JPH081070Y2 - Resin extrusion equipment - Google Patents
Resin extrusion equipmentInfo
- Publication number
- JPH081070Y2 JPH081070Y2 JP1990064788U JP6478890U JPH081070Y2 JP H081070 Y2 JPH081070 Y2 JP H081070Y2 JP 1990064788 U JP1990064788 U JP 1990064788U JP 6478890 U JP6478890 U JP 6478890U JP H081070 Y2 JPH081070 Y2 JP H081070Y2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- extruder
- screw
- additive
- screw thread
- 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 - Lifetime
Links
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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/53—Screws having a varying channel depth, e.g. varying the diameter of the longitudinal screw trunk
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/375—Plasticisers, homogenisers or feeders comprising two or more stages
- B29C48/385—Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in separate barrels
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/52—Screws with an outer diameter varying along the longitudinal axis, e.g. for obtaining different thread clearance
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
本考案は、架橋剤などの添加剤を含むゴム、プラスチ
ックなどの樹脂を押し出しするにおいて有用な樹脂押出
装置に関するものである。The present invention relates to a resin extruding apparatus useful for extruding a resin such as rubber or plastic containing an additive such as a crosslinking agent.
従来、2段押出方式を取り、例えば第5図に示したよ
うに、ポリエチレンなどのプラスチック樹脂に架橋剤や
老化防止剤などの添加剤を混合する場合、第1の押出機
1にフィルター部2、冷却部3などを介して接続部をな
すクロスヘッド4を接続し、この第1の押出機1から供
給されるプラスチック樹脂中に、上記クロスヘッド4に
接続された添加剤圧入装置5から所望量の添加剤を圧
入、混合し、この混合されたプラスチック樹脂を、第2
の押出機6に導き、この第2の押出機6のヘッド部7か
ら、例えば電線導体8に絶縁体9としてプラスチック樹
脂を押出被覆する方法が、既に提案れている。Conventionally, a two-stage extrusion method is adopted, and for example, as shown in FIG. 5, when a plastic resin such as polyethylene is mixed with an additive such as a cross-linking agent or an antioxidant, the first extruder 1 is provided with a filter unit 2 , A crosshead 4 forming a connecting part is connected via a cooling part 3 or the like, and a plastic resin supplied from the first extruder 1 is supplied with the additive press-fitting device 5 connected to the crosshead 4 as desired. A quantity of additive is pressed in and mixed, and the mixed plastic resin is mixed with the second
A method has been already proposed in which, for example, the electric wire conductor 8 is extruded and covered with a plastic resin as an insulator 9 from the head portion 7 of the second extruder 6 by introducing the plastic resin into the extruder 6.
このような樹脂押出装置系において、第2の押出機6
部分では、例えば6図に示したように添加剤圧入装置5
から圧入された架橋剤などの10は樹脂11中に囲まれる形
で供給され、混練されるわけであるが、このとき、押出
機シリンダ12の樹脂供給口側から直ちに強力な攪拌力
(混練力)により混練すると、当該部分でスコーチ(早
期架橋)が起こるなどの問題があった。 つまり、樹脂供給部において、スクリュー山部とシリ
ンダー内壁との間で樹脂の切断が起こり、液状の架橋剤
10が漏れ、架橋剤10が滞留し、分散されないため、架橋
が局部的に促進されるからと、考えられる。 そこで、第6図のように混練用のスクリュ13の樹脂供
給口部分のネジ山部14aの高さを、例えば1.5ピッチ分ほ
ど、他の部分のネジ山部14bより低くして、なるべく樹
脂切れや樹脂の切断を防止しようとするものである。と
ころが、今度は新たな問題として、上記高いネジ山部14
bの始まる基端から少々先端方向に進んだ部分(領域
A)でスコーチが発生することが判った。 この理由としては、次のことが考えられる。 このスクリュ13の場合、低いネジ山部14a部分では、
シリンダ12内壁面との間に若干の隙間があるため、樹脂
11は山部を越えて進行していくが、高いネジ山部14b部
分では、シリンダ12内壁面との間に隙間が殆どないた
め、樹脂11の進行速度が遅くなる。一方、このスクリュ
13では、山部の高さが変化する部分において、液状の架
橋剤10が樹脂11中にある程度分散しているものの、まだ
液状塊となっている部分があるため、樹脂11の流れが遅
くなる部分で通常の強力な攪拌、混練が行われると、こ
の液状塊の架橋剤10がスクリュー表面に接して滑りを起
こし、滞留することにより、当該部分でスコーチが発生
するようになるから、と思われる。 本考案は、このような従来の実情に鑑みて、架橋剤な
どの添加剤がスクリュの全長にわたて良好に分散混練さ
れる形状のスクリュとした押出機を用いた樹脂押出装置
を提供せんとするものである。In such a resin extruder system, the second extruder 6
In the part, for example, as shown in FIG.
Cross-linking agent 10 pressed in from is supplied in a form surrounded by resin 11 and kneaded.At this time, a strong stirring force (kneading force) is immediately applied from the resin supply port side of extruder cylinder 12. However, there was a problem that scorch (premature cross-linking) occurred in the relevant part when kneading was performed with the above method. That is, in the resin supply part, the resin is cut between the screw crest part and the cylinder inner wall, and the liquid crosslinking agent
It is considered that 10 leaks and the crosslinking agent 10 stays and is not dispersed, so that the crosslinking is locally promoted. Therefore, as shown in FIG. 6, the height of the screw thread portion 14a of the resin supply port portion of the kneading screw 13 is made lower than the screw thread portion 14b of the other portion by, for example, about 1.5 pitch, so that the resin breaks as much as possible. It is intended to prevent the resin from being cut. However, this time, as a new problem, the above-mentioned high thread portion 14
It was found that scorch is generated in a portion (region A) slightly advanced from the base end where b starts to the tip end direction. The reason for this is considered as follows. In the case of this screw 13, at the low thread portion 14a,
Since there is a slight gap between the inner wall surface of the cylinder 12 and
Although the resin 11 advances beyond the ridges, there is almost no gap between the high screw ridges 14b and the inner wall surface of the cylinder 12, so the resin 11 slows down. On the other hand, this screw
In 13, the liquid cross-linking agent 10 is dispersed in the resin 11 to some extent in the portion where the height of the mountain portion changes, but there is still a liquid lump, so the flow of the resin 11 slows down. When strong stirring and kneading are usually performed in the part, the cross-linking agent 10 in the liquid mass causes sliding on the screw surface and stays, so that scorch is generated in the part, Be done. In view of such conventional circumstances, the present invention provides a resin extruder using an extruder having a screw shape in which an additive such as a cross-linking agent is well dispersed and kneaded over the entire length of the screw. To do.
かゝる本考案の樹脂押出装置は、第1の押出機で架橋
剤などの添加剤を含まないゴム、プラスチックなどの樹
脂を押し出し、第2の押出機との接続部で前記樹脂に架
橋剤などの添加剤を圧入、混合し、これを第2の押出機
で混練して押し出す樹脂押出装置において、前記第2の
押出機のシリンダ中に回転自在に挿入され、螺旋状のネ
ジ山を有するスクリュのほぼ中央部にミキシング部を設
けると共に、当該ミキシング部から樹脂供給口側にかけ
てのネジ山部の高さを当該ミキシング部からスクリュの
先端側にかけてのネジ山部に比べて低くしたものであ
る。The resin extruder of the present invention is such that the first extruder extrudes a resin such as rubber or plastic that does not contain an additive such as a cross-linking agent, and the cross-linking agent is added to the resin at the connecting portion with the second extruder. In a resin extrusion apparatus in which additives such as the above are pressed and mixed, and the mixture is kneaded and extruded by a second extruder, the resin extruder is rotatably inserted into the cylinder of the second extruder and has a spiral thread. A mixing portion is provided in the substantially central portion of the screw, and the height of the screw thread portion from the mixing portion to the resin supply port side is lower than that of the screw thread portion from the mixing portion to the tip side of the screw. .
本考案の樹脂押出装置では、スクリュのほぼ中央部に
設けたミキシング部から樹脂供給口側にかけての相当長
い領域で、ネジ山部の高さを低くし、かつその終端が直
ちにミキシング部となるようにしてあるため、良好な添
加剤の分散混練が行われ、スコーチの発生などが効果的
に抑えられる。In the resin extrusion device of the present invention, the height of the screw thread portion is lowered in a considerably long region from the mixing portion provided in the substantially central portion of the screw to the resin supply port side, and the terminal end becomes the mixing portion immediately. Therefore, good additive dispersion kneading is performed, and scorch generation and the like can be effectively suppressed.
第1図は本考案に係る樹脂押出装置に用いれる第2の
押出機のスクリュの一実施例を示したものである。 この第2の押出機6のスクリュ13Aでは、シリンダ12
の樹脂供給口12a側からそのほぼ中央部のミキシング部1
5までの間のネジ山部14aの高さを、当該ミキシング部15
からスクリュ13Aの先端側にかけてのネジ山部14bに比べ
て、低くし、シリンダ内壁面との間に少々の隙間を設け
てある。 一方、このミキシング部15より先端方向のネジ山部14
bの高さは通常の高さにしてある。なお、本樹脂押出装
置において、他の構成部分は上述した第5図の樹脂押出
装置の場合と同様である。 上記ミキシング部15は、特に限定されないが、例えば
第2図〜第4図に示したようにネジ形成部より少々径を
太くした太径部15aの中央の周方向に環状溝15bを設ける
と共に、左右の太径部15aの外周の軸方向には、刻設位
置を少々ずらした多数の独立した小溝15c・・・が設け
てなる。 したがって、このスクリュ13Aの場合、シリンダ12の
樹脂供給口12aから供給された樹脂11およびこの樹脂11
中に含まれた架橋剤などの液状の添加剤10は、この樹脂
供給口12aからミキシング部15にかけて、当該領域のス
クリュ13Aのネジ山部14aの高さが低いため、比較的弱い
攪拌力で攪拌され、かつ樹脂11がネジ山部14aを越えて
流れるため、速い流速でミキシング部15に運ばれる。つ
まり、この間では、添加剤10の分散が不十分ながらも、
局部的に偏在することなく、ほぼ均一に行われ、スコー
チの発生は効果的に防止される。 そして、ミキシング部15に達すると、この部分の各溝
15b、15c・・・の作用により、樹脂11と添加剤10との攪
拌はより極め細かく行われ、さらに、このミキシング部
15より先端方向の通常の高さのネジ山部14bでは、より
強力な攪拌、混練が行われるため、添加剤10はほぼ完全
に樹脂11中に分散されるようになる。 この完全な添加剤10の分散が行われた樹脂11が、この
第2の押出機6により、電線導体など絶縁体などとして
押出被覆される。 なお、上記実施例では、第2の押出機6への適用の場
合であったが、本考案は、これに限定されず、単独の押
出機、または架橋剤以外の添加剤入れ樹脂の押出機にも
応用できることができる。FIG. 1 shows one embodiment of the screw of the second extruder used in the resin extruder according to the present invention. In the screw 13A of the second extruder 6, the cylinder 12
From the resin supply port 12a side of the
The height of the screw thread portion 14a up to 5 is set to the mixing portion 15
To the tip side of the screw 13A, the screw thread portion 14b is made lower than the thread portion 14b, and a small gap is provided between the screw thread portion 14A and the inner wall surface of the cylinder. On the other hand, the screw thread portion 14 in the tip direction from the mixing portion 15
The height of b is the normal height. The other components of the resin extrusion device are the same as those of the resin extrusion device of FIG. 5 described above. The mixing portion 15 is not particularly limited, but for example, as shown in FIGS. 2 to 4, while providing an annular groove 15b in the central circumferential direction of a large diameter portion 15a slightly thicker than the thread forming portion, In the axial direction of the outer circumference of the left and right large-diameter portions 15a, a large number of independent small grooves 15c ... With slightly deviated engraving positions are provided. Therefore, in the case of this screw 13A, the resin 11 supplied from the resin supply port 12a of the cylinder 12 and this resin 11
The liquid additive 10 such as a cross-linking agent contained in the resin supply port 12a to the mixing section 15 has a relatively low stirring force because the screw thread 14a of the screw 13A in the area is low in height. Since the resin 11 is agitated and flows over the screw thread portion 14a, it is conveyed to the mixing portion 15 at a high flow rate. That is, during this period, although the dispersion of the additive 10 is insufficient,
It is carried out almost uniformly without being locally unevenly distributed, and the occurrence of scorch is effectively prevented. Then, when it reaches the mixing section 15, each groove in this section
Due to the action of 15b, 15c ..., the resin 11 and the additive 10 are agitated more finely.
In the screw thread portion 14b having a normal height from the tip end 15 side, stronger stirring and kneading are performed, so that the additive 10 is almost completely dispersed in the resin 11. The resin 11 in which the additive 10 is completely dispersed is extrusion-coated by the second extruder 6 as an insulator such as a wire conductor. In addition, in the above-mentioned embodiment, the case was applied to the second extruder 6, but the present invention is not limited to this, and a single extruder or an extruder containing an additive-containing resin other than the crosslinking agent is used. It can also be applied to.
このように本考案の樹脂押出装置では、スクリュのほ
ぼ中央部に設けたスクリュのミキシング部から樹脂供給
口側にかけて、相当長い領域でネジ山部の高さを低く
し、かつその終端が直ちにミキシング部となるようにし
てあるため、この間、攪拌力が適度に抑えられ、かつま
た山部を越えた樹脂の流れがスムーズに行われるので、
樹脂切れや樹脂の切断などによる添加剤漏れ、流動速度
の低下が効果的に防止され、良好な添加剤の分散混練が
行われ、スコーチの発生などが効果的に抑えられる。As described above, in the resin extrusion device of the present invention, the height of the screw thread portion is lowered in a considerably long region from the mixing portion of the screw provided in the substantially central portion of the screw to the resin supply port side, and the end thereof is immediately mixed. Since it is made into a part, the stirring force is appropriately suppressed during this time, and the resin flows smoothly over the mountain part,
Additive leakage due to resin breakage or resin breakage and reduction in flow rate are effectively prevented, good additive dispersion kneading is performed, and scorch is effectively suppressed.
第1図は本考案に係る樹脂押出装置における第2の押出
機の一実施例を示した部分縦断面図、第2図は第1図の
押出機のスクリュのミキシング部の縦断面図、第3図は
第2図のミキシング部の平面図、第4図は第3図のIV-I
V線断面図、第5図は一般的な2段押出方式による樹脂
押出装置の概略説明図、第6図は第5図の樹脂押出装置
における従来の押出機を示した縦断面図である。 図中、 1……第1の押出機、4……クロスヘッド、6……第2
の押出機、10……添加剤、11……樹脂、12……シリン
ダ、12a……樹脂供給口、13A……スクリュ、14a……低
いネジ山部、14b……高いネジ山部、15……ミキシング
部、FIG. 1 is a partial vertical sectional view showing an embodiment of a second extruder in a resin extruder according to the present invention, and FIG. 2 is a vertical sectional view of a mixing portion of a screw of the extruder shown in FIG. FIG. 3 is a plan view of the mixing section of FIG. 2, and FIG. 4 is IV-I of FIG.
FIG. 5 is a cross-sectional view taken along the line V, FIG. 5 is a schematic explanatory view of a resin extrusion apparatus using a general two-stage extrusion method, and FIG. 6 is a vertical sectional view showing a conventional extruder in the resin extrusion apparatus of FIG. In the figure, 1 ... first extruder, 4 ... crosshead, 6 ... second
Extruder, 10 ... Additive, 11 ... Resin, 12 ... Cylinder, 12a ... Resin supply port, 13A ... Screw, 14a ... Low thread part, 14b ... High thread part, 15 ... … The mixing department,
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭58−108609(JP,A) 特開 昭60−21228(JP,A) 実開 平2−34226(JP,U) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-58-108609 (JP, A) JP-A-60-21228 (JP, A) Jitsukaihei 2-34226 (JP, U)
Claims (1)
ないゴム、プラスチックなどの樹脂を押し出し、第2の
押出機との接続部で前記樹脂に架橋剤などの添加剤を圧
入、混合し、これを第2の押出機で混練して押し出す樹
脂押出装置において、前記第2の押出機のシリンダ中に
回転自在に挿入され、螺旋状のネジ山を有するスクリュ
のほぼ中央部にミキシング部を設けると共に、当該ミキ
シング部から樹脂供給口側にかけてのネジ山部の高さを
当該ミキシング部からスクリュの先端側にかけてのネジ
山部に比べて低くしたことを特徴とする樹脂押出装置。1. A first extruder extrudes a resin such as rubber or plastic containing no additive such as a cross-linking agent, and an additive such as a cross-linking agent is pressed into the resin at a connecting portion with a second extruder. , In a resin extruder for kneading and extruding the mixture with a second extruder, the screw is rotatably inserted into the cylinder of the second extruder and has a screw thread having a spiral shape at substantially the center. A resin extruding device, wherein a mixing portion is provided and the height of a screw thread portion from the mixing portion to the resin supply port side is made lower than that of a screw thread portion from the mixing portion to the tip end side of the screw.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1990064788U JPH081070Y2 (en) | 1990-06-19 | 1990-06-19 | Resin extrusion equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1990064788U JPH081070Y2 (en) | 1990-06-19 | 1990-06-19 | Resin extrusion equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0424327U JPH0424327U (en) | 1992-02-27 |
JPH081070Y2 true JPH081070Y2 (en) | 1996-01-17 |
Family
ID=31596044
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1990064788U Expired - Lifetime JPH081070Y2 (en) | 1990-06-19 | 1990-06-19 | Resin extrusion equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH081070Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4034124B2 (en) * | 2002-06-05 | 2008-01-16 | 株式会社ブリヂストン | Extruder screw and method for producing the same |
FR3125354A1 (en) * | 2021-07-19 | 2023-01-20 | Nexans | Method for manufacturing an electric cable by extruding a composition based on a propylene polymer and a dielectric liquid with a barrier screw comprising a mixing section |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58108609A (en) * | 1981-12-22 | 1983-06-28 | 古河電気工業株式会社 | Method of producing crosslinked rubber or plastic cable |
JPS6021228A (en) * | 1983-07-15 | 1985-02-02 | Showa Denko Kk | Extruding machine for foamy extrusion forming |
JPH0234226U (en) * | 1988-08-26 | 1990-03-05 |
-
1990
- 1990-06-19 JP JP1990064788U patent/JPH081070Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0424327U (en) | 1992-02-27 |
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