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JPS6356048B2 - - Google Patents
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JPS6356048B2 - - Google Patents

Info

Publication number
JPS6356048B2
JPS6356048B2 JP15751583A JP15751583A JPS6356048B2 JP S6356048 B2 JPS6356048 B2 JP S6356048B2 JP 15751583 A JP15751583 A JP 15751583A JP 15751583 A JP15751583 A JP 15751583A JP S6356048 B2 JPS6356048 B2 JP S6356048B2
Authority
JP
Japan
Prior art keywords
mixing
groove
screw
resin
stage
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
Application number
JP15751583A
Other languages
Japanese (ja)
Other versions
JPS6049907A (en
Inventor
Tadahiko Kohama
Susumu Shibata
Atsuo Teraoka
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.)
Aisin Corp
Original Assignee
Aisin Seiki Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Aisin Seiki Co Ltd filed Critical Aisin Seiki Co Ltd
Priority to JP58157515A priority Critical patent/JPS6049907A/en
Publication of JPS6049907A publication Critical patent/JPS6049907A/en
Publication of JPS6356048B2 publication Critical patent/JPS6356048B2/ja
Granted 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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/46Means for plasticising or homogenising the moulding material or forcing it into the mould
    • B29C45/58Details
    • B29C45/60Screws
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/67Screws having incorporated mixing devices not provided for in groups B29C48/52 - B29C48/66

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 本発明は、熱可塑性樹脂とガラス繊維等の無機
質繊維との混合、及び分散を向上するための射出
成形機のスクリユーの改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in the screw of an injection molding machine for improving the mixing and dispersion of a thermoplastic resin and inorganic fibers such as glass fibers.

従来の樹脂成形機のスクリユーについては、特
開昭56−92039号「熱可塑性樹脂成形用スクリユ
ー」及び特開昭58−31728号「プラスチツク押出
機用可塑化混練装置」の公報に、マドツク型スク
リユーについて、ミキシング部に設けたミキシン
グ溝とシリンダー内面との連動作用により、未溶
融樹脂体を含む樹脂を完全に混合,混練する旨開
示されている。
Regarding the screws of conventional resin molding machines, the screws of the conventional resin molding machines are described in the publications of JP-A-56-92039 ``Screws for Thermoplastic Resin Molding'' and JP-A-58-31728 ``Plasticizing and Kneading Apparatus for Plastic Extrusion Machines.'' It is disclosed that the resin including the unmolten resin is completely mixed and kneaded by the interlocking action of the mixing groove provided in the mixing section and the inner surface of the cylinder.

即ち、これを第1図〜第2図により説明すれ
ば、1′はマドツク型スクリユー、2′はフライ
ト、3′はミキシング部、3′aはその外径、3′
bは樹脂の流動を良くするために前記外径3′a
を一部削り取つた部分(斜線で示す)の外径、
4′a,4′b,……はミキシング溝、5′はシリ
ンダー内面、そしてS′はシリンダー内面5′とミ
キシング溝3′bとのスキマである。この様に従
来のマドツク型スクリユーにおいては、ホツパー
側より投入された樹脂は各工程をへて、ミキシン
グ溝4′b,4′c,……及びスキマS′により、実
線で示す様に流動し、加熱,溶融,混合されて樹
脂は完全に分散する。
That is, to explain this with reference to FIGS. 1 and 2, 1' is a screw type screw, 2' is a flight, 3' is a mixing part, 3'a is its outer diameter, and 3'
b is the outer diameter 3'a to improve resin flow.
The outer diameter of the part (indicated by diagonal lines) that has been partially removed,
4'a, 4'b, . . . are mixing grooves, 5' is the inner surface of the cylinder, and S' is the gap between the inner surface of the cylinder 5' and the mixing groove 3'b. In this way, in the conventional mud screw type screw, the resin charged from the hopper side passes through each process and flows through the mixing grooves 4'b, 4'c, ... and the gap S' as shown by the solid line. , heated, melted, and mixed to completely disperse the resin.

