JPH02182421A - Manufacture of fiber reinforced thermoplastic synthetic resin molded article - Google Patents
Manufacture of fiber reinforced thermoplastic synthetic resin molded articleInfo
- Publication number
- JPH02182421A JPH02182421A JP64000998A JP99889A JPH02182421A JP H02182421 A JPH02182421 A JP H02182421A JP 64000998 A JP64000998 A JP 64000998A JP 99889 A JP99889 A JP 99889A JP H02182421 A JPH02182421 A JP H02182421A
- Authority
- JP
- Japan
- Prior art keywords
- synthetic resin
- thermoplastic synthetic
- raw material
- kneaded
- supplied
- 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
Links
- 229920001169 thermoplastic Polymers 0.000 title claims abstract description 22
- 239000004416 thermosoftening plastic Substances 0.000 title claims abstract description 22
- 229920003002 synthetic resin Polymers 0.000 title claims abstract description 21
- 239000000057 synthetic resin Substances 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000000835 fiber Substances 0.000 title description 6
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 238000004898 kneading Methods 0.000 claims abstract description 9
- 238000002844 melting Methods 0.000 claims abstract description 8
- 230000008018 melting Effects 0.000 claims abstract description 8
- 238000000465 moulding Methods 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims description 15
- 229920005989 resin Polymers 0.000 claims description 12
- 239000002657 fibrous material Substances 0.000 claims description 11
- 239000011347 resin Substances 0.000 claims description 11
- 238000001746 injection moulding Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 19
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 239000000853 adhesive Substances 0.000 abstract description 2
- 230000001070 adhesive effect Effects 0.000 abstract description 2
- 239000004745 nonwoven fabric Substances 0.000 abstract description 2
- 239000000843 powder Substances 0.000 abstract description 2
- -1 polypropylene Polymers 0.000 description 4
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000003365 glass fiber Substances 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- UPZFLZYXYGBAPL-UHFFFAOYSA-N 2-ethyl-2-methyl-1,3-dioxolane Chemical compound CCC1(C)OCCO1 UPZFLZYXYGBAPL-UHFFFAOYSA-N 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 229920001893 acrylonitrile styrene Polymers 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- SCUZVMOVTVSBLE-UHFFFAOYSA-N prop-2-enenitrile;styrene Chemical compound C=CC#N.C=CC1=CC=CC=C1 SCUZVMOVTVSBLE-UHFFFAOYSA-N 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000012260 resinous material Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920006163 vinyl copolymer Polymers 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C39/00—Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
- B29C39/22—Component parts, details or accessories; Auxiliary operations
- B29C39/24—Feeding the material into the mould
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C39/00—Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
- B29C39/003—Shaping 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/0005—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor using fibre reinforcements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
- B29K2105/08—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of continuous length, e.g. cords, rovings, mats, fabrics, strands or yarns
- B29K2105/0854—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of continuous length, e.g. cords, rovings, mats, fabrics, strands or yarns in the form of a non-woven mat
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は繊維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
′fした繊維強化熱可塑性合成樹脂成形品全製造する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a fiber-reinforced thermoplastic synthetic resin molded article. Specifically, the present invention relates to a method for producing fiber-reinforced thermoplastic synthetic resin molded articles that are superior in moldability, material loss, molding efficiency, and the like.
/
繊維強化熱可塑性合成樹脂成形品を製造する方法として
は、短繊維を樹脂に練り込んだ、所謂コンパウンド材料
や、長繊維のマントに樹脂を含浸させた材料等がある。/ Methods for manufacturing fiber-reinforced thermoplastic synthetic resin molded products include so-called compound materials in which short fibers are kneaded into resin, and materials in which long fiber cloaks are impregnated with resin.
こnらの材料を用いて成形品を得る方法としては、筐ず
原反シートを成形品の重量、形状に合わせて切断し、次
にこのシートラ赤外線ヒーターや熱風ヒーター等により
加熱して樹脂全溶融状態とし、こn’i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り成形品を
得ている。The method of obtaining molded products using these materials is to cut the original Kahozu sheet according to the weight and shape of the molded product, and then heat the sheet with an infrared heater, hot air heater, etc. to completely remove the resin. A molded product is obtained by bringing it into a molten state, conveying it onto a mold of a hot press machine, and press-molding it.
