JPS6116828A - Screw type extruding apparatus for thermosetting resin - Google Patents

Screw type extruding apparatus for thermosetting resin

Info

Publication number
JPS6116828A
JPS6116828A JP59136580A JP13658084A JPS6116828A JP S6116828 A JPS6116828 A JP S6116828A JP 59136580 A JP59136580 A JP 59136580A JP 13658084 A JP13658084 A JP 13658084A JP S6116828 A JPS6116828 A JP S6116828A
Authority
JP
Japan
Prior art keywords
screw
cylinder
section
extrusion
resin
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
JP59136580A
Other languages
Japanese (ja)
Inventor
Yoshiaki Fukuda
義明 福田
Takeshi Miyasaka
宮坂 猛
Shuhei Imon
修平 井門
Hideo Kawashima
秀雄 川島
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP59136580A priority Critical patent/JPS6116828A/en
Publication of JPS6116828A publication Critical patent/JPS6116828A/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
    • 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
    • B29C48/30Extrusion nozzles or dies
    • B29C48/32Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B29C48/33Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles with parts rotatable relative to each other
    • 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
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • 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
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • 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
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • 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
    • B29K2101/00Use of unspecified macromolecular compounds as moulding material
    • B29K2101/10Thermosetting resins
    • 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
    • B29K2301/00Use of unspecified macromolecular compounds as reinforcement
    • B29K2301/10Thermosetting resins

Landscapes

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

Abstract

PURPOSE:To make an extruded item obtainable continuously and stably with good productivity, by facilitating a curing reaction in a clearance formed between a cylinder section and smooth section at the forward end of a screw, and shaping a material to such a degree that enables it to hold the shape by itself after the extrusion. CONSTITUTION:A thermosetting resin material fed from a hopper 1 is heated and melted in a cylinder 2 by a heater 3, is moved helically from the forward end of the flight of a screw 4 to a smooth section 5 and is compressed and fused due to the gradually decreased clearance between the cylinder and the screw flight that causes friction to the material. Then the fused resin is shaped in the course of movement through the screw smooth section to such a degree that enables it to hold the shape by itself after the extrusion. In this case, a back pressure applying apparatus 6 attached to the forward end of the cylinder gives a suitable back pressure to the resin enough to compress and fuse it. Thus, a shaped continuous pipelike item 7 that has a thick wall can be obtained stably with good productivity.

Description

【発明の詳細な説明】 産業上の利用分野: 本発明は熱硬化性樹脂の新規な押出成形装置に関する。[Detailed description of the invention] Industrial applications: The present invention relates to a novel extrusion molding apparatus for thermosetting resin.

従来の技術とその問題点: 熱硬化性樹脂の成形方法としては圧縮成形法、トランス
ファー成形法、射出成形法および押出成形法が知られ、
夫々の成形方法に適合した装置が用いられている。
Conventional techniques and their problems: Compression molding, transfer molding, injection molding, and extrusion molding are known as methods for molding thermosetting resins.
Equipment suitable for each molding method is used.

これらの熱硬化性樹脂の成形方法のうち、押出成形装置
としてはプランジャー押出装置が一般的であシ(例えば
特開昭48−83155公報、プラスチックy、 Vo
t25、A3、P47 )、丸棒やパイプなどの単純な
形状の長尺押出製品が生産されている。
Among these thermosetting resin molding methods, a plunger extrusion device is generally used as an extrusion molding device (for example, Japanese Patent Application Laid-Open No. 48-83155, Plastics Y, Vo.
t25, A3, P47), long extruded products with simple shapes such as round bars and pipes are produced.

しかし乍らプランジャー押出成形装置に於ては、金型部
における押出圧が高く、シかも間欠押出であるため均一
な成形品を得ることが困難であり生産性も低い。
However, in the plunger extrusion molding apparatus, the extrusion pressure in the mold section is high and the extrusion is performed intermittently, so it is difficult to obtain uniform molded products and the productivity is low.

か\る事情から、所謂スクリュー型押出成形装置を用い
る成形法が例えば特開昭54−23661公報により開
示されている。これは押出機内で混線溶融された熱硬化
性樹脂を、アダプターを通じて金型内へ導ひき最終形状
に賦形する成形装置である。
Under these circumstances, a molding method using a so-called screw type extrusion molding apparatus has been disclosed, for example, in Japanese Patent Application Laid-Open No. 54-23661. This is a molding device that guides the cross-melted thermosetting resin in the extruder into the mold through an adapter and shapes it into the final shape.

しかし乍らこの様な形成装置では、樹脂流路が複雑に変
化し、僅かな温度や圧力の差で熱硬化反応が急激に進行
したり、滞留の発生によって局部的に硬化反応が進行し
たりすることにより、連続して安定な成形を行うことが
困難であった。
However, in such a forming device, the resin flow path changes in a complicated manner, and the thermosetting reaction may proceed rapidly due to a slight difference in temperature or pressure, or the curing reaction may proceed locally due to the occurrence of stagnation. This made it difficult to perform continuous and stable molding.

またこの種の装置ではマンドレルを支持するスパイダ一
部の存在によるスパイダーマーク或竺それによるウェル
ド部分に起因する品質上の障害を回避することはできな
かった。
Furthermore, with this type of device, it has not been possible to avoid quality problems caused by spider marks or welds caused by the presence of a part of the spider supporting the mandrel.

本発明者らは、建築分野、電気、電子分野等において市
場の要求の強い難燃性、耐熱性等に優れた熱硬化性樹脂
の成形品の成形方法、特に上記した問題点の解決につい
て種々検討を重ねた結果、スクリューの平滑部に於て押
−出抜自己形状を保持できる程度にまで賦形することに
より連続的に且つ安定でしかも生産性良く目的を達成し
得ることを見出して先に新規な装置を提供した。(特願
昭58−51526 、特願昭58−104891 )
即ち、その装置は、供給部、圧縮部、計量部および平滑
部から成るスクリュー、該供給部、圧縮部および計量部
に対応する熱供給機能を有するシリンダー部分、および
該計量部の最終スクリュー径に等しいかまたは異なる径
を有する該平滑部に対応する熱供給機能を有するシリン
ダー部分より成シ、該平滑部とそれに対応するシリンダ
ー部分とによって形成される間隙部において硬化反応を
促進させ押出後自己形状を保持できる程度にまで賦形す
る様にした熱硬化性樹脂のスクリュー型押出成形装置で
ある。
The present inventors have developed a method for molding thermosetting resin molded products with excellent flame retardancy, heat resistance, etc., which are in strong market demand in the fields of architecture, electricity, electronics, etc., and in particular, various methods for solving the above-mentioned problems. As a result of repeated studies, we discovered that the purpose could be achieved continuously, stably, and with good productivity by shaping the smooth part of the screw to the extent that it could retain its extruded and extruded shape. provided new equipment to (Patent application No. 58-51526, Patent application No. 104891-1983)
That is, the device consists of a screw consisting of a supply section, a compression section, a metering section and a smooth section, a cylinder section having a heat supply function corresponding to the supply section, compression section and metering section, and a final screw diameter of the metering section. It is composed of a cylinder part having a heat supply function corresponding to the smooth part having the same or different diameter, and promotes the curing reaction in the gap formed by the smooth part and the corresponding cylinder part, and has a self-shaping shape after extrusion. This is a screw-type extrusion molding device for thermosetting resin that can be shaped to the extent that it can hold.

しかし乍ら、本発明者らの知見によれば、上述の装置を
用いて肉厚のパイプを製造する場合は、肉厚が増大する
と材料によっては充分な背圧が得られず、平滑部におけ
る樹脂の圧縮圧着が不充分となってクラックが入りやす
くなったシ、表面の平滑性が失なわれ、従って光沢が劣
るなどの問題が派生した。これらの問題に対しては、ス
クリューの圧縮比や平滑部の長さを変えることにより成
程度は解決可能であるが、その場合肉厚や材料特性によ
り、それらに適したスクリューを各々用意する必要があ
る。
However, according to the findings of the present inventors, when manufacturing thick-walled pipes using the above-mentioned apparatus, as the wall thickness increases, depending on the material, sufficient back pressure may not be obtained, and Problems such as insufficient compression and bonding of the resin resulted in easy cracking, and the surface smoothness was lost, resulting in poor gloss. These problems can be solved by changing the compression ratio and length of the smooth part of the screw, but in that case, it is necessary to prepare screws suitable for each depending on the wall thickness and material properties. There is.

問題点を解決する手段: 本発明者らは、材料特性が変っても肉厚が同じであるか
ぎシ同一スクリユーの使用において上述の問題が起きな
い手段を種々検討した結果、前記した装置のシリンダー
先端に背圧付与装置を装着することにより、良好な肉厚
のパイプが得られることを見出し本発明に到達した。
Means for solving the problem: The inventors of the present invention have investigated various means that do not cause the above-mentioned problem when using screws with the same wall thickness even when the material properties are changed. The present invention was achieved by discovering that a pipe with good wall thickness can be obtained by attaching a back pressure applying device to the tip.

すなわち本発明は、供給部、圧縮部、計量部および平滑
部から成るスクリュー、該供給部、圧縮部および計量部
に対応する熱制御機構を有するシリンダー部分、該計量
部の最終スクリュー径に等しいか又は異なる径を有する
該平滑部に対応する熱供給機能を有するシリンダー部分
、およびシリンダー先端に装着されたを圧付与装置より
成り、該平滑部とそれに対応するシリンダー部分とによ
って形成される間隙部において硬化反応を促進させ押出
後自己形状を保持できる程度にまで賦形する様にした熱
硬化性樹脂のスクリュー型押出成形装置である。
That is, the present invention provides a screw consisting of a supply section, a compression section, a metering section, and a smooth section, a cylinder section having a thermal control mechanism corresponding to the supply section, the compression section, and the metering section, and a screw having a diameter equal to the final screw diameter of the metering section. or a cylinder part having a heat supply function corresponding to the smooth part having a different diameter, and a pressure applying device attached to the tip of the cylinder, in the gap formed by the smooth part and the corresponding cylinder part. This is a screw-type extrusion molding device for thermosetting resin that accelerates the curing reaction and shapes the resin to the extent that it can maintain its own shape after extrusion.

本発明の特徴は先端に平滑部を有するスクリューを使用
して熱硬化性樹脂を賦形するにあたって、シリンダー先
端に背圧付与装置を装着することにより、押出成形時の
背圧を調整することにある。
The feature of the present invention is that when shaping thermosetting resin using a screw with a smooth portion at the tip, the back pressure during extrusion molding can be adjusted by attaching a back pressure applying device to the tip of the cylinder. be.

本発明を図によって説明すれば第1図は本発明の方法を
実施するのに好ましい装置の1例を示すものである。
To explain the invention with the aid of figures, FIG. 1 shows one example of a preferred apparatus for carrying out the method of the invention.

第1図に於て、ホッパー1より供給された熱硬化性樹脂
材料はシリンダー2内でヒーター3により加熱熔融され
、スクリュー4のフライト先端部よりうセン状で平滑部
5へ移行し、シリンダーとの摩擦抵抗により、スクリュ
ーフライトによって生ずる間隙部分が狭められついには
圧融着される。
In Fig. 1, the thermosetting resin material supplied from the hopper 1 is heated and melted by the heater 3 in the cylinder 2, moves from the tip of the flight of the screw 4 to the smooth part 5 in a spiral shape, and then joins the cylinder. Due to the frictional resistance, the gap created by the screw flight is narrowed and finally pressure fused.

次いで融着樹脂は、スクリュー平滑部を移動する間に、
押出後自己形状を保持できる程度にまで賦形され、この
際シリンダー先端に装着された背圧付与装置6により適
度な背圧がかかシ、樹脂は充分に圧融着、賦形されてシ
リンダー先端、背圧付与装置を経て連続したパイプ状成
形品7となって押出される。
Next, while the fusion resin moves on the screw smooth part,
After extrusion, the resin is shaped to the extent that it can maintain its own shape, and at this time, an appropriate back pressure is applied by the back pressure applying device 6 installed at the tip of the cylinder, and the resin is sufficiently pressure-fused and shaped to form the cylinder. The tip passes through a back pressure applying device and is extruded into a continuous pipe-shaped molded product 7.

第2図および第3図は本発明の特徴の1つである背圧付
与装置の1例を示すものであシ、割シ型8、締付は具9
及びアダプター10より成シ、締め付は具がアダフリー
へネジ込まれることにより、割り型を締め付ける構造と
なっている。この締め付けの程度を変えることにより背
圧付与効果を加減することができる。
Figures 2 and 3 show an example of a back pressure applying device which is one of the features of the present invention.
The split mold is tightened by screwing the tool into the adapter 10 and the adapter 10. By changing the degree of tightening, the effect of applying back pressure can be adjusted.

本発明の背圧付与装置は、この構造に限定されるもので
はなく、例えば、筒の一端に割り溝を切ったものを周囲
より締め付ける構造のもの、筒の内面に先端に向って内
径が小さくなるようにテーパーをつけたもの(この場合
は背圧付与効果は固定される)等が挙げられ、締め付は
方法もネジ込みだけでなく油圧、空気圧、バネなどによ
る方法を採用することができる。すなわち、本発明で言
う背圧付与装置はシリンダー内径より、極くわずか径の
小さな内径を有する装置であれば良く、その中をパイ”
プが通る際に適度な抵抗を与えるものであれば良い。又
、その内径を調整できる機構であれば更に望ましい。
The back pressure applying device of the present invention is not limited to this structure, but for example, a structure in which a groove is cut at one end of the cylinder and tightened from the surroundings, or a structure in which the inner diameter of the cylinder is narrowed toward the tip. (In this case, the effect of applying back pressure is fixed) etc. For tightening, methods such as hydraulic pressure, pneumatic pressure, springs, etc. can be used in addition to screwing. . In other words, the back pressure applying device referred to in the present invention may be any device that has an inner diameter that is extremely slightly smaller than the inner diameter of the cylinder, and the
It is sufficient as long as it provides a suitable amount of resistance when the pipe passes through. Further, it would be even more desirable if the mechanism could adjust its inner diameter.

本発明の押出成形装置の他の特徴は押出機の先端部の構
造にあシ、特に先端に平滑部を有するスクリューを使用
して賦形する点にある。使用される押出装置としては、
単軸スクリュー押出装置のみならず、二軸スクリューあ
るいは多軸スクリュー押出装置であっても先端部が最終
的に単軸に集約される押出装置の何れも使用できる。本
発明に使用できるこれらの押出装置の内部構造として、
押出装置の供給部から先端の計量部に至る間に脱気孔を
設けたり、特殊な混線構造を設けることは何ら差し支え
ない。
Another feature of the extrusion molding apparatus of the present invention is that the tip of the extruder is shaped using a reed, particularly a screw having a smooth portion at the tip. The extrusion equipment used is
Not only a single-screw extrusion device, but also any extrusion device, such as a twin-screw extrusion device or a multi-screw extrusion device, whose tip end is finally consolidated into a single screw can be used. The internal structure of these extrusion devices that can be used in the present invention is as follows:
There is no problem in providing a deaeration hole or a special cross-wire structure between the supply section and the measuring section at the tip of the extrusion device.

本発明に使用されるスクリューの代表的なものは、第4
図に示す様に先端部に平滑部5を有するスクリュー(以
下特殊スクリューと略称する)であり、このスクリュー
は、例えば供給部11、圧縮部12、計量部13よりな
る。平滑部5は第4図の様に供給部の終了したところか
ら、また第5図の様に圧縮部の終了したところからある
いは第6図の様に計量部の途中から始まる様な型式でも
良い。
A typical screw used in the present invention is a fourth screw.
As shown in the figure, it is a screw (hereinafter referred to as a special screw) having a smooth portion 5 at its tip, and this screw includes, for example, a supply section 11, a compression section 12, and a metering section 13. The smooth section 5 may be of a type such that it starts from the end of the supply section as shown in Fig. 4, from the end of the compression section as shown in Fig. 5, or from the middle of the measuring section as shown in Fig. 6. .

また平滑部5のスクリュー径またはその部位のシリンダ
ーの内径は、フライトを有する部位のスクリュー底部の
径および又はシリンダーの内径とは別個に、所望する成
形品の外径および内径に合わせて等しくまたは異なる径
に、即ち拡大もしくは縮小して調整することができる。
In addition, the diameter of the screw in the smooth part 5 or the inner diameter of the cylinder in that part may be equal to or different from the diameter of the screw bottom of the part having flights and/or the inner diameter of the cylinder, depending on the outer diameter and inner diameter of the desired molded product. The diameter can be adjusted by expanding or contracting.

この装置に使用される特殊スクリューのL / Dは、
通常7〜40、好ましくは10〜35、更に好ましくは
15〜25、圧縮比は1.0〜5.0好ましくけ1.2
〜40、更に好ましくは15〜6.01スクリユ一先端
部の平滑部の長さは1D〜15D好ましくは2D〜10
D1更に好ましくは2D〜7Dの範囲から適宜選択する
ことができる。
The L/D of the special screw used in this device is:
Usually 7-40, preferably 10-35, more preferably 15-25, compression ratio 1.0-5.0 preferably 1.2
~40, more preferably 15~6.01 The length of the smooth part of the tip of the screw is 1D~15D, preferably 2D~10
D1, more preferably, can be appropriately selected from the range of 2D to 7D.

先端に平滑部の無い通常のフルフライトスクリューでは
パイプ状の成形品は得られず、ラセン状の成形品が得ら
れるのみである。更に平滑部の長さが1D未満の場合は
、押出後得られる成形品に変形が生じ連続的に良好な成
形品を得ることが困難である。また平滑部の長さが15
D以上となる場合は、成形圧力が大きくなり、押出装置
の機械強度の点からも実用的でない。
A normal full-flight screw without a smooth part at the tip cannot produce a pipe-shaped molded product, but only a helical-shaped molded product. Furthermore, if the length of the smooth portion is less than 1D, the molded product obtained after extrusion will be deformed, making it difficult to continuously obtain a good molded product. Also, the length of the smooth part is 15
When it is D or more, the molding pressure becomes large and it is not practical from the point of view of the mechanical strength of the extrusion device.

スクリューの圧縮比と平滑部の長さは、スクリューの平
滑部とそれに対応するシリンダー部分とによって形成さ
れる間隙、換言すれば成形品の肉厚、押出速度及び使用
する材料の特性等の組合せによって種々の制限を受ける
。而してスクリューの圧縮比と平滑部の長さは、それが
大きい程あるいは小さい程、背圧付与機能が大きくある
いは小さい。
The compression ratio of the screw and the length of the smooth part are determined by the gap formed by the smooth part of the screw and the corresponding cylinder part, in other words, by a combination of the thickness of the molded product, extrusion speed, and the characteristics of the material used. Subject to various restrictions. The larger or smaller the compression ratio of the screw and the length of the smooth portion, the larger or smaller the back pressure applying function.

背圧が大きすぎるとフライトを有する部分で過度の混線
が起シ、その結果として材料の過度の発熱と硬化が起る
ので好ましくない。一方、背圧が小さすぎると材料の圧
縮充填及び混線が不充分となるので同様に好ましくない
。適度な背圧が材料の圧縮充填と適度な混線のために必
要である。
If the back pressure is too large, excessive cross-talk will occur in the portion having flights, resulting in excessive heat generation and hardening of the material, which is undesirable. On the other hand, if the back pressure is too small, compression and filling of the material and crosstalk will become insufficient, which is likewise undesirable. Adequate back pressure is necessary for compaction filling of the material and adequate cross-crossing.

即ち、安定した押出と良好な製品を得るためには適度の
スクリューの圧縮比と平滑部の長さが要求される。
That is, in order to achieve stable extrusion and a good product, an appropriate compression ratio of the screw and a suitable length of the smooth portion are required.

そしてスクリューの平滑部とそれに対応するシリンダー
部分とによって形成される間隙が大きい程あるいは小さ
い程、押出速度が小さい程あるいは大きい程、使用する
材料の粘度が小さい程あるいは大きい程、また使用する
材料の硬化速度が小さい程あるいは大きい程、スクリュ
ーの圧縮比と平滑部の長さは大きくあるいは小さくする
必要がある。
The larger or smaller the gap formed by the smooth part of the screw and the corresponding cylinder part, the lower or higher the extrusion speed, the lower or higher the viscosity of the material used, the more The lower or higher the curing rate, the larger or smaller the compression ratio of the screw and the length of the smooth part need to be.

このスクリュー型押出成形装置を使用するにあたって、
押出装置各部の温度設定は、使用する材料の特性やスク
リューの圧縮比、スクリュー平滑部とバレルの間隙、平
滑部の長さ、押出速度等の組合せにより当然変る−が、
スクリューの圧縮部、計量部及び平滑部に対応するシリ
ンダー部位の温度設定は通常50〜200℃、好ましく
は60〜150℃の範囲であり、通常かかる設定温度で
成形し得る熱容量の熱供給機能を有するシリンダー構造
が採られる。
When using this screw type extrusion molding equipment,
The temperature settings for each part of the extrusion device will naturally vary depending on the combination of the characteristics of the material used, the compression ratio of the screw, the gap between the smooth part of the screw and the barrel, the length of the smooth part, the extrusion speed, etc.
The temperature setting of the cylinder parts corresponding to the compression part, metering part, and smooth part of the screw is usually in the range of 50 to 200 °C, preferably 60 to 150 °C, and the heat supply function of the heat capacity that can normally be molded at this set temperature is A cylindrical structure is adopted.

而して設定温度が50℃以下の場合は、樹脂の硬化反応
が充分に進行しないため良好な成形品は得難い傾向があ
り、一方200℃までの温度で通常用いられる熱硬化性
樹脂は充分に熱硬化するのでそれ以上の熱供給機能にす
る必要はない。
However, if the set temperature is below 50°C, the curing reaction of the resin will not proceed sufficiently and it will be difficult to obtain a good molded product.On the other hand, thermosetting resins normally used at temperatures up to 200°C will Since it is thermally cured, there is no need for any further heat supply function.

このスクリュー型押出成形装置においては、スクリユー
平滑部とそれに対応するシリンダー部分とによって形成
される間隙部において硬化反応が促進され少くとも押出
後成形品が自己形状を保持できる程度にまで進められ且
つこの間において最終成形品または殆んどそれに近似す
る形状にまで賦形される。
In this screw type extrusion molding apparatus, the curing reaction is promoted in the gap formed by the screw smooth part and the corresponding cylinder part, and the curing reaction is advanced to at least the extent that the molded product can maintain its own shape after extrusion, and during this time The finished product is then shaped into the final molded product or a shape that closely approximates it.

従来の熱硬化性樹脂の押出成形に於てはシリンダー内で
加熱溶融された樹脂は、アダプターを経て金型内へ導入
され最終形状に賦形されるが、この過程に於て樹脂の流
れはアダプターで絞られ、スパイダーで固定されたマン
ドレルの回シヘ再展張されるなど樹脂の流路が複雑に変
化するために、樹脂の滞留が起シやすく、局部的に硬化
反応が進行したシ、僅かな圧力や温度の変化で硬化反応
が急激に起るなどの問題を引き起す。−!だ、複雑な流
路による抵抗に打ち勝ち滞留を防止しつつ樹脂を押出す
ためには、強大な押出圧力を要し特殊な押出装置を必要
とする。而してかかる成形法による場合の押出速度は高
々3QcWL/min程度であシ且つ真円度及び肉厚分
□布の良いものを得ることは困難である。
In conventional extrusion molding of thermosetting resin, the resin is heated and melted in a cylinder, then introduced into the mold through an adapter and shaped into the final shape, but during this process, the flow of the resin is Because the flow path of the resin changes in a complicated way, such as being squeezed with an adapter and re-expanded into a mandrel fixed with a spider, resin tends to stagnate, and the curing reaction progresses locally. Changes in pressure or temperature can cause problems such as rapid curing reactions. -! However, in order to overcome the resistance created by the complicated flow paths and extrude the resin while preventing stagnation, it requires enormous extrusion pressure and special extrusion equipment. However, when using such a molding method, the extrusion speed is at most about 3 QcWL/min, and it is difficult to obtain a product with good roundness and wall thickness distribution.

本発明のスクリュー型押出成形装置によればスクリュー
平滑部とそれに対応するシリンダー部分とによって形成
される間隙部分が金型の役割を果たし、樹脂の流路はシ
リンダーとスクリューとの間隙のみであるため、樹脂の
滞留は全くなく局部的な硬化反応や圧力、温度の変化に
よる急激な硬化反応を引き起すことがない。
According to the screw type extrusion molding apparatus of the present invention, the gap formed by the screw smooth part and the corresponding cylinder part plays the role of a mold, and the only resin flow path is the gap between the cylinder and the screw. There is no stagnation of resin at all, and localized curing reactions and rapid curing reactions due to changes in pressure and temperature do not occur.

また本発明のスクリューは先端が開放されており、その
全長に於て昇圧機能部分と背圧付与機能部分をもつため
、両者の力が相殺しスクリューのスラストベアリングに
かかる力はスクリューと金型を用いる一般的な押出成形
法にくらべ本質的に小さい。
In addition, the screw of the present invention has an open tip and has a pressure increasing function part and a back pressure applying function part over its entire length, so the forces of the two cancel each other out and the force applied to the thrust bearing of the screw is reduced by the force between the screw and the mold. It is inherently smaller than the common extrusion methods used.

更に、一般的押出成形法に於ける金型内のマンドレルに
相当する本発明のスクリュー平滑部は回転しているため
、硬化した樹脂と金属部分との摩擦抵抗が、比較的小さ
く、押出圧力も通常のスクリュー押出装置で得られる圧
力で充分である。この゛様な本発明の装置による場合は
、80m/minのような押出速度が容易に得られる。
Furthermore, since the smooth part of the screw of the present invention, which corresponds to the mandrel in the mold in general extrusion molding, is rotating, the frictional resistance between the hardened resin and the metal part is relatively small, and the extrusion pressure is also low. Pressures obtained with conventional screw extrusion equipