JPH02235613A - Manufacture of fiber reinforced thermosetting synthetic resin molding - Google Patents

Manufacture of fiber reinforced thermosetting synthetic resin molding

Info

Publication number
JPH02235613A
JPH02235613A JP1055765A JP5576589A JPH02235613A JP H02235613 A JPH02235613 A JP H02235613A JP 1055765 A JP1055765 A JP 1055765A JP 5576589 A JP5576589 A JP 5576589A JP H02235613 A JPH02235613 A JP H02235613A
Authority
JP
Japan
Prior art keywords
synthetic resin
molding
resin
web
kneading
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP1055765A
Other languages
Japanese (ja)
Inventor
Shigeo Go
郷 茂夫
Toshio Fujii
敏雄 藤井
Tetsushi Kamizono
神園 徹志
Toyomitsu Kondo
近藤 豊光
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP1055765A priority Critical patent/JPH02235613A/en
Publication of JPH02235613A publication Critical patent/JPH02235613A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C39/00Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
    • B29C39/003Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C39/00Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
    • B29C39/22Component parts, details or accessories; Auxiliary operations
    • B29C39/24Feeding the material into the mould
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/0005Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor using fibre reinforcements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2077/00Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Reinforced Plastic Materials (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Moulding By Coating Moulds (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To make material sizing unnecessary and enable automatic molding by molten-kneading a web-shaped material containing thermoplastic synthetic resin and fibrous substance of 3-100mm in length at a specified volumetric rate by a screw type kneading extruding machine, and obtaining a molding then. CONSTITUTION:A web-shaped material containing thermoplastic synthetic resin of 60-90vol.%, fibrous substance of 10-40vol.% and fibers of 3-100mm in length is introduced into a screw type kneading extruding machine equipped with a heating unit inside a barrel and/or screw, and molten-kneading them, and then the molten kneaded matters are supplied into a molding mold or injection mold, and thus obtaining a molding. Olefin resin of polypropylene, polyethylene, ethylene-propylene copolymer or the like, and amide resin of nylon 6, nylon 6-10 or the like are sued as thermoplastic resin. And,inorganic fibers of glass fiber, carbon fiber, boron fiber or the like as well as organic fibers of synthetic or natural fiber can also be used as a fibrous substance.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は/繊雄強化熱可塑性合成樹脂成形品の製造方法
に関する。詳しくは、成形性、材料ロス、成形効率等に
優れたメ繊維強化熱可塑性合成樹脂成形品tM造する方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a fiber-reinforced thermoplastic synthetic resin molded article. More specifically, the present invention relates to a method for producing fiber-reinforced thermoplastic synthetic resin molded products having excellent moldability, material loss, molding efficiency, etc.

〔従来の技術及びその課題〕[Conventional technology and its problems]

繊維強化熱可塑性合成樹脂成形品を製造するにあたり材
料としては、短繊維を樹脂に練9込んだ、所謂コンパウ
ンド材料や、長繊維のマットに樹脂を含浸させた材料等
がある。
Materials for producing fiber-reinforced thermoplastic synthetic resin molded articles include so-called compound materials in which short fibers are kneaded into resin, and materials in which mats of long fibers are impregnated with resin.

又、せんい長として中間領域(3〜toorttx)の
せんいを用いた複合材がある。コンパウンド材料はペレ
ット形態で供給されるが、後コ者はその製法上可撓性の
あるウェブ状シート形態又は樹脂を一旦溶融してプレス
することにより板状シート形態で供給される。
Further, there is a composite material using fibers in the intermediate region (3 to ttx) as the fiber length. The compound material is supplied in the form of pellets, but the material is supplied in the form of a flexible web-like sheet due to its manufacturing method, or in the form of a plate-like sheet by melting the resin once and pressing it.

上記のシート形態の材料を用いて成形品を得る方法とし
ては、まず原反シー}1成形品の重量、形状に合わせて
切断し、次にこのシー}t赤外線ヒーターや熱風ヒータ
ー等により加熱して樹脂を溶融状態とし、これを熱間プ
レス装置の金型上に搬送し、プレス成形することによシ
成形品を得ている。
To obtain a molded product using the above-mentioned material in the form of a sheet, first the original sheet is cut according to the weight and shape of the molded product, and then this sheet is heated with an infrared heater, hot air heater, etc. The resin is molten, transferred onto a mold of a hot press machine, and press-molded to obtain a molded product.

