 40% by volume. Further, 100 parts by weight of high density polyethylene, 15 parts by weight of silane crosslinkable polypropylene, 5 parts by weight of azodicarbonamide (foaming temperature 190 ° C.), glass fiber (filament diameter φ14, fiber length 5 m)
m) A foamable resin composition consisting of 10 parts by weight was supplied with a diameter of 30 m.
extruding while maintaining the resin temperature at 170 ° C. or lower by a twin-screw extruder having a thickness of 1 m to obtain a foamable resin composition sheet having a thickness of 1 mm.
Laminated and heat-sealed at 0 ° C., and a non-laminated portion of the foamable thermoplastic resin sheet is provided at one end with a length of 10 mm, and 1 mm
A 110 mm wide composite sheet 99 having a foamable thermoplastic resin layer and a 1 mm fiber reinforced thermoplastic resin layer was obtained.
【0114】上記複合シート99は、実施例15の場合
と同様に巻取機によりコイル状に巻き取られるが、これ
は図11に示す繊維強化熱可塑性樹脂発泡体製造装置の
巻き戻しロール81に移し替えられる。The composite sheet 99 is wound in a coil shape by a winder in the same manner as in the case of Example 15, but is wound on a rewind roll 81 of a fiber-reinforced thermoplastic resin foam manufacturing apparatus shown in FIG. Transferred.
【0115】この繊維強化熱可塑性樹脂発泡体製造装置
は、図10の装置と較べて、押出機の存在しないこと、
内コア95が賦形金型83より前方に突出しておらず、
真空成形装置85に導入せられる直前の中空状体91を
賦形金型83の内面に押圧せしめるシリコンゴム製押圧
頭部96を内コア95の前端に首部97を介して備えて
いること、冷却金型88内に冷却水噴霧ノズル98が内
蔵せしめられていること以外は、図10の装置と同じで
ある。冷却水噴霧ノズル98に接続せられた冷却水供給
多岐管99は、真空引き用配管が利用されて設けられて
いる。図11の装置において、図10の装置と同一のも
のについては同一符号を付してその説明を省略する。The apparatus for producing a fiber-reinforced thermoplastic resin foam is different from the apparatus shown in FIG. 10 in that an extruder does not exist.
The inner core 95 does not protrude forward from the shaping mold 83,
A silicon rubber pressing head 96 for pressing the hollow body 91 immediately before being introduced into the vacuum forming device 85 against the inner surface of the shaping die 83 is provided at the front end of the inner core 95 via a neck 97, and cooling. The apparatus is the same as the apparatus of FIG. 10 except that a cooling water spray nozzle 98 is built in the mold 88. The cooling water supply manifold 99 connected to the cooling water spray nozzle 98 is provided using a vacuum evacuation pipe. In the apparatus of FIG. 11, the same elements as those of the apparatus of FIG. 10 are denoted by the same reference numerals, and description thereof will be omitted.
【0116】上記装置において、巻き戻しロール81か
ら巻き戻された複合シート99をその発泡性熱可塑性樹
脂層を内側にしU形に折り曲げて賦形金型83に挿入
し、賦形金型83内で170℃に加熱しつつ連続的に中
空状体に賦形することにより外径29.0mm、厚み2
mmの中空状体91となし、この中空状体91を220
℃に加熱された真空成形装置85内に導入し、減圧力7
00mmHgで真空成形装置85の内面に中空状体91
を吸引して賦形しつつ、内側の発泡性熱可塑性樹脂層の
発泡を開始させ、ついで、発泡させつつ加熱金型86に
導入し、樹脂温度を210℃に保持して発泡を完了させ
た後、冷却金型88により外層表面温度を40℃にまで
冷却し、成形速度を1.5m/minで、発泡倍率4倍
の芯材層100と表皮層101とよりなる30mm×3
0mmの横断面矩形の繊維強化熱可塑性樹脂発泡体10
2を連続的に得た。得られた繊維強化熱可塑性樹脂発泡
体の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚み
の最大値、最小値及びCV値を実施例2と同様の方法に
より測定し、その結果を表1に示した。In the above apparatus, the composite sheet 99 unwound from the unwinding roll 81 is bent into a U-shape with the expandable thermoplastic resin layer inside, and inserted into the shaping mold 83. While heating to 170 ° C. to form a hollow body continuously to obtain an outer diameter of 29.0 mm and a thickness of 2
mm hollow body 91, and this hollow body 91
Introduced into the vacuum forming apparatus 85 heated to
A hollow body 91 is formed on the inner surface of the vacuum forming device 85 at 00 mmHg.
While suctioning and shaping, foaming of the inner foamable thermoplastic resin layer was started, and then the foamed thermoplastic resin layer was introduced into the heating mold 86 while foaming, and the foaming was completed by maintaining the resin temperature at 210 ° C. Thereafter, the outer layer surface temperature is cooled to 40 ° C. by a cooling mold 88, the molding speed is 1.5 m / min, and the core material layer 100 having a foaming ratio of 4 times and the skin layer 101 are 30 mm × 3.
0 mm cross section rectangular fiber reinforced thermoplastic resin foam 10
2 was obtained continuously. The flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were tabulated. 1 is shown.
【0117】(実施例18) 押圧頭部96の代わりに、内コア95の中央に後方から
通気孔が設けられており、通気孔から賦形金型83の先
端部内側に空気を供給し、内部圧力0.2kg/cm2
を発生させることにより、中空状体91を賦形金型83
内面に押圧し、ついで真空成形装置85に導入し、真空
成形装置85で減圧力550mmHgにより、円形中空
状体から30mm×30mmの矩形中空状体に成形した
こと、成形速度を1.2m/minとしたこと以外は、
実施例17と同様にして、芯材層の発泡倍率は3.5倍
の繊維強化熱可塑性樹脂発泡体を得た。得られた繊維強
化熱可塑性樹脂発泡体の曲げ強度、曲げ弾性率及び圧縮
強度、表面層の厚みの最大値、最小値及びCV値を実施
例2と同様の方法により測定し、その結果を表1に示し
た。(Embodiment 18) Instead of the pressing head 96, a ventilation hole is provided from the rear in the center of the inner core 95, and air is supplied from the ventilation hole to the inside of the tip of the shaping die 83, Internal pressure 0.2kg / cm2
Is generated, thereby forming the hollow body 91 into the shaping mold 83.
The inner surface was pressed, and then introduced into a vacuum forming device 85. The vacuum forming device 85 formed a circular hollow body into a 30 mm × 30 mm rectangular hollow body with a reduced pressure of 550 mmHg. The forming speed was 1.2 m / min. Except that
In the same manner as in Example 17, a fiber-reinforced thermoplastic resin foam having a foaming ratio of the core material layer of 3.5 was obtained. The flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were tabulated. 1 is shown.