しかしながら、この方法には、以下に述べるような問題
点が存在する。However, this method has the following problems.
a)個々の成形品に応じて、原反シー)&切断、サイジ
ングしなけ扛ばならず、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) Depending on the individual molded product, it is necessary to perform raw fabric sheathing, cutting, and sizing, which makes the process complicated and inefficient, and there is a lot of material loss because of the production of cut ends.
b)加熱溶融状態のンートヲ搬送したすせねばならず、
ハンドリングが複雑で自動化が難かしい。b) The material must be transported in a heated and molten state,
Handling is complicated and automation is difficult.
C)加熱溶融状態のシートが比較的長くオープン状態で
あるため、発煙、臭気等が作業環境を悪化する。C) Since the heated and molten sheet remains open for a relatively long time, smoke, odor, etc. deteriorate the working environment.
本発明者等は、前述のような課題を解決するべく鋭意検
討を行なった結果、特定量の繊維状物質を含有する熱可
塑性合成樹脂ウェブ又は板状物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 to solve the above-mentioned problems, the present inventors have found that a thermoplastic synthetic resin web or plate-like material containing a specific amount of fibrous material can be melt-kneaded and molded using a specific method. The inventors have discovered that the object can be achieved by doing the following, and have completed the present invention.
すなわち、本発明の要旨は、熱可塑性合成樹脂60〜9
θ容量係、繊維状物質1o−eo答量St含有する原材
料をウェブ状又は板状で供給し、これを前記熱可塑性合
成樹脂の融点以上の温度に予熱し、予熱状態のままスク
リュー式混練機に導入して溶融混練を行ない、該溶融混
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
形品の製造方法に存する。That is, the gist of the present invention is that thermoplastic synthetic resin 60-9
A raw material containing θ volume ratio, fibrous material 1o-eo answer St is supplied in the form of a web or plate, and this is preheated to a temperature equal to or higher than the melting point of the thermoplastic synthetic resin, and is then passed through a screw kneader in the preheated state. The present invention relates to a method for producing a fiber-reinforced thermoplastic synthetic resin molded article, characterized in that the melt-kneaded product is introduced into a press mold or an injection mold to obtain a molded article.
本発明の方法に用い得る熱可塑性合成樹脂とシテハ、ポ
リプロピレン、ポリエチレン、エチレン−プロピレン共
重合体、エチレン−酢eビ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6−I
O、ナイロン12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、アクリロニトリル−スチレン共
重合体等のスチレン系樹脂、ポリ塩化ビニル、ボIJ
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れている熱可塑性合成樹脂が挙げら
れる。Thermoplastic synthetic resins that can be used in the method of the present invention, olefinic resins such as silica, polypropylene, polyethylene, ethylene-propylene copolymer, ethylene-acetic acid e-vinyl copolymer, nylon 6, nylon 6-6, nylon 6- I
O, amide resins such as nylon 12, ester resins such as polyethylene terephthalate and polybutylene terephthalate, styrene resins such as polystyrene, acrylonitrile-styrene copolymer, polyvinyl chloride, plastic IJ
Examples include thermoplastic synthetic resins commonly used in extrusion molding and injection molding, such as vinyl chloride resins such as vinylidene chloride.
中でも成形性、強度等の点からオレフィン系樹脂が好ん
で用いられる。Among them, olefin 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
、炭素繊維、金属繊維、ウィスカ、ボロン繊維等の無機
繊維のほか合成又は天然の有機繊維等も用い得る。通常
はガラス繊維又は好ましくは3〜!rOmg程度のもの
が好適に用いらn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 boron fibers, synthetic or natural organic fibers can also be used. Usually glass fiber or preferably 3~! A substance of about rOmg is preferably used.
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
10−リ0答量係であることが必要である。108量係
より少ないと強化の役を果たさず、グθ容量%(H超え
ると均一な溶融混練が行なえなくなる。The ratio of the thermoplastic synthetic resin to the fibrous material must be such that the amount of the fibrous material is 10-1. If it is less than 108% by volume, it will not serve as a reinforcement, and if it exceeds θ volume % (H), uniform melting and kneading will not be possible.