しかしながら、この方法Kは、以下に述べるような問題
点が存在する。
However, this method K has the following problems.

a)個々の成形品に応じて、原反シートを切断、サイジ
ングしなけ粁ぱならず、工程的に繁雑で効率が悪く、切
端が出るので材料ロスも多い。
a) The raw sheet must be cut and sized according to each individual molded product, making the process complicated and inefficient, and there is a lot of material loss due to the production of cut edges.

b)  加熱溶融状態のシートt搬送し,たりせねばな
らず、ハンドリングが複雑で自動化が難かしい。
b) Sheets in a heated and molten state must be transported and dried, making handling complicated and difficult to automate.

C)加熱溶融状態のシートが比較的長くオーノン状態で
あるため、発煙、臭気等が作業環境を悪化する。
C) Since the sheet in the heated and molten state remains in the ohnon state for a relatively long time, smoke, odor, etc. deteriorate the working environment.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者等は、前述のような課題全解決するべく鋭意検
討を行なった結果、特定量及び・特定範囲の長さの繊維
状物質全含有するウエブ形態の熱可塑性合成樹脂材料全
特定の方法で溶融混練して成形することにより目的を達
成し得ることを見出し、本発明を完成するに至った。
As a result of intensive studies aimed at solving all of the above-mentioned problems, the present inventors have developed a method for completely specifying a thermoplastic synthetic resin material in the form of a web containing all fibrous substances in a specific amount and length within a specific range. It was discovered that the object could be achieved by melt-kneading and molding, and the present invention was completed.

すなわち、本発明の要旨は、熱可塑性合成樹脂60〜9
Q容量%、繊維状物質/ 0 =− uθ容量係、かつ
せんい長3〜ioo■のせんい全含有するウェブ状原材
料全バレル及び/又はスクリュー内部に加熱装量全備え
たスクリュー式混練押出機に導入して溶融混練を行ない
、該溶融混練物tプレス成形金型又は射出成形金型に供
給し、成形品を得ること全特命とする繊維強化熱可塑性
合成樹脂成形品の製造方法に存する。
That is, the gist of the present invention is that thermoplastic synthetic resin 60-9
Q volume %, fibrous material / 0 = - uθ capacity ratio, and all web-like raw materials containing all fibers with a length of 3 to ioo The present invention relates to a method for producing a fiber-reinforced thermoplastic synthetic resin molded article, in which the melt-kneaded product is introduced, melt-kneaded, and supplied to a press mold or injection mold to obtain a molded product.

本発明の方法に用い得る熱可塑性合成樹脂とし,てぱ、
ボリプロビレン、ポリエチレン、エチレンー・プロピレ
ン共重合体、エチレンー酢酸ヒニル共重合体等のオレフ
ィン系樹脂、ナイロン6、ナイロン6−6、ナイロンA
−/0,ナイロン7.2等のアミド系樹脂、ポリエチレ
ンテレフタレート、ポリブチレンテレフタレート等のエ
ステル系樹脂、ポリスチレン、アクリロ二トリルースチ
レン共重合体等のスチレン系樹脂、ポリ塩化ビニル、ポ
リ塩化ビニリデン等の塩化ビニル系樹脂等、通常押出成
形や射出成形に用いらnている熱可塑性合成樹脂が挙げ
らnる。
The thermoplastic synthetic resin that can be used in the method of the present invention includes:
Olefin resins such as polypropylene, polyethylene, ethylene-propylene copolymer, ethylene-hinyl acetate copolymer, nylon 6, nylon 6-6, nylon A
-/0, amide resins such as nylon 7.2, ester resins such as polyethylene terephthalate and polybutylene terephthalate, styrene resins such as polystyrene and acrylonitrile-styrene copolymers, polyvinyl chloride, polyvinylidene chloride, etc. Examples include thermoplastic synthetic resins commonly used in extrusion molding and injection molding, such as vinyl chloride resins.

中でも成形性、強度等の点からオレ7イン系樹脂が好ん
で用いらnる。
Among these, ole7-based resins are preferably used from the viewpoint of moldability, strength, etc.