【0118】(実施例19) 繊維強化熱可塑性樹脂シートを、粉体状樹脂組成物とし
て、高密度ポリエチレン(溶融粘度1.4×105 ポイ
ズ)を用いたとしたこと、得られる繊維強化熱可塑性樹
脂シートの厚みを0.5mmに調整したこと以外、実施
例15と同様にして製造した。繊維強化熱可塑性樹脂シ
ート中、ガラス繊維の含有量は、40体積%であった。
繊維強化熱可塑性樹脂シートは、後述のように複合発泡
性シートと一体化されるが、複合発泡性シートは図12
に示す装置により製造した。(Example 19) The fiber-reinforced thermoplastic resin sheet was made of high-density polyethylene (melt viscosity: 1.4 × 10 5 poise) as the powdery resin composition, and the obtained fiber-reinforced thermoplastic resin was used. The sheet was manufactured in the same manner as in Example 15 except that the thickness of the sheet was adjusted to 0.5 mm. The content of glass fibers in the fiber-reinforced thermoplastic resin sheet was 40% by volume.
The fiber-reinforced thermoplastic resin sheet is integrated with the composite foamable sheet as described later, but the composite foamable sheet is not shown in FIG.
Was manufactured by the apparatus shown in FIG.
【0119】図12の装置は、ガラスマット103が巻
回された巻き戻しロール104と、その前方に配置せら
れかつ連続的に移動せしめられている上下無端ベルト1
05、106と、上下無端ベルト105、106の所定
間隙をおいて対向せしめられた挾持部105a、106
aが通過しうるように設けられている180℃に保持さ
れた加熱炉107と、加熱炉107の前方に配置せられ
かつ挾持部105a、106aを加圧する上下複数対の
加圧ロール108と、下無端ベルト106の後方突出上
側移送部106bの下側に配置せられこれに振動を与え
る振動装置109と、移送部106bの上方に配置せら
れた、粉体110(高密度ポリエチレン100重量部、
シラン架橋性ポリプロピレン15重量部、アゾジカルボ
ンアミド(発泡温度190℃)4重量部からなる発泡性
樹脂組成物を直径30mmの2軸押出機を用い、樹脂温
度175℃で混練し、ペレット化した後、冷凍粉砕し、
粒径100μm以下の粉体としたもの)供給ホッパー1
11と、ホッパーの排出口に配置せられ、粉体110の
供給量を一定にするための羽根車112およびこれの羽
根と所定の間隔をおいて羽根車112に対峙せしめられ
たローラ113と、ホッパー111と移送部106bと
の間に、相互に先端が隙間をおいて重なるようにかつ粉
体110の落下線上に向かって下向き斜めに配置せられ
た複数の傾斜板114とを備えている。The apparatus shown in FIG. 12 includes a rewinding roll 104 on which a glass mat 103 is wound, and an upper and lower endless belt 1 disposed in front of the rewinding roll 104 and continuously moved.
And the endless belts 105a, 106 facing each other with a predetermined gap between the upper and lower endless belts 105, 106.
a heating furnace 107 maintained at 180 ° C. so that a can pass therethrough; a plurality of pairs of upper and lower pressure rolls 108 disposed in front of the heating furnace 107 and pressing the holding portions 105a and 106a; A vibrating device 109 disposed below the upper end transfer section 106b of the lower endless belt 106 and applying vibration thereto, and a powder 110 (100 parts by weight of high-density polyethylene,
After kneading a foamable resin composition comprising 15 parts by weight of silane crosslinkable polypropylene and 4 parts by weight of azodicarbonamide (foaming temperature 190 ° C.) at a resin temperature of 175 ° C. using a twin screw extruder having a diameter of 30 mm, and pelletizing the mixture, , Frozen and crushed,
Powder having a particle size of 100 μm or less) Supply hopper 1
11, an impeller 112 arranged at a discharge port of the hopper, for keeping the supply amount of the powder 110 constant, and a roller 113 opposed to the impeller 112 at a predetermined interval from the impeller, A plurality of inclined plates 114 are disposed between the hopper 111 and the transfer section 106b so as to be overlapped with a gap therebetween and to be inclined downward toward the falling line of the powder 110.
【0120】用いられたガラスマットの組成は、ガラス
繊維(繊維径7〜17μm、繊維長50〜100mm)
100重量部と、有機繊維(ポリエチレン、繊維径30
μm、繊維長50mm)50重量部とを混合したもので
あり、その成形条件は、目付け重量が680〜700g
/cm2 、ニードル仕様が針種、#32(オルガン針社
製)、パンチ密度が60〜70箇所/cm2 、パンチ深
さが9〜10mmである。得られた複合発泡性シート中
の発泡性樹脂組成物の重量は、40重量%であった。The composition of the glass mat used was glass fiber (fiber diameter: 7 to 17 μm, fiber length: 50 to 100 mm)
100 parts by weight and organic fiber (polyethylene, fiber diameter 30
μm, fiber length 50 mm) and 50 parts by weight. The molding condition is that the basis weight is 680 to 700 g.
/ Cm 2, needle type is needle type, # 32 (manufactured by Organ Needle), punch density is 60 to 70 points / cm 2, and punch depth is 9 to 10 mm. The weight of the foamable resin composition in the obtained composite foamable sheet was 40% by weight.
【0121】この実施例では、図13に示す装置によ
り、繊維強化熱可塑性樹脂発泡体を製造した。図13の
装置は、厚み0.5mm、幅458mmの繊維強化熱可
塑性樹脂シート115が巻回されている上下の巻き戻し
ロール116と、下巻き戻しロール116の後方に配置
せられた厚み4mm、幅445mmの複合発泡性シート
117の巻回された巻き戻しロール125と、上下巻き
戻しロール116の前方に配置せられた上下の遠赤外線
ヒータ118と、両ヒータ118の前方に後から順に配
置せられた加熱金型119、加熱真空成形装置120、
加熱金型121、断熱材122、冷却金型123および
引取機124を備えている。In this example, a fiber-reinforced thermoplastic resin foam was manufactured using the apparatus shown in FIG. The apparatus shown in FIG. 13 includes upper and lower rewind rolls 116 on which a fiber-reinforced thermoplastic resin sheet 115 having a thickness of 0.5 mm and a width of 458 mm is wound, and a thickness of 4 mm disposed behind the lower rewind roll 116. A rewind roll 125 on which a composite foamable sheet 117 having a width of 445 mm is wound, upper and lower far-infrared heaters 118 disposed in front of upper and lower rewind rolls 116, and rear heaters 118 are disposed in front of both heaters 118 in that order. Heating mold 119, heating vacuum forming apparatus 120,
A heating mold 121, a heat insulating material 122, a cooling mold 123, and a take-off machine 124 are provided.