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1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。FIG. 1 is an explanatory diagram showing, partially in cross section, 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)、コは予熱装置、3はエアー
ポンプ、lはヒーター; Sは多孔ドラム、6は混練機
、7はヒーター、gはアキュムレーター、デはパルプ、
IOは導管1.、はパルプ、ia、i2’は下及び上金
型をそれぞn示すO
原材料lは熱可塑性合成樹脂40−90容量係と繊維状
物質lO〜e(17容量係とからなり取扱いの上から繊
維状物質を不織布状とし、これに粉状、微粒状の熱可塑
性合成樹脂を僅かに溶着させたり、接着成分を用いたシ
して担持させたもの(ウェブ状)が好ましい。このよう
な構造とすれば、巻芯等に巻回して取シ扱うことができ
る。勿論、このウェブ状のものを加熱して樹脂成分′f
rg融させた後冷却固化す扛ば硬い板状体が得られるが
、このような板状体を原材料とすることもできる。板状
体を原材料とする場合には、次の予熱工程をウェブ状の
ものとは異なった方法で行なうこととなろう。In the figure, l is the raw material (web), C is the preheating device, 3 is the air pump, l is the heater; S is the porous drum, 6 is the kneading machine, 7 is the heater, g is the accumulator, D is the pulp,
IO is conduit 1. , are pulp, ia, i2' are lower and upper molds, respectively. Raw material l is a thermoplastic synthetic resin with a volume of 40-90 and a fibrous material lO~e (with a volume of 17). Preferably, the fibrous material is in the form of a non-woven fabric and a thermoplastic synthetic resin in the form of powder or fine particles is slightly welded or supported using an adhesive component (web form).Such a structure If so, it can be handled by winding it around a core, etc.Of course, this web-like material can be heated to release the resin component 'f.
If the material is melted and then cooled and solidified, a hard plate-like body can be obtained, but such a plate-like body can also be used as a raw material. If a plate-like material is used as the raw material, the subsequent preheating step will be performed in a different manner than when a web-like material is used.
供給さnた原材料l(ウェブ状の場合)は次いで予熱装
置コに送ら扛る。図示した予熱装置コは多孔ドラムが内
蔵されたものであり、ウェブlをこの多孔ドラムに巻回
して移送しつつ、ヒーター弘で加熱された空気を多孔ド
ラムの外側から内側に通過させ、この熱によシウエプl
を加熱する方法のものである。従ってこの装置の場合、
原材料が可撓性のウェブ状のものに適用される。硬い板
状の原材料を用いる場合には平らな状態で移送しつつ遠
赤外線ヒーターや熱風ヒーター等により加熱することと
なろう。The supplied raw material (if it is in the form of a web) is then sent to a preheating device to be scraped. The preheating device shown in the figure has a built-in perforated drum, and while the web 1 is wound around this perforated drum and transferred, air heated by a heater is passed from the outside of the perforated drum to the inside, and this heat is transferred. Yoshiuepu l
It is a method of heating. Therefore, for this device,
The raw material is applied in the form of a flexible web. If a hard plate-shaped raw material is used, it will be heated with a far-infrared heater, hot air heater, etc. while being transported in a flat state.
この予熱は、原材料の熱可塑性合成樹脂の融点以上、好
ましくは融点より20℃以上、より好ましくは融点より
50℃以上の温度まで加熱さ扛る。勿論樹脂が分解を起
すような温度にまで加熱しない。This preheating involves heating to a temperature higher than the melting point of the raw thermoplastic synthetic resin, preferably 20° C. or higher than the melting point, and more preferably 50° C. or higher than the melting point. Of course, the resin should not be heated to a temperature that would cause it to decompose.
予熱さnた樹脂と繊維状物質とからなる原材料ハ、次い
でヒータークが設けら扛たスクリュー式の混練8乙に送
らn1浴融混練さnる。The raw material consisting of preheated resin and fibrous material is then sent to a screw-type kneading chamber equipped with a heater and melt-kneaded in a bath.
この溶綜混練はあまり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、原材料中のガス抜き
、加圧、均一分散を行なうのが目的である。If this melt-kneading is performed too vigorously, the fibrous material will break, so light kneading is preferred, and the purpose is to degas, pressurize, and uniformly disperse the raw materials.