本発明の方法に用い得る繊維状物質としてはガラス繊維
、炭素禮維、金属繊維、ウイスカ、ピロン繊維等の無機
繊維のほか合成又は天然の有機繊維等も用い得る。通常
はガラス繊維又は炭素繊維が用いらむる。
As the fibrous material that can be used in the method of the present invention, in addition to inorganic fibers such as glass fibers, carbon fibers, metal fibers, whiskers, and pilon fibers, synthetic or natural organic fibers can also be used. Usually glass fiber or carbon fiber is used.

繊維状物質としては長さ3〜/0θ謬程度、好1しくけ
3〜50W程度のものが好適に用いられる。
As the fibrous material, a material having a length of about 3 to 0.theta. and a thickness of about 3 to 50 W is preferably used.

本発明においてウエブ状原材料とは、長さ3〜/0θ鰭
程度、好ましくは3〜SO■程度で径が50〃以下の繊
維状物質を10−ダθ容量係と、平均粒径が2■以下の
粒状熱可塑性合成樹脂(粒状樹脂){ijO−90容量
チ含有し、前記繊維状物質を厚さ0./〜30■程度の
マツト状、ンート状等(以下シート状と云う)としと てその内部に粒状樹脂/接着状態又は非接着状態で分散
させた構造とさnておシ、全体として通気性金有し、ロ
ール状に巻回し得る程度の柔軟性と自己保持性を有する
ものである。
In the present invention, the web-like raw material is defined as a fibrous material having a length of about 3 to 0 θ fins, preferably about 3 to 0 SO, a diameter of 50 or less, and an average particle size of 2 Contains the following granular thermoplastic synthetic resin (granular resin) {ijO-90 by volume, and the fibrous material has a thickness of 0. It has a structure in which granular resin is dispersed in an adhesive or non-adhesive state in the form of a pine-like, sheet-like, etc. (hereinafter referred to as a sheet-like) material of about 30 mm, and is breathable as a whole. It is made of metal and has enough flexibility and self-retention ability to be wound into a roll.

ンート状の繊維状物質自体の形状及び繊維状物質中に分
散された粒状樹脂を保持する手段として、粒状樹脂及び
繊維状物質の合計量に対してθ,θ/〜5重量チ程度の
接着剤を用いて繊維状物質同志の接点部分や繊維状物質
と粒状樹脂との接触部分を接着したり、繊維状物質中に
分散さnた粒状樹脂に熱を加え、粒状樹脂の一部(表面
)全溶融させ、繊維状物質の交差部分及び/又は繊維状
物質と粒状樹脂金融着させた状態とする等の手段が用い
られる。
As a means to hold the shape of the fibrous material itself and the granular resin dispersed in the fibrous material, an adhesive of about θ, θ/~5% by weight is applied to the total amount of the granular resin and fibrous material. By applying heat to the granular resin dispersed in the fibrous material, a part (surface) of the granular resin can be bonded by using a fibrous material to bond the contact points between the fibrous materials or between the fibrous material and the granular resin, or by applying heat to the granular resin dispersed in the fibrous material. Means such as completely melting the fibrous material and bringing it into a state where the fibrous material intersects with the fibrous material and/or the fibrous material and the granular resin material are bonded is used.

前記した接着剤としては例えばポリ酢酸ビニル、ポリア
クリル酸エステル、合成ゴム、カルポキンメチルセルロ
ース、デキストリン、ポリビニルアルコール、澱粉等が
好適に用いられる−。
As the above adhesive, for example, polyvinyl acetate, polyacrylic acid ester, synthetic rubber, carpoquin methylcellulose, dextrin, polyvinyl alcohol, starch, etc. are suitably used.

ウエブ形態の原料シート全構成する熱可塑性合成樹脂と
繊維状物質との割合は繊維状物質が/θ〜lIo容量壬
であることが必要である。
It is necessary that the ratio of the thermoplastic synthetic resin and the fibrous material constituting the entire raw material sheet in the form of a web is such that the fibrous material has a volume of /θ to lIo.

/O容量11少ないと強化の役を果たさず、lIo容量
%を超えると溶融材料の流動性が低下し、成形時に不利
となる。
If the /O capacity is less than 11%, it will not serve as a reinforcement, and if it exceeds 1Io volume%, the fluidity of the molten material will decrease, which will be disadvantageous during molding.

以下、図面を用いて本発明の方法の一例につき更に詳細
に説明する。
Hereinafter, an example of the method of the present invention will be explained in more detail using the drawings.

第l図は本発明の方法に用いて好適な装置の一例を一部
断面にして表わした哉明図である。
FIG. 1 is a partial cross-sectional view of an example of an apparatus suitable for use in the method of the present invention.

図中lは原材料(ウェブ)、コは混練機、3はヒーター
 lはアキュムレーター 5はパルブ、6は導管、7は
バルプ、g:,g’は下及び上金型をそnぞ扛示す。
In the figure, l is the raw material (web), c is the kneading machine, 3 is the heater, l is the accumulator, 5 is the valve, 6 is the conduit, 7 is the valve, g:, g' are the lower and upper molds. .

原材料lは熱可塑性合成樹脂60〜90容量チと長さ3
〜/00■の繊維状物質/0−グθ容量チとからなるウ
エブ状原材料である。
Raw material l is a thermoplastic synthetic resin with a capacity of 60 to 90 and a length of 3.
It is a web-like raw material consisting of a fibrous material of ~/00■/0-g θ capacity Q.

ウェブ状原材料lは柔軟であるから図示するように巻芯
等に巻回して取扱うことができるし、勿論、所定の寸法
に切断したシート状の材料としても取扱える。
Since the web-like raw material 1 is flexible, it can be handled by being wound around a core as shown in the figure, and of course, it can also be handled as a sheet-like material cut into predetermined dimensions.

ウェブ状の原材料/は、次いでヒーター一が設けら扛た
スクリュー式の混練機乙に送ら扛、溶融混練される。混
練機はスクリューの内部にもヒーターを有する構造にな
っているものが好ましい。
The web-shaped raw material is then sent to a screw-type kneader B equipped with a heater B, where it is melted and kneaded. It is preferable that the kneader has a structure in which a heater is also provided inside the screw.

この溶融混練はあま9強く行なうと繊維状物質が折扛て
しまうので、軽い混練が好ましく、原材料/中の樹脂の
溶融、ガス抜き、加圧、均一分散を行なうのが目的であ
る。この為、スクリューの7イードゾー//ヲ材料が通
過する時間が/S秒以上となるような滞留時間の長いス
クリュー形状、回転数とするのが望ましい。
If this melt-kneading is carried out too vigorously, the fibrous material will break, so light kneading is preferred, and the purpose is to melt, degas, pressurize, and uniformly disperse the resin in the raw materials/inside. For this reason, it is desirable to have a screw shape and rotation speed that provides a long residence time so that the material passes through the screw for at least /S seconds.

溶融混練物は、そのままプレス金型等に送らnても良い
が、図示するようにバルプを経てアキュムレーターダに
一旦溜めら詐るのが計量を正確とし、送シ出しを一気に
かつスムーズに行なう上で好ましい。
The molten and kneaded material may be sent as is to a press mold, etc., but as shown in the figure, it is best to pass through a valve and accumulate it in an accumulator for accurate metering and smooth delivery all at once. preferred above.

アキュムレーターダに溜められた溶融混練物は導管6を
通じて下金型g上に供給さnる。導管6はフレキシブル
なものとさnているのが良い。これによυ下金型の任意
の位置に溶融混練物を任意量供給し得ることとなり、厚
み変化の大きい成形品にも対応し得る。逆に金型g,g
’が位置を動かし得るようにさ扛ていても同様の効果が
ある。金型への供給のタイミングはノ《ルフ7で行なわ
れる。
The molten kneaded material stored in the accumulator is supplied onto the lower mold g through the conduit 6. Preferably, the conduit 6 is flexible. This makes it possible to supply an arbitrary amount of the melt-kneaded material to an arbitrary position of the lower mold, and it is possible to handle molded products with large thickness changes. On the contrary, mold g, g
A similar effect can be obtained even if ' is moved so that it can be moved. The timing of supply to the mold is done at Nolf 7.

図はプレス成形用の金型g.g’+示したが、ここに射
出成形の金型を置き、射出成形を行なうことも可能であ
る。
The figure shows a press mold g. Although g'+ is shown, it is also possible to place an injection mold here and perform injection molding.

この場合アキュムレーターグから一気に溶融混練物を射
出し、射出成形金型のキャビテイーに充填すれば良い。
In this case, the melted and kneaded material may be injected all at once from the accumulator tag and filled into the cavity of the injection mold.