【0122】加熱金型119の後方には、図示していな
いが、上下の繊維強化熱可塑性樹脂シート115の両側
部をお互いに向き合う方向にL形に折り曲げる賦形板が
配置されており、この賦形板にそわせながら両繊維強化
熱可塑性樹脂シート115の両縁部を4mm重ね合わせ
つつ、両者の内側に複合発泡性シート117を入れた状
態で加熱金型119に導入する。図示したように幅45
0mm×長さ50mmのシリンダーを有しエアシリンダ
ー126よりシート115、117に一定の圧力(1k
g/cm2 )を与えることによりこれらシートを一体化
する。加熱金型119への挿入までに両繊維強化熱可塑
性樹脂シート115を遠赤外線ヒーター118で100
℃に予熱しておくことにより、加熱金型119への導入
が容易となる。加熱金型119は210℃に温度調整さ
れており、この加熱金型119の前端部において発泡性
熱可塑性樹脂組成物の発泡が開始するように速度を調整
しながら複合発泡性シート内蔵板状中空状体を加熱真空
成形装置120へ導入し、真空圧650mmHgで減圧
することにより、複合発泡性シート内蔵板状中空状体を
5mmから12mmまで発泡性シートの厚みを拡張し、
加熱金型121で発泡を完了させ、冷却金型123によ
り減圧力720mmHgで表面を冷却金型123内面に
密着させつつ滑らせ、表面温度50℃にまで冷却するこ
とにより、発泡倍率2.1倍の芯材層125と表皮層1
26とよりなる厚み12mm、幅450mmの板状繊維
強化熱可塑性樹脂発泡体127を得た。成形速度を80
cm/minとした。得られた繊維強化熱可塑性樹脂発
泡体の曲げ強度、曲げ弾性率及び圧縮強度、表面層の厚
みの最大値、最小値及びCV値を実施例2と同様の方法
により測定し、その結果を表1に示した。Although not shown, a shaping plate for bending both sides of the upper and lower fiber reinforced thermoplastic resin sheets 115 into an L-shape in a direction facing each other is arranged behind the heating mold 119. The two fiber-reinforced thermoplastic resin sheets 115 are introduced into the heating mold 119 in a state where the composite foamable sheet 117 is placed inside the both sides while overlapping both edges of the thermoplastic resin sheet 115 by 4 mm while being aligned with the shaping plate. Width 45 as shown
It has a cylinder of 0 mm x 50 mm in length and has a constant pressure (1 k
g / cm @ 2) to integrate these sheets. Before insertion into the heating mold 119, both the fiber-reinforced thermoplastic resin sheets 115 are
By preheating to ° C., introduction into the heating mold 119 becomes easy. The temperature of the heating mold 119 is adjusted to 210 ° C., and at the front end of the heating mold 119, the speed of the foaming thermoplastic resin composition is adjusted so as to start foaming, and the plate-shaped hollow with a built-in composite foaming sheet is adjusted. By introducing the shaped body into the heating vacuum forming apparatus 120 and reducing the pressure with a vacuum pressure of 650 mmHg, the thickness of the foamed sheet is expanded from 5 mm to 12 mm in the composite foamed sheet built-in plate-shaped hollow body,
The foaming is completed by the heating die 121, the surface is brought into close contact with the inner surface of the cooling die 123 by the depressurizing force 720mmHg by the cooling die 123, and the surface is cooled down to a surface temperature of 50 ° C., whereby the expansion ratio is 2.1 times. Core layer 125 and skin layer 1
26, a plate-like fiber-reinforced thermoplastic resin foam 127 having a thickness of 12 mm and a width of 450 mm was obtained. Molding speed 80
cm / min. The flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were tabulated. 1 is shown.
【0123】(実施例20) 厚み0.6mm、幅60mmの繊維強化熱可塑性樹脂シ
ート8aを3枚使用し、図17に示す賦形金型83aに
挿入する際に、略半分ずつ相互に重ねて挿入したこと、
内コア84内の中央に前方にのびた通気孔を設け、通気
孔より加熱真空成形装置85通過中の中空状体内に空気
を供給し0.3kg/cm2 の内部圧力を発生させると
同時に、加熱真空成形装置85で400mmHgの減圧
力により、円形中空状体から18mm×40mmの矩形
中空状体に成形したこと、成形速度を1.2m/min
としたこと以外は、実施例15と同様にして、芯材層の
発泡倍率4.7倍の繊維強化熱可塑性樹脂樹脂発泡体を
得た。得られた繊維強化熱可塑性樹脂発泡体の曲げ強
度、曲げ弾性率及び圧縮強度、表面層の厚みの最大値、
最小値及びCV値を実施例2と同様の方法により測定
し、その結果を表1に示した。Example 20 Three fiber-reinforced thermoplastic resin sheets 8a each having a thickness of 0.6 mm and a width of 60 mm were used, and when they were inserted into the shaping mold 83a shown in FIG. Inserted
A vent hole extending forward is provided in the center of the inner core 84, and air is supplied from the vent hole into the hollow body passing through the heating vacuum forming device 85 to generate an internal pressure of 0.3 kg / cm @ 2, The circular hollow body was formed into a rectangular hollow body of 18 mm × 40 mm by the forming device 85 under a reduced pressure of 400 mmHg, and the forming speed was 1.2 m / min.
A fiber-reinforced thermoplastic resin foam having a foaming ratio of 4.7 times the core material layer was obtained in the same manner as in Example 15 except that the above conditions were satisfied. Flexural strength of the obtained fiber-reinforced thermoplastic resin foam, flexural modulus and compressive strength, the maximum value of the thickness of the surface layer,
The minimum value and CV value were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0124】(実施例21) 幅60mmの繊維強化熱可塑性樹脂シート8aを3枚使
用し、図17に示す賦形金型83aに挿入する際に、略
半分ずつ相互に重ねて挿入したこと、内コア84内の中
央に前方にのびた通気孔を設け、通気孔より加熱真空成
形装置85通過中の中空状体内に空気を供給し0.3k
g/cm2 の内部圧力を発生させると同時に、加熱真空
成形装置85で400mmHgの減圧力により、円形中
空状体から18mm×40mmの矩形中空状体に成形し
たこと、成形速度を1.2m/minとしたこと以外
は、実施例16と同様にして、芯材層の発泡倍率4.7
倍の繊維強化熱可塑性樹脂樹脂発泡体を得た。得られた
繊維強化熱可塑性樹脂発泡体の曲げ強度、曲げ弾性率及
び圧縮強度、表面層の厚みの最大値、最小値及びCV値
を実施例2と同様の方法により測定し、その結果を表1
に示した。(Example 21) When three fiber-reinforced thermoplastic resin sheets 8a having a width of 60 mm were used and inserted into the shaping mold 83a shown in FIG. An air hole extending forward is provided in the center of the inner core 84, and air is supplied from the air hole into the hollow body passing through the heating vacuum forming device 85 to 0.3 k.
g / cm @ 2, and at the same time, from a circular hollow body to a rectangular hollow body of 18 mm.times.40 mm by a vacuum forming device 85 under a reduced pressure of 400 mmHg. The forming speed was 1.2 m / min. Except having been described, the expansion ratio of the core material layer was 4.7 in the same manner as in Example 16.
A double fiber-reinforced thermoplastic resin foam was obtained. The flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam, the maximum value, the minimum value and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results were tabulated. 1
It was shown to.
【0125】(実施例22) 複合シートは、実施例12で用いられたものを用いた。
図21に示す製造装置を用いて、繊維強化熱可塑性樹脂
発泡体を得た。図18と同様な場合は、図18と同様の
番号を用い、説明は省略する。押出機132の代わり
に、熱風吸気孔152及び熱風排気孔153を有する熱
風吸排気151を用い、断熱材141と加熱金型136
間に加熱真空成形機149を備え、該加熱真空成形機1
49の入口断面形状を幅12×90mmの矩形とし、漸
次変化させ、出口断面形状を、図18−ヘに示す形状と
したこと、冷却金型138の代わりに、真空冷却金型1
50を用いたこと、加熱金型136、真空成形金型15
0の断面形状を、加熱真空成形機の出口形状に対応した
形状としたこと以外は、実施例10において用いられ
た、繊維強化熱可塑性樹脂発泡体の製造装置と同様の製
造装置であった。繊維強化熱可塑性樹脂シート128の
代わりに、実施例12で用いられた複合シート148を
用いたこと、熱風吸気孔から210℃の熱風を中空状体
の内面に供給すると同時に、熱風排気孔153から排気
したこと、金型145、146の温度を210℃に保持
したこと、200℃に保持された加熱真空成形機で、中
空状体を650mmHgの圧力で中空状体を賦形したこ
と、加熱金型の温度を200℃としたこと、真空冷却金
型150で、720mmHgの圧力で真空引きしつつ、
表皮層を40℃に冷却したこと以外は、実施例10と同
様にして、繊維強化熱可塑性樹脂発泡体154を得た。
得られた繊維強化熱可塑性樹脂発泡体154の曲げ強
度、曲げ弾性率及び圧縮強度、表面層の厚みの最大値、
最小値及びCV値を実施例2と同様の方法により測定
し、その結果を表1に示した。Example 22 The composite sheet used in Example 12 was used.
A fiber-reinforced thermoplastic resin foam was obtained using the manufacturing apparatus shown in FIG. In the case similar to FIG. 18, the same numbers as those in FIG. 18 are used, and the description is omitted. Instead of the extruder 132, a hot air intake / exhaust 151 having a hot air intake hole 152 and a hot air exhaust hole 153 is used, and a heat insulating material 141 and a heating mold 136 are used.
A heating vacuum forming machine 149 is provided between
The inlet cross-sectional shape of 49 is a rectangle of width 12 × 90 mm, and is gradually changed, and the outlet cross-sectional shape is a shape shown in FIG. 18- F .
50, heating mold 136, vacuum forming mold 15
The manufacturing apparatus was the same as the apparatus for manufacturing a fiber-reinforced thermoplastic resin foam used in Example 10, except that the cross-sectional shape of No. 0 was a shape corresponding to the outlet shape of the heating vacuum forming machine. Instead of using the fiber-reinforced thermoplastic resin sheet 128, the composite sheet 148 used in Example 12 was used. Hot air at 210 ° C. was supplied to the inner surface of the hollow body from the hot air intake hole, and at the same time, the hot air exhaust hole 153 was used. Evacuation, maintaining the temperature of the molds 145 and 146 at 210 ° C., shaping the hollow body with a heating vacuum forming machine maintained at 200 ° C. at a pressure of 650 mmHg, The temperature of the mold was set to 200 ° C., and vacuum evacuation was performed with a vacuum cooling mold 150 at a pressure of 720 mmHg.
A fiber-reinforced thermoplastic resin foam 154 was obtained in the same manner as in Example 10, except that the skin layer was cooled to 40 ° C.
Flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 154, the maximum value of the thickness of the surface layer,
The minimum value and CV value were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0126】(実施例23) 1枚の幅200mmの繊維強化熱可塑性樹脂シートを用
いて中空状体に賦形したこと以外は、実施例19と同様
にして、発泡倍率2.5倍の芯材層を有する繊維強化熱
可塑性樹脂発泡体を得た。得られた繊維強化熱可塑性樹
脂発泡体102の曲げ強度、曲げ弾性率及び圧縮強度、
表面層の厚みの最大値、最小値及びCV値を実施例2と
同様の方法により測定し、その結果を表1に示した。Example 23 A core having an expansion ratio of 2.5 times was produced in the same manner as in Example 19, except that the hollow body was formed using one fiber-reinforced thermoplastic resin sheet having a width of 200 mm. A fiber reinforced thermoplastic resin foam having a material layer was obtained. Flexural strength, flexural modulus and compressive strength of the obtained fiber-reinforced thermoplastic resin foam 102,
The maximum value, the minimum value, and the CV value of the thickness of the surface layer were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0127】(比較例1) 図8に示した製造装置を用いて複合体を成形した。芯材
68として実施例1で用いられた発泡性樹脂組成物を押
出成形することによって得られた、発泡倍率3.5倍、
外径26mm、長さ4000mmの発泡体を使用し、ま
た図中69は直径23μmのフィラメントより構成され
るロービング状ガラス繊維束(4400tex)であ
り、170℃に加熱軟化された芯材68の上方と下方の
2方向から、液状の熱硬化性樹脂(不飽和ポリエステ
ル)を注入した樹脂液槽70の中を通過した後、複数の
整列装置71を経て移送され、芯材68の外周囲に導か
れると共に、一方、不織布(ガラス繊維のコンティニュ
アスマット)72を繰り出しながら、この強化繊維69
の外周上に移送し、これら成形材料を、断面形状が内径
29mmの円形である、引抜成形金型73に送り込ん
だ。次に、この成形金型73内で180℃に加熱硬化さ
せ複合体74となし、引取機75にて引き取られた。Comparative Example 1 A composite was formed using the manufacturing apparatus shown in FIG. A foaming ratio of 3.5 times, obtained by extruding the foamable resin composition used in Example 1 as the core material 68,
A roving-like glass fiber bundle (4400 tex) made of a filament having a diameter of 23 μm is used above a core material 68 heated and softened to 170 ° C. A foamed material having an outer diameter of 26 mm and a length of 4000 mm is used. After passing through a resin liquid tank 70 filled with a liquid thermosetting resin (unsaturated polyester) from two directions below, the liquid is transferred through a plurality of alignment devices 71 and guided around the outer periphery of the core 68. On the other hand, while the nonwoven fabric (continuous mat of glass fiber) 72 is being unwound, the reinforcing fibers 69
These molding materials were fed to a pultruding mold 73 having a circular cross section having an inner diameter of 29 mm. Next, it was heated and cured at 180 ° C. in the molding die 73 to form a composite 74, and was taken up by a take-up machine 75.
【0128】得られた複合体74の曲げ強度、曲げ弾性
率及び圧縮強度、表面層の厚みの最大値、最小値及びC
V値を実施例1と同様の方法により測定し、その結果を
表1に示した。The flexural strength, flexural modulus and compressive strength of the obtained composite 74, the maximum and minimum values of the thickness of the surface layer, and C
The V value was measured in the same manner as in Example 1, and the results are shown in Table 1.
【0129】(比較例2) 実施例6で用いられた繊維質シートに、厚み0.3mm
のポリ塩化ビニルシートを200℃に加熱した加圧ロー
ル間で溶融ラミネートしたものを用いた。得られたガラ
ス繊維強化ポリ塩化ビニルシートのガラス繊維含有率は
42体積%、シート厚みは1.2mmであった。Comparative Example 2 The fibrous sheet used in Example 6 had a thickness of 0.3 mm.
What was melt-laminated between pressure rolls heated to 200 ° C. was used. The glass fiber content of the obtained glass fiber reinforced polyvinyl chloride sheet was 42% by volume, and the sheet thickness was 1.2 mm.