然し樹脂にガラス繊維を混合する場合には、次
のような理由により、混練、分散が極めて困難で
ある。即ち、ガラス繊維と樹脂とを直接混練する
場合には、太さ10〜30μmのガラス繊維を数百本
束ね、数mmにカツトして、樹脂と共にホツパーよ
り投入,加熱,圧縮等の工程を経て樹脂とガラス
繊維が混合してミキシング部へフライトにより送
られ、次に溝4′b→スキマS′→溝4′cの経路で
混練され、金型に射出成形されるが、この程度の
混練では分散性が悪く、成形品の各所にガラス繊
維の束がそのまま残る、という不具合があつた。
However, when glass fibers are mixed with resin, kneading and dispersion are extremely difficult for the following reasons. In other words, when directly kneading glass fibers and resin, several hundred glass fibers with a thickness of 10 to 30 μm are bundled, cut into pieces of several mm, and put together with the resin through a hopper, heated, compressed, etc. The resin and glass fibers are mixed and sent by flight to the mixing section, then kneaded along the route of groove 4'b → gap S' → groove 4'c, and injection molded into a mold. However, the problem was that the dispersibility was poor and bundles of glass fibers remained in various parts of the molded product.

この結果、成形品の強度が不均一で、引張り強
度も低くなり、外観も非常に見劣りがするという
欠点がある。これを第3図により説明すれば、イ
は樹脂80%にガラス繊維20%を混入し、前記従来
のマドツク型スクリユーにより、混練成形したも
ので、6′は成形品で、7′a,7′b……はガラ
ス繊維の分散が不充分で束のかたまりの状態で、
その一部をテストピース8′(大きさ50×50mm)
を切り取り、更にその一部分9′を拡大した状況
をハに示す。10′a,10′bはガラス繊維の束
の固まりで、これを写真1に示す。10′a及び
10′bの如く、分散が不充分で外観的にも良好
でないことがよく判る。
As a result, the strength of the molded product is uneven, the tensile strength is low, and the appearance is very poor. To explain this with reference to Fig. 3, A is a mixture of 80% resin and 20% glass fiber, kneaded and molded using the conventional screw type screw, 6' is a molded product, 7'a, 7''b...' is a state in which the glass fibers are not sufficiently dispersed and form a bunch,
Part of it is a test piece 8′ (size 50 x 50 mm)
The situation in which the image is cut out and a portion 9' of the image is further enlarged is shown in FIG. 10'a and 10'b are clusters of glass fiber bundles, which are shown in Photo 1. As shown in samples 10'a and 10'b, it is clearly seen that the dispersion was insufficient and the appearance was not good.

この様に、従来のマドツク型スクリユーにおい
ては、樹脂とガラス繊維との混合,混練が極めて
困難なために、現在のFRPの製造については、
すべて、樹脂とガラス繊維を適量混合して、ペレ
ツトを製造し、このペレツトをホツパーより投入
してFRPを製造しており、コスト高の原因とな
つている。
As described above, since it is extremely difficult to mix and knead the resin and glass fiber with the conventional screw type screw, current production of FRP is difficult.
In all cases, appropriate amounts of resin and glass fiber are mixed to produce pellets, and the pellets are fed into a hopper to produce FRP, which is a cause of high costs.

本発明は、前記欠点を改良したものである。即
ち、樹脂とガラス繊維の混練により、FRPを製
造する場合に、前記ペレツト製造工程を省略し、
直接樹脂とガラス繊維を混練してガラス繊維を均
一に分散させ、強度的にも優れ、且つ外観も良
い、樹脂射出成形機のスクリユーを提供するもの
である。
The present invention improves the above drawbacks. That is, when manufacturing FRP by kneading resin and glass fiber, the pellet manufacturing process is omitted,
To provide a screw for a resin injection molding machine that directly kneads resin and glass fiber to uniformly disperse the glass fiber, has excellent strength, and has a good appearance.