射出成形の場合、繊維状物質として長さの短かいもの、
すなわち長さ/Owr以下、好ましくは3ms以下のも
のを用いるのが、分散性等の点から好ましい。
In the case of injection molding, short length fibrous materials,
That is, it is preferable to use one having a length of less than /Owr, preferably less than 3 ms, from the viewpoint of dispersibility and the like.

本発明の方法に用いる装置はアキュムレータ一方式が好
ましいが、混練時にスクリエーが後退してシリンダーの
先端部に溶融混練物を溜め、スクリエーが一気に前進し
て溶融混練物を射出(押し出し)する゜所.謂スクリュ
ーインライン式の成形機等も採用することができる。
The apparatus used in the method of the present invention is preferably a one-type accumulator, but it is a place where the screer retreats during kneading to accumulate the melted mixture at the tip of the cylinder, and the screier moves forward all at once to inject (extrude) the melted mixture. .. A so-called screw in-line molding machine or the like can also be employed.

〔発明の効果〕 成形品ごとに原反ウエブ状原材料をサイジングする等の
工程が不要なので切端ロス等の発生が少ない。また、肉
厚変化のある成形品にも容易に対応でき、作業も簡便で
ちる。加熱状態にあるシート等がオープンにならないの
で発煙、臭気等の問題がない。成形システムの自動化が
容易である等実用上大変効果的である。
[Effects of the Invention] Since there is no need for processes such as sizing the original web-like raw material for each molded product, there is less occurrence of edge loss. In addition, it can easily handle molded products with changes in wall thickness, and the work is simple and easy. Since the heated sheets do not open, there are no problems with smoke, odor, etc. It is very effective in practical terms, such as the ease of automating the molding system.

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

第l図は本発明の方法に用いて好適な装置の一例を一部
断面にして表わした説明図である。 図中lは原材料(ウェブ)、コは混練機、3はヒーター
 弘はアキュムレーター 5はバルプ、6は導管、7は
バルプ、g,g’は下及び上金型をそnぞれ示す。
FIG. 1 is an explanatory diagram showing an example of a device suitable for use in the method of the present invention, partially in section. In the figure, l is the raw material (web), c is the kneading machine, 3 is the heater, Hiro is the accumulator, 5 is the bulb, 6 is the conduit, 7 is the bulb, and g and g' are the lower and upper molds, respectively.

Claims (1)

【特許請求の範囲】[Claims] (1)熱可塑性合成樹脂60〜90容量%、長さ3〜1
00mmの繊維状物質10〜40容量%を含有するウェ
ブ状原材料をバレル及び/又はスクリュー内部に加熱装
置を備えたスクリュー式混練押出機に導入して溶融混練
を行ない、この溶融混練物をプレス成形金型又は射出成
形金型に供給し、成形品を得ることを特徴とする繊維強
化熱可塑性合成樹脂成形品の製造方法。
(1) Thermoplastic synthetic resin 60-90% by volume, length 3-1
A web-like raw material containing 10 to 40% by volume of 00 mm fibrous material is introduced into a screw-type kneading extruder equipped with a heating device inside the barrel and/or screw to perform melt-kneading, and this melt-kneaded product is press-molded. 1. A method for producing a fiber-reinforced thermoplastic synthetic resin molded article, which comprises supplying a molded article to a mold or an injection mold to obtain a molded article.
JP1055765A 1989-03-08 1989-03-08 Manufacture of fiber reinforced thermosetting synthetic resin molding Pending JPH02235613A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1055765A JPH02235613A (en) 1989-03-08 1989-03-08 Manufacture of fiber reinforced thermosetting synthetic resin molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1055765A JPH02235613A (en) 1989-03-08 1989-03-08 Manufacture of fiber reinforced thermosetting synthetic resin molding

Publications (1)

Publication Number Publication Date
JPH02235613A true JPH02235613A (en) 1990-09-18

Family

ID=13007953

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1055765A Pending JPH02235613A (en) 1989-03-08 1989-03-08 Manufacture of fiber reinforced thermosetting synthetic resin molding

Country Status (1)

Country Link
JP (1) JPH02235613A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5653534A (en) * 1994-10-12 1997-08-05 Sumitomo Chemical Company, Limited Screw apparatus and method for supplying reinforcing fiber-containing molten resin using the apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5653534A (en) * 1994-10-12 1997-08-05 Sumitomo Chemical Company, Limited Screw apparatus and method for supplying reinforcing fiber-containing molten resin using the apparatus

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