【0130】図9に示す製造装置を用いて、発泡体を成
形した。製造装置は、発泡性樹脂組成物押出用押出機7
6、発泡性樹脂組成物押出用金型77、加熱冷却金型7
8、引取機79よりなる。発泡性樹脂組成物押出用金型
77には押出機76から直径5mmの流路80が設けら
れており、流路80より発泡性樹脂組成物が押し出され
る構造となっていた。この金型77には金型内面断面形
状が直径27.5mmの円形である、加熱冷却金型78
が取り付けられていた。発泡性樹脂組成物押出用金型7
7から、実施例6で用いられた発泡性樹脂組成物を発泡
させながら押し出し、加熱冷却金型78の加熱部分で発
泡を完了させ、冷却部分で冷却固化させ、発泡倍率3.
0倍のポリ塩化ビニル発泡体を製造した。得られた発泡
体は断面が直径27.5mmの円形であった。この発泡
体の外側に上記ガラス繊維強化ポリ塩化ビニルシートを
エマルジョン状態の酢酸ビニル接着剤で貼り付けて繊維
強化ポリ塩化ビニル層と発泡体層の2層からなる複合発
泡体を得た。A foam was molded using the manufacturing apparatus shown in FIG. The production apparatus is an extruder 7 for extruding a foamable resin composition.
6, foaming resin composition extrusion mold 77, heating and cooling mold 7
8. It consists of a take-off machine 79. The foamable resin composition extrusion die 77 was provided with a flow path 80 having a diameter of 5 mm from the extruder 76, and had a structure in which the foamable resin composition was extruded from the flow path 80. This mold 77 has a heating / cooling mold 78 whose inner cross-sectional shape is a circle having a diameter of 27.5 mm.
Was attached. Mold for foaming resin composition extrusion 7
7, the foaming resin composition used in Example 6 was extruded while being foamed, foaming was completed in the heating portion of the heating / cooling mold 78, and was cooled and solidified in the cooling portion.
A 0x polyvinyl chloride foam was produced. The cross section of the obtained foam was a circle having a diameter of 27.5 mm. The above-mentioned glass fiber reinforced polyvinyl chloride sheet was adhered to the outside of this foam with a vinyl acetate adhesive in an emulsion state to obtain a composite foam composed of a fiber reinforced polyvinyl chloride layer and a foam layer.
【0131】得られた複合発泡体の曲げ強度、曲げ弾性
率及び圧縮強度、繊維強化ポリ塩化ビニル層の厚みの最
大値、最小値及びCV値を実施例1と同様の方法により
測定し、その結果を表1に示した。複合発泡体の曲げ強
度を測定する際、繊維強化ポリ塩化ビニル層と発泡体層
とが剥離した。The flexural strength, flexural modulus and compressive strength of the obtained composite foam, the maximum value, the minimum value and the CV value of the thickness of the fiber-reinforced polyvinyl chloride layer were measured in the same manner as in Example 1. The results are shown in Table 1. When measuring the bending strength of the composite foam, the fiber reinforced polyvinyl chloride layer and the foam layer were separated.
【0132】(比較例3) 実施例1で用いられた製造装置において、繊維強化熱可
塑性樹脂シートを供給しなかったこと、入口断面形状が
加熱金型11と同一形状であり、前方につれて、漸次変
化し、出口断面形状が30×30mmの矩形となった、
冷却金型を用い、25℃で急冷した以外は実施例1と同
様の方法で、発泡体を製造した。得られた発泡体表面に
は、厚さ1mmの未発泡層が形成されていた。得られた
発泡体の曲げ強度、曲げ弾性率及び圧縮強度、表面層の
厚みの最大値、最小値及びCV値を実施例2と同様の方
法により測定し、その結果を表1に示した。(Comparative Example 3) In the manufacturing apparatus used in Example 1, the fiber-reinforced thermoplastic resin sheet was not supplied, and the cross-sectional shape of the inlet was the same as that of the heating mold 11. Changed, the outlet cross section became a rectangle of 30 × 30 mm,
Using a cooling mold, a foam was produced in the same manner as in Example 1 except that the foam was rapidly cooled at 25 ° C. An unfoamed layer having a thickness of 1 mm was formed on the surface of the obtained foam. The flexural strength, flexural modulus and compressive strength of the foam obtained, the maximum value, the minimum value and the CV value of the surface layer thickness were measured in the same manner as in Example 2, and the results are shown in Table 1.
【0133】[0133]
【表1】 [Table 1]
【0134】[0134]
【発明の効果】本発明の構成は上記の通りであり、予め
成形された発泡体を用意する必要がないため、生産性に
優れ、又、発泡圧により中空状体を賦形するものである
ため、中空状体からなる表皮層の厚みむらが発生しにく
く、剛性等の均質な繊維強化熱可塑性樹脂発泡体を得る
ことができる。The constitution of the present invention is as described above, and it is not necessary to prepare a preformed foam, so that the productivity is excellent and the hollow body is shaped by the foaming pressure. Therefore, thickness unevenness of the skin layer formed of the hollow body is less likely to occur, and a uniform fiber-reinforced thermoplastic resin foam having rigidity or the like can be obtained.
【0135】表皮層及び芯材層には熱可塑性樹脂を用
い、発泡圧により賦形しているので、製造過程において
所望形状に賦形することが可能であり、複雑な断面形状
を有する繊維強化熱可塑性樹脂発泡体を得ることがで
き、用いられる樹脂は、熱可塑性樹脂であるため、再成
形及びリサイクルが可能である。Since the skin layer and the core layer are made of a thermoplastic resin and are shaped by foaming pressure, they can be formed into a desired shape in the manufacturing process, and fiber reinforced having a complicated cross-sectional shape can be formed. A thermoplastic resin foam can be obtained. Since the resin used is a thermoplastic resin, it can be remolded and recycled.
【0136】しかも、発泡性樹脂組成物が発泡する発泡
圧により、溶融状態にある発泡途上の樹脂が、中空状体
を内部から均一な力で押すことにより、表面層と芯材層
が融着一体化したものであるため、表面層と芯材層の界
面において部分的に融着の弱い部分が存在せず、曲げ強
度等の剛性の品質の均一な繊維強化熱可塑性樹脂発泡体
を得ることができる。Further, the foaming resin foaming pressure causes the foaming resin in the molten state to push the hollow body from inside with a uniform force, so that the surface layer and the core material layer are fused. Since it is integrated, there is no weak fusion part at the interface between the surface layer and the core material layer, and a fiber-reinforced thermoplastic resin foam with uniform rigidity quality such as bending strength is obtained. Can be.
【0137】又、複合シートを用いると、表皮層と芯材
層との界面に、発泡性樹脂組成物から生じたガスが残存
し、得られる繊維強化熱可塑性樹脂発泡体の表面層と芯
材層との間にボイドが発生するのを防止することができ
る。When the composite sheet is used, gas generated from the foamable resin composition remains at the interface between the skin layer and the core material layer, and the surface layer of the resulting fiber-reinforced thermoplastic resin foam and the core material The generation of voids between the layer and the layer can be prevented.
【0138】又、繊維質シートを用いると、発泡性樹脂
組成物が発泡して、繊維質シートの繊維間に樹脂が含浸
するので、予め繊維強化熱可塑性樹脂シート等を製造し
ておく必要がないので、工程を省くことができる。When a fibrous sheet is used, the foamable resin composition foams and the resin is impregnated between the fibers of the fibrous sheet. Therefore, it is necessary to produce a fiber-reinforced thermoplastic resin sheet or the like in advance. Since it is not provided, the process can be omitted.