溶融混練物は、その筐まプレス金型等に送られても良い
が、図示するようにパルプ9を経てアキュムレーターg
に一旦溜めらnるのが計量全正確とし、送り出しを一気
にかつスムーズに行なう上で好ましい。The melted and kneaded material may be sent to its box or press mold, but as shown in the figure, it passes through the pulp 9 and is then sent to the accumulator g.
It is preferable to accumulate the amount once to ensure accurate measurement and to perform smooth delivery all at once.
アキュムレーターgに溜めらnた溶融混練物は導管10
を通じて下金型lコ上に供給さnる。The melted and kneaded material accumulated in the accumulator g is transferred to the conduit 10.
The material is fed through the lower mold onto the lower mold.
導管ioはフレキシブルなものとされているのが良い。The conduit io is preferably flexible.
こ扛により下金型の任意の位置に溶融混練物を任意世供
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/λ、/、2’が位置を動かし得るよ
うにさnていても同様の効果がある。金型への供給のタ
イミングはパルプ/lで行なわれる。By this method, the melted and kneaded material can be supplied to any desired position of the lower mold, and it is possible to handle molded products with large thickness changes. Conversely, the same effect can be obtained even if the mold /λ, /, 2' is made movable. The timing of supply to the mold is done in pulp/l.
図はプレス成形用の金型lコ、/2’f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。Although the figure shows a mold for press molding, 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g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ィ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 g 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lO++I!I+以下、好ましくは5問以
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, the length lO++I! It is preferable to use questions of I+ or less, preferably 5 or less questions, from the viewpoint of dispersibility.
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、混練時にスクリューが後退してンリンダーの
先端部に浴融混練物を溜め、スクリ、−が一気に前進し
て浴融混練物を射出(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 during kneading, the screw retreats and accumulates the bath melt kneaded material at the tip of the unlinder, and the screw advances all at once to inject (extrude) the bath melt kneaded material. ) may also be used.
成形品ごとに原反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、作業も簡便である。加熱状態
にあるシート等がオープンになる時間は短かいので発煙
、臭気等の問題が少ない。成形ン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。There is no need for processes such as sizing the original fabric for each molded product, so 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. Since the time when the heated sheet etc. is open is short, there are fewer problems such as smoke and odor. It is very effective in practical terms, as it is easy to automate the forming stem.
第1図は本発明の方法に用いて好適な装置の一例金一部
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)、2は予熱装置、3はエアー
ポンプ、qはヒーター 5は多孔ドラム、乙は混練機、
7はヒーター gはアキュムレーター タはパルプ、I
Oは導管、llはパルプ、/2./l’は下及び止金型
をそ扛ぞれ示す。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), 2 is the preheating device, 3 is the air pump, q is the heater, 5 is the perforated drum, O is the kneading machine,
7 is heater g is accumulator ta is pulp, I
O is conduit, ll is pulp, /2. /l' indicates the bottom and clasp molds respectively.
Claims (1)
10〜40容量%を含有する原材料をウェブ状又は板状
で供給し、これを前記熱可塑性合成樹脂の融点以上の温
度に予熱し、予熱状態のままスクリュー式混練機に導入
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) A raw material containing 60 to 90% by volume of a thermoplastic synthetic resin and 10 to 40% by volume of a fibrous material is supplied in the form of a web or plate, and this is preheated to a temperature equal to or higher than the melting point of the thermoplastic synthetic resin. , a fiber-reinforced thermoplastic composition characterized in that it is introduced into a screw kneader in a preheated state to perform melt-kneading, and the melt-kneaded product is supplied to a press molding mold or an injection molding mold to obtain a molded product. Method for manufacturing resin molded products.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP64000998A JPH02182421A (en) | 1989-01-06 | 1989-01-06 | Manufacture of fiber reinforced thermoplastic synthetic resin molded article |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP64000998A JPH02182421A (en) | 1989-01-06 | 1989-01-06 | Manufacture of fiber reinforced thermoplastic synthetic resin molded article |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02182421A true JPH02182421A (en) | 1990-07-17 |
Family
ID=11489259
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP64000998A Pending JPH02182421A (en) | 1989-01-06 | 1989-01-06 | Manufacture of fiber reinforced thermoplastic synthetic resin molded article |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02182421A (en) |
-
1989
- 1989-01-06 JP JP64000998A patent/JPH02182421A/en active Pending
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