このために、樹脂とガラス繊維を混練するミキ
シング部において、ミキシングするための溝の配
列及び形状に関して、当発明者らは種々テストを
繰返し、その結果、ミキシング部にほぼミキシン
グ部の長さに相当する溝(以下1段のミキシング
溝という)を設け、1段のミキシング溝の両端を
行き止まりとし、次に1段のミキシング溝に平行
して、ミキシング部の長さの約1/2に相当する溝
(以下2段のミキシング溝という)を直列的に配
置し、かつ、1段のミキシング溝と2段のミキシ
ング溝を交互に配列し、2段のミキシング溝のそ
れぞれの一方端はホツパー側及びノズル側に連通
し、かつ1段のミキシング溝と2段のミキシング
溝のうち、ホツパー側に位置する2段のミキシン
グ溝のスクリユー軸の反回転方向側に隣接する1
段のミキシング溝との間に樹脂及びカツトされた
ガラス繊維が通過し易い様にミキシング部の外形
を一部削り取り通路とし、この1段のミキシング
溝とスクリユー回転軸の反回転方向に隣接するノ
ズル側の2段のミキシング溝との間にミキシング
部の外形を一部削り取り、樹脂及びガラス繊維の
通路を設け、スクリユーの作動する射出成形機の
シリンダー内面と前記ミキシング部の外径を削り
取つた壁面とのスキマSを構成したミキシング部
の構造である。
To this end, the inventors have repeatedly conducted various tests regarding the arrangement and shape of the grooves for mixing in the mixing section where resin and glass fiber are kneaded, and as a result, we have found that the length of the mixing section is approximately the same as the length of the mixing section. A groove (hereinafter referred to as a 1-stage mixing groove) is provided, and both ends of the 1-stage mixing groove are dead ends, and then a groove corresponding to approximately 1/2 of the length of the mixing section is installed parallel to the 1-stage mixing groove. Grooves (hereinafter referred to as two-stage mixing grooves) are arranged in series, and the first-stage mixing groove and the second-stage mixing groove are arranged alternately, and one end of each of the two-stage mixing groove is connected to the hopper side and the second-stage mixing groove. 1 which communicates with the nozzle side and is adjacent to the opposite rotation direction side of the screw shaft of the 2-stage mixing groove located on the hopper side among the 1-stage mixing groove and the 2-stage mixing groove.
A part of the outer shape of the mixing part is cut out to make it easy for the resin and cut glass fibers to pass between the mixing groove of the first stage and the nozzle adjacent to the mixing groove of the first stage in the counter-rotational direction of the screw rotation shaft. A part of the outer shape of the mixing part was removed between the two mixing grooves on the side to create a passage for the resin and glass fibers, and the inner surface of the cylinder of the injection molding machine where the screw operates and the outer diameter of the mixing part were removed. This is the structure of the mixing section that forms a gap S with the wall surface.

この様な構造のミキシング部においては、溶融
した樹脂材料と充填材であるカツトされたガラス
繊維が、2段のミキシング溝のホツパー側より流
入し、溝の中で回転,混合しながら前進し、前記
スキマS1を経て、1段のミキシング溝に流入し、
この1段のミキシング溝内を回転,混合しながら
前進し、次にスキマS2を経て2段のミキシング溝
の一方に流入し、更に回転、混合を繰返して、ノ
ズル側へ送られるものである。この場合、2段の
ミキシング溝から1段のミキシング溝へ、1段の
ミキシング溝から2段のミキシング溝へ移送さ
れ、S1,S2……のスキマを通過するたびに、ガラ
ス繊維は強い剪断力を受け、ガラス繊維はこの剪
断力により集束された束をほぐす作用を受け、更
に前記各ミキシング溝の中で樹脂及びガラス繊維
は、スクリユーの回転によりスキマを2回以上通
過することにより、ガラス繊維の集束はまつたく
無くなり、極めて効果的な分散が出来るものであ
る。
In a mixing section with such a structure, molten resin material and cut glass fibers as a filler enter from the hopper side of the two-stage mixing groove, move forward while rotating and mixing in the groove, After passing through the gap S1 , it flows into the first stage of mixing groove,
It moves forward while rotating and mixing inside this one-stage mixing groove, then flows into one of the two-stage mixing grooves through gap S 2 , repeats further rotation and mixing, and is sent to the nozzle side. . In this case, the glass fibers are transferred from the second mixing groove to the first mixing groove, and from the first mixing groove to the second mixing groove, and each time they pass through the gaps S 1 , S 2 ..., the glass fibers become stronger. The glass fibers are subjected to shearing force, and the shearing force acts to loosen the bundle, and the resin and glass fibers in each of the mixing grooves pass through the gap two or more times due to the rotation of the screw. The glass fibers are no longer bunched together and can be dispersed very effectively.

この結果本装置によれば、 (1) 樹脂とガラス繊維をペレツト製造工程を経ず
に直接FRPを製造することが出来、 (2) ガラス繊維の集束が無くなり、均一に分散が
可能となり、 (3) FRPの引張り強度も10〜20%向上し、 (4) 工程短縮による大巾なコストダウンを計るこ
とが出来る。
As a result, with this device, (1) it is possible to directly manufacture FRP from resin and glass fibers without going through the pellet manufacturing process, (2) the glass fibers are no longer bundled and can be uniformly dispersed, and ( 3) The tensile strength of FRP is also improved by 10 to 20%, and (4) significant cost reductions can be achieved by shortening the process.

等の効果がある。There are other effects.

以下具体的に実施例について第4図〜第6図に
より説明する。
Examples will be specifically described below with reference to FIGS. 4 to 6.

1はスクリユー、2はフライト、3はミキシン
グ部、3aはその外径、3bは3aの外径を一部
削除した(斜線で示す)外径である。4は1段の
ミキシング溝で、ミキシング部の長さよりやや短
かく溝の両端4a,4bは行き止まりの形状であ
り、1段のミキシング溝に平行して2段のミキシ
ング溝5及び6が設けられ、溝の端部はホツパー
側との連通部5aと行き止まり部5bよりなり、
2段のミキシング溝の他方の溝6も行き止まり部
6bとノズル側への連通部6aよりなつている。
1 is a screw, 2 is a flight, 3 is a mixing section, 3a is its outer diameter, and 3b is an outer diameter obtained by removing a part of the outer diameter of 3a (indicated by diagonal lines). Reference numeral 4 denotes a one-stage mixing groove, which is slightly shorter than the length of the mixing section, and both ends 4a and 4b of the groove have a dead-end shape, and two-stage mixing grooves 5 and 6 are provided in parallel to the first-stage mixing groove. , the end of the groove consists of a communicating part 5a with the hopper side and a dead end part 5b,
The other groove 6 of the two-stage mixing groove also consists of a dead end portion 6b and a communicating portion 6a to the nozzle side.

スクリユー1は第4図ロに於て時計方向に回転
する、この時ホツパー側の2段のミキシング溝の
スクリユーの反回転方向側に隣接する1段のミキ
シング溝との間、およびこの1段のミキシング溝
とスクリユーの反回転方向側に隣接するノズル側
の2段のミキシング溝との間に前記材料通過のた
めの一部削除したスキマがある。7はシリンダ
ー、7aはシリンダーの内面で、7aと3bとの
スキマS≒0.5mmであり、7aと3aとのスキマ
は0.1mm以内である。
The screw 1 rotates clockwise in FIG. There is a partially removed gap for the material to pass between the mixing groove and the two-stage mixing groove on the nozzle side adjacent to the opposite rotation direction of the screw. 7 is a cylinder, 7a is the inner surface of the cylinder, the gap S between 7a and 3b is approximately 0.5 mm, and the gap between 7a and 3a is within 0.1 mm.

以上の構成において、ホツパー側より投入され
た樹脂とカツトされたガラス繊維は、2段のミキ
シング溝、スキマS11段のミキシング溝、スキマ
S2、2段のミキシング溝、ノズル側へ流出し、A
→B→C→D→E→F→Gの方向へ移送され、ス
キマS1及びS2によりガラス繊維の束は剪断され、
各溝内での材料の回転移動により混合,混練が繰
返えされ、ガラス繊維の均一な分散が行なわれる
ものである。
In the above configuration, the resin fed from the hopper side and the cut glass fibers are distributed between two mixing grooves, a gap S 1, a first mixing groove, and a gap S1 .
S 2 , two-stage mixing groove, flowing out to the nozzle side, A
→B→C→D→E→F→G, the glass fiber bundle is sheared by skimmers S 1 and S 2 ,
Mixing and kneading are repeated by rotating the materials within each groove, and the glass fibers are uniformly dispersed.

第6図は本発明により射出成形された製品9の
外観図で、まつたくガラス繊維の集束がなく、テ
ストピース10を取つて約30倍に拡大した実物を
写真2に示す。この写真より、ガラス繊維が整然
と均一に一本一本分散している状態が良く判る。
この様に、均一に分散した場合の強度、つまり、
ポリプロピレン樹脂にガラス繊維20%を混入した
場合の引張り強度は460Kg/cm2であり、従来品よ
り10〜15%の強度がアツプするものである。
FIG. 6 is an external view of a product 9 injection-molded according to the present invention, in which the glass fibers are not bunched together, and the actual product is shown in Photo 2, which is enlarged approximately 30 times by taking a test piece 10. This photo clearly shows that the glass fibers are neatly and evenly distributed one by one.
In this way, the strength when uniformly dispersed, that is,
The tensile strength when 20% glass fiber is mixed into polypropylene resin is 460 kg/cm 2 , which is 10 to 15% higher than conventional products.

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

第1図は従来のスクリユーの外観図、第2図は
その拡大を示すもので、イはミキシング部の側面
図、ロはイの〜断面図、第3図は従来例によ
る成形品を示すもので、イは斜視図、ロはその一
部の拡大図、ハはさらに拡大した説明図、第4図
は本発明による実施例を示すもので、イは側面
図、ロはイの〜断面図、第5図はミキシング
部の断面を示すもので、イは1段のミキシング溝
の断面図、ロは2段のミキシング溝の断面図、そ
して第6図は本実施例にもとづく成形品の斜視図
である。 1……スクリユー、3……ミキシング部、4…
…1段のミキシング溝、5,6……2段のミキシ
ング溝、S,S1,S2……スキマ。
Figure 1 is an external view of a conventional screw, Figure 2 is an enlarged view of it, A is a side view of the mixing section, B is a sectional view of A, and Figure 3 is a molded product according to the conventional example. A is a perspective view, B is a partially enlarged view, C is a further enlarged explanatory view, and FIG. 4 shows an embodiment of the present invention, A is a side view, and B is a sectional view of A. , Fig. 5 shows a cross-section of the mixing part, A is a cross-sectional view of the first-stage mixing groove, B is a cross-sectional view of the second-stage mixing groove, and Fig. 6 is a perspective view of the molded product based on this example. It is a diagram. 1...screw, 3...mixing department, 4...
...1st stage mixing groove, 5, 6...2nd stage mixing groove, S, S 1 , S 2 ... gap.

Claims (1)

【特許請求の範囲】[Claims] 1 射出成形機の射出部を構成するシリンダーと
スクリユーのうち、該スクリユーに複数のミキシ
ング溝を持つたミキシング部を設け、前記ミキシ
ング溝のうち、ほぼミキシング部の長さに相当す
る1段のミキシング溝と、前記1段のミキシング
溝に平行に2段のミキシング溝を直列的に配置
し、ホツパー側の2段のミキシング溝のスクリユ
ー反回転方向側に隣接する1段のミキシング溝と
の間に射出成形材料が流動するスキマを設け、か
つ前記1段のミキシング溝のスクリユー反回転方
向側に隣接するノズル側ミキシング溝との間に射
出成形材料が流動するスキマを設けたことを特徴
とする射出成形機のスクリユー。
1 Of the cylinder and screw that constitute the injection section of an injection molding machine, the screw is provided with a mixing section having a plurality of mixing grooves, and among the mixing grooves, one stage of mixing approximately corresponds to the length of the mixing section. A groove and two mixing grooves arranged in series parallel to the first mixing groove, and between the first mixing groove adjacent to the two mixing grooves on the hopper side in the direction opposite to the screw rotation direction. An injection method characterized in that a gap is provided in which the injection molding material flows, and a gap in which the injection molding material flows is provided between the first mixing groove and the adjacent nozzle-side mixing groove on the opposite side of the screw rotation direction. Molding machine screw.
JP58157515A 1983-08-29 1983-08-29 Screw of injection molding machine Granted JPS6049907A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58157515A JPS6049907A (en) 1983-08-29 1983-08-29 Screw of injection molding machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58157515A JPS6049907A (en) 1983-08-29 1983-08-29 Screw of injection molding machine

Publications (2)

Publication Number Publication Date
JPS6049907A JPS6049907A (en) 1985-03-19
JPS6356048B2 true JPS6356048B2 (en) 1988-11-07

Family

ID=15651359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58157515A Granted JPS6049907A (en) 1983-08-29 1983-08-29 Screw of injection molding machine

Country Status (1)

Country Link
JP (1) JPS6049907A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998035813A1 (en) * 1997-02-17 1998-08-20 Mitsubishi Heavy Industries, Ltd. Plasticizing screw

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0384126U (en) * 1989-12-18 1991-08-27
US7021816B2 (en) * 2002-04-08 2006-04-04 Robert Malloy Plasticating screw
JP6759707B2 (en) * 2016-05-20 2020-09-23 三菱ケミカル株式会社 Screws, extruders and mixing devices

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998035813A1 (en) * 1997-02-17 1998-08-20 Mitsubishi Heavy Industries, Ltd. Plasticizing screw

Also Published As

Publication number Publication date
JPS6049907A (en) 1985-03-19

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