【0139】請求項3〜5、請求項8記載の発明では、
発泡圧又は/及び空気圧成形により、中空状体を賦形し
ているため、発泡圧のみの場合に比して、より断面形状
の複雑な繊維強化熱可塑性樹脂発泡体を、より精度良く
製造することができる。In the inventions according to claims 3 to 5 and claim 8 ,
Since the hollow body is shaped by foaming pressure or / and pneumatic molding, a fiber-reinforced thermoplastic resin foam having a more complex cross-sectional shape can be manufactured more accurately than when only foaming pressure is used. be able to.
【0140】繊維強化熱可塑性樹脂シートとして、連続
繊維が多数配向したものを用い、連続繊維が長手方向と
なるように中空状体に賦形することは、中空状体を引き
抜きつつ、繊維強化熱可塑性樹脂発泡体を製造すること
ができ、生産性を向上させることができる。As the fiber-reinforced thermoplastic resin sheet, a sheet in which a large number of continuous fibers are oriented and shaped into a hollow body so that the continuous fibers are in the longitudinal direction can be obtained by pulling out the hollow body while removing the fiber-reinforced thermoplastic resin sheet. A plastic foam can be manufactured, and productivity can be improved.
【0141】請求項8に記載の発明では、発泡性繊維強
化熱可塑性樹脂組成物を加熱発泡するとともに空気圧成
形した際に中空状体における発泡性シートの厚みが拡張
するので、マット状物の強化繊維がほぼ厚さ方向にの
び、その結果きわめて圧縮強度に優れた繊維強化熱可塑
性樹脂発泡体を得ることができる。According to the eighth aspect of the present invention, the thickness of the foamable sheet in the hollow body is expanded when the foamable fiber-reinforced thermoplastic resin composition is heated and foamed and pneumatically molded. As a result, the fiber-reinforced thermoplastic resin foam excellent in compressive strength can be obtained.
【図1】実施例1において用いられた、繊維強化熱可塑
性樹脂シートの製造装置の断面模式図である。FIG. 1 is a schematic cross-sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin sheet used in Example 1.
【図2】実施例1において用いられた、繊維強化熱可塑
性樹脂発泡体の製造装置の断面模式図である。FIG. 2 is a schematic cross-sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 1.
【図3】実施例3において用いられた、繊維強化熱可塑
性樹脂シートの製造装置の断面模式図である。FIG. 3 is a schematic cross-sectional view of a device for manufacturing a fiber-reinforced thermoplastic resin sheet used in Example 3.
【図4】図4(イ)は、実施例4において用いられた、
繊維強化熱可塑性樹脂発泡体の製造装置の断面模式図で
ある。図4(ロ)は、図4(イ)における、賦形金型の
4(ロ)−4(ロ)断面矢視図である。FIG. 4 (a) shows the results obtained in Example 4;
It is a cross section of an apparatus for manufacturing a fiber-reinforced thermoplastic resin foam. FIG. 4B is a sectional view taken along the arrow 4 (B) -4 (B) of the shaping mold in FIG. 4 (A).
【図5】図5(イ)は、実施例5において用いられた、
繊維強化熱可塑性樹脂発泡体の製造装置の断面模式図で
ある。図5(ロ)は、図5(イ)における、加熱金型の
5(ロ)−5(ロ)断面矢視図である。図5(ハ)は、
図5(イ)における、加熱金型の5(ハ)−5(ハ)断
面矢視図である。図5(ニ)は、加熱金型入口におけ
る、複合シートにより楕円形に賦形し、得られた中空状
体の断面図である。FIG. 5 (a) is a cross-sectional view used in Example 5.
It is a cross section of an apparatus for manufacturing a fiber-reinforced thermoplastic resin foam. FIG. 5B is a cross-sectional view taken along line 5 (B) -5 (B) of the heating mold in FIG. FIG.
FIG. 5C is a sectional view of the heating mold taken along line 5 (c) -5 (c) in FIG. FIG. 5D is a cross-sectional view of a hollow body obtained by forming an elliptical shape using a composite sheet at the entrance of a heating mold.
【図6】実施例6において用いられた、繊維強化熱可塑
性樹脂発泡体の製造装置の断面模式図である。FIG. 6 is a schematic sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 6.
【図7】実施例7において用いられた、繊維強化熱可塑
性樹脂発泡体の製造装置の断面模式図である。FIG. 7 is a schematic sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 7.
【図8】比較例1において用いられた、複合体の製造装
置の断面模式図である。FIG. 8 is a schematic cross-sectional view of a composite manufacturing apparatus used in Comparative Example 1.
【図9】比較例2において用いられた、繊維強化熱可塑
性樹脂発泡体の製造装置の断面模式図である。FIG. 9 is a schematic sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Comparative Example 2.
【図10】実施例15に用いられた繊維強化熱可塑性樹
脂発泡体製造装置の断面模式図である。FIG. 10 is a schematic sectional view of a fiber-reinforced thermoplastic resin foam manufacturing apparatus used in Example 15.
【図11】実施例17に用いられた繊維強化熱可塑性樹
脂発泡体の製造装置の断面模式図である。FIG. 11 is a schematic sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 17.
【図12】実施例19に用いられた複合発泡性シートの
製造装置の断面模式図である。FIG. 12 is a schematic sectional view of an apparatus for manufacturing a composite foamable sheet used in Example 19.
【図13】実施例19に用いられた繊維強化熱可塑性樹
脂発泡体の製造装置の断面模式図である。FIG. 13 is a schematic sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 19.
【図14】図13における、加熱金型の14−14断面
矢視図である。FIG. 14 is a cross-sectional view of the heating mold taken along line 14-14 in FIG.
【図15】図13における、加熱金型の15−15断面
矢視図である。FIG. 15 is a sectional view of the heating mold taken along line 15-15 in FIG.
【図16】図13における、16−16断面矢視図であ
る。FIG. 16 is a sectional view taken along arrow 16-16 in FIG. 13;
【図17】実施例20において用いられた繊維強化熱可
塑性樹脂シートの製造装置の賦形金型の一部横断面図で
ある。FIG. 17 is a partial cross-sectional view of a shaping mold of the apparatus for manufacturing a fiber-reinforced thermoplastic resin sheet used in Example 20.
【図18】図18(イ)は、実施例10において用いら
れた繊維強化熱可塑性樹脂発泡体の製造装置の断面模式
図である。図18(ロ)は、スリット部材130に繊維
強化熱可塑性樹脂シートを挿入した状態の断面矢視図で
ある。図18(ハ)は、スリット部材131に繊維強化
熱可塑性樹脂シートを挿入した状態の断面矢視図であ
る。図18(ニ)は、スリット部材133に繊維強化熱
可塑性樹脂シートを挿入した状態の断面矢視図である。
図18(ホ)は、スリット部材134に繊維強化熱可塑
性樹脂シートを挿入した状態の断面矢視図である。図1
8(ヘ)は、加熱金型140出口部分の断面図である。
図18(ト)は、加熱金型入口における、中空状体の断
面形状図である。FIG. 18 (a) is a schematic cross-sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 10. FIG. 18B is a cross-sectional view of the state in which the fiber-reinforced thermoplastic resin sheet is inserted into the slit member 130. FIG. 18C is a cross-sectional view of the slit member 131 in which a fiber-reinforced thermoplastic resin sheet is inserted. FIG. 18D is a cross-sectional view of the state in which the fiber-reinforced thermoplastic resin sheet is inserted into the slit member 133.
FIG. 18E is a cross-sectional view of the state in which the fiber-reinforced thermoplastic resin sheet is inserted into the slit member 134. FIG.
8 (f) is a cross-sectional view of the exit portion of the heating mold 140.
FIG. 18G is a cross-sectional view of the hollow body at the entrance of the heating mold.
【図19】実施例12の加熱金型入口における、中空状
体の断面形状図である。FIG. 19 is a cross-sectional view of a hollow body at the entrance of a heating mold of Example 12.
【図20】実施例18の加熱金型入口における、中空状
体の断面形状図である。FIG. 20 is a sectional view of a hollow body at the entrance of a heating mold of Example 18.
【図21】実施例22で用いられた繊維強化熱可塑性樹
脂発泡体の製造装置の断面模式図である。FIG. 21 is a schematic sectional view of an apparatus for producing a fiber-reinforced thermoplastic resin foam used in Example 22.
5、25E、29A、115、128 繊維強化熱
可塑性樹脂シート 15、39 発泡性樹脂
組成物 16、41、52、59A、67、94、102、12
7、147、154繊維強化熱可塑性樹脂発泡体 42A、99、148 複合シート 61、64 繊維質シー
ト 91 中空状体 117 複合発泡性
シート 11、32、48、58、66、136、85、86、
120、121、136、149
(中空状体賦形)金型5, 25E, 29A, 115, 128 Fiber reinforced thermoplastic resin sheet 15, 39 Foamable resin composition 16, 41, 52, 59A, 67, 94, 102, 12
7, 147, 154 fiber-reinforced thermoplastic resin foam 42A, 99, 148 composite sheet 61, 64 fibrous sheet 91 hollow body 117 composite foamable sheet 11, 32, 48, 58, 66, 136, 85, 86,
120, 121, 136, 149
(Hollow shaped) Mold
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B29K 105:04 105:08 B29L 9:00 31:10 (56)参考文献 特開 昭52−58771(JP,A) 特開 平4−216923(JP,A) 特開 昭55−71531(JP,A) 特開 平3−161318(JP,A) 特開 平4−27532(JP,A) 特開 平5−16253(JP,A) 特開 昭62−181137(JP,A) 特開 昭59−140034(JP,A) (58)調査した分野(Int.Cl.6,DB名) B29C 44/00 - 44/60 B29C 67/20 B29C 70/00 - 70/56 B32B 1/06 B32B 5/00 - 5/32 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification symbol FI B29K 105: 04 105: 08 B29L 9:00 31:10 (56) References JP-A-52-58771 (JP, A) JP-A JP-A-4-216923 (JP, A) JP-A-55-71531 (JP, A) JP-A-3-161318 (JP, A) JP-A-4-27532 (JP, A) JP-A-5-16253 (JP) JP-A-62-181137 (JP, A) JP-A-59-140034 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) B29C 44/00-44/60 B29C 67/20 B29C 70/00-70/56 B32B 1/06 B32B 5/00-5/32
Claims (8)
中空状体に賦形する工程、中空状体の内面に、熱可塑性
樹脂及び発泡剤を含有する発泡性樹脂組成物を発泡させ
ながら供給し、中空状体を発泡圧により所望形状に賦形
する工程を包含することを特徴とする繊維強化熱可塑性
樹脂発泡体の製造方法。1. A step of continuously forming one or a plurality of fibrous sheets into a hollow body, wherein a foamable resin composition containing a thermoplastic resin and a foaming agent is foamed on the inner surface of the hollow body. A method for producing a fiber-reinforced thermoplastic resin foam, comprising the steps of: feeding the mixture while forming the hollow body into a desired shape by foaming pressure.
中空状体に賦形する工程、中空状体の内面に、熱可塑性
樹脂及び発泡剤を含有する発泡性樹脂組成物を供給し、
発泡性樹脂組成物を発泡剤の発泡温度以上に加熱し、中
空状体を発泡圧により所望形状に賦形する工程を包含す
ることを特徴とする繊維強化熱可塑性樹脂発泡体の製造
方法。2. A step of continuously shaping one or a plurality of fibrous sheets into a hollow body, and supplying a foamable resin composition containing a thermoplastic resin and a foaming agent to the inner surface of the hollow body. And
A method for producing a fiber-reinforced thermoplastic resin foam, comprising a step of heating the foamable resin composition to a temperature equal to or higher than the foaming temperature of a foaming agent and shaping the hollow body into a desired shape by foaming pressure.
ートを連続的に中空状体に賦形する工程、中空状体を所
定横断面形状に空気圧成形する工程、及び、中空状体の
内面に、熱可塑性樹脂及び発泡剤を含有する発泡性樹脂
組成物を発泡させながら供給し、中空状体を発泡圧によ
り所望形状に賦形する工程を包含することを特徴とする
繊維強化熱可塑性樹脂発泡体の製造方法。3. A step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets into a hollow body, a step of pneumatically forming the hollow body into a predetermined cross-sectional shape, and A fiber-reinforced thermoplastic material comprising a step of foaming and supplying a foamable resin composition containing a thermoplastic resin and a foaming agent to an inner surface thereof, and shaping the hollow body into a desired shape by foaming pressure. A method for producing a resin foam.
ートを連続的に中空状体に賦形する工程、中空状体を所
定横断面形状に空気圧成形する工程、及び、中空状体の
内面に、熱可塑性樹脂及び発泡剤を含有する発泡性樹脂
組成物を供給し、発泡性樹脂組成物を発泡剤の発泡温度
以上に加熱し、中空状体を発泡圧により所望形状に賦形
する工程を包含することを特徴とする繊維強化熱可塑性
樹脂発泡体の製造方法。4. A step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets into a hollow body, a step of pneumatically forming the hollow body into a predetermined cross-sectional shape, and On the inner surface, a foamable resin composition containing a thermoplastic resin and a foaming agent is supplied, and the foamable resin composition is heated to the foaming temperature of the foaming agent or more, and the hollow body is shaped into a desired shape by foaming pressure. A method for producing a fiber-reinforced thermoplastic resin foam, comprising the steps of:
及び発泡性樹脂組成物層からなる複合シートを、繊維強
化熱可塑性樹脂層が外面となるように連続的に中空状体
に賦形する工程、中空状体を所定横断面形状に空気圧成
形する工程、及び、発泡性樹脂組成物層を発泡させ、中
空状体を発泡圧により所望形状に賦形する工程を包含す
ることを特徴とする繊維強化熱可塑性樹脂発泡体の製造
方法。5. A hollow sheet is continuously provided with one or more composite sheets comprising a fiber-reinforced thermoplastic resin layer and a foamable resin composition layer so that the fiber-reinforced thermoplastic resin layer becomes an outer surface. Shaping, pneumatically forming the hollow body into a predetermined cross-sectional shape, and foaming the foamable resin composition layer and shaping the hollow body into a desired shape by foaming pressure. For producing a fiber-reinforced thermoplastic resin foam.
た繊維強化熱可塑性樹脂シートを、連続繊維が長手方向
となるように連続的に中空状体に賦形する工程、中空状
体を金型内に供給する工程、中空状体の内面に、熱可塑
性樹脂及び発泡剤を含有する発泡性樹脂組成物を発泡さ
せながら供給し、中空状体を引き抜きつつ、中空状体を
発泡圧により所望形状に賦形する工程を包含することを
特徴とする繊維強化熱可塑性樹脂発泡体の製造方法。6. A step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets in which a large number of continuous fibers are oriented into a hollow body so that the continuous fibers extend in the longitudinal direction. Supplying a foamable resin composition containing a thermoplastic resin and a foaming agent to the inner surface of the hollow body while foaming the foamed body. A method for producing a fiber-reinforced thermoplastic resin foam, comprising a step of shaping the fiber into a desired shape.
た繊維強化熱可塑性樹脂シートを、連続繊維が長手方向
となるように連続的に中空状体に賦形する工程、中空状
体を金型内に供給する工程、中空状体の内面に、熱可塑
性樹脂及び発泡剤を含有する発泡性樹脂組成物を供給
し、発泡性樹脂組成物を発泡剤の発泡温度以上に加熱
し、中空状体を引き抜きつつ、中空状体を発泡圧により
所望形状に賦形する工程を包含することを特徴とする繊
維強化熱可塑性樹脂発泡体の製造方法。7. A step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets in which a large number of continuous fibers are oriented into a hollow body so that the continuous fibers are in the longitudinal direction. A step of supplying a foamable resin composition containing a thermoplastic resin and a foaming agent to the inner surface of the hollow body, heating the foamable resin composition to a foaming temperature of the foaming agent or higher, A method for producing a fiber-reinforced thermoplastic resin foam, comprising a step of shaping the hollow body into a desired shape by foaming pressure while extracting the hollow body.
ートを連続的に中空状体に賦形する工程、中空状体内
に、繊維を主成分とするマット状物中に、熱可塑性樹脂
及び分解型発泡剤を含有する発泡性樹脂組成物が含浸せ
しめられてなる複合発泡性シートを供給し中空状体と一
体化する工程、及び、複合発泡性シートと一体化された
中空状体を空気圧成形すると共に、発泡性樹脂組成物を
発泡剤の発泡温度以上に加熱することにより、中空状体
における複合発泡性シートの厚みを拡張する工程を包含
することを特徴とする繊維強化熱可塑性樹脂発泡体の製
造方法。8. A step of continuously forming one or a plurality of fiber-reinforced thermoplastic resin sheets into a hollow body, wherein the hollow body contains a thermoplastic resin in a mat-like material containing fibers as a main component. Supplying a composite foamable sheet impregnated with a foamable resin composition containing a decomposable foaming agent, and integrating with a hollow body, and a hollow body integrated with the composite foamable sheet. By air-forming and heating the foamable resin composition above the foaming temperature of the foaming agent, the hollow body
A method for producing a fiber-reinforced thermoplastic resin foam, comprising the step of: expanding the thickness of the composite foamable sheet in the above .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6276652A JP2974582B2 (en) | 1993-11-10 | 1994-11-10 | Method for producing fiber-reinforced thermoplastic resin foam |
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28111693 | 1993-11-10 | ||
| JP5-281116 | 1994-08-29 | ||
| JP20328794 | 1994-08-29 | ||
| JP6-203287 | 1994-08-29 | ||
| JP6276652A JP2974582B2 (en) | 1993-11-10 | 1994-11-10 | Method for producing fiber-reinforced thermoplastic resin foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08118484A JPH08118484A (en) | 1996-05-14 |
| JP2974582B2 true JP2974582B2 (en) | 1999-11-10 |
Family
ID=27328216
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6276652A Expired - Fee Related JP2974582B2 (en) | 1993-11-10 | 1994-11-10 | Method for producing fiber-reinforced thermoplastic resin foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2974582B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5597152B2 (en) * | 2011-03-23 | 2014-10-01 | 株式会社神戸製鋼所 | Manufacturing method and manufacturing apparatus for long fiber reinforced resin strand |
| KR20180134392A (en) * | 2016-04-15 | 2018-12-18 | 씨씨3디 엘엘씨 | Head and system for continuously manufacturing a composite hollow structure |
| JP7849980B2 (en) * | 2022-02-09 | 2026-04-22 | 株式会社ジェイエスピー | Method for manufacturing extruded articles |
| CN115570811A (en) * | 2022-09-23 | 2023-01-06 | 歌尔科技有限公司 | Carbon fiber composite shell, its preparation method, and electronic device |
-
1994
- 1994-11-10 JP JP6276652A patent/JP2974582B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH08118484A (en) | 1996-05-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0653280B1 (en) | Method for producing a fiber reinforced thermoplastic resin foamed product | |
| US20140335321A1 (en) | Embossed polymer sheet | |
| US4159294A (en) | Method of manufacturing fiber-reinforced thermoplastic resin of cellular structure | |
| JP2974582B2 (en) | Method for producing fiber-reinforced thermoplastic resin foam | |
| JPH02258326A (en) | Expansile fiber complex structure and its producing method | |
| JPH1044178A (en) | Foamable thermoplastic resin sheet, thermoplastic resin foam, and methods for producing them | |
| CN106280348B (en) | Biological-bone-head-imitated structural section prepared from renewable materials and preparation method thereof | |
| JP3754525B2 (en) | Decorative molding sheet, method for producing the same, and method for producing fiber reinforced thermoplastic resin foam using the decorative molding sheet | |
| JP3255844B2 (en) | Method for producing foam and foamable sheet used therefor | |
| JPH08276524A (en) | Method for producing composite molded article having porous core | |
| JP7650790B2 (en) | Method for producing fiber-reinforced resin foam | |
| JPH08267475A (en) | Method for producing fiber-reinforced thermoplastic resin foam | |
| JPH08216172A (en) | Method for producing fiber-reinforced thermoplastic resin foam | |
| JPH09150463A (en) | Method for producing fiber-reinforced thermoplastic resin foam | |
| JPH10113943A (en) | Continuous production method of fiber reinforced thermoplastic resin foam | |
| JPH08300434A (en) | Method for producing fiber-reinforced thermoplastic resin molding | |
| JPH09234801A (en) | Method for producing fiber-reinforced resin foam and fiber-reinforced resin foam | |
| JP3214892B2 (en) | Method for producing hollow cross-section shaped body | |
| JPH1067052A (en) | Continuous production method of fiber reinforced thermoplastic resin foam | |
| JPH10166465A (en) | Method for producing fiber-reinforced resin foam | |
| JPH08300537A (en) | Fiber reinforced thermoplastic resin foam | |
| JPH08300536A (en) | Fiber-reinforced thermoplastic hollow elongate foam and method for producing the same | |
| JPH08300373A (en) | Method for producing fiber-reinforced thermoplastic resin foam | |
| JPH1067051A (en) | Continuous production method of fiber reinforced thermoplastic resin foam | |
| JPH08174697A (en) | Method for producing fiber-reinforced thermoplastic resin foam |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20070903 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080903 Year of fee payment: 9 |
|
| LAPS | Cancellation because of no payment of annual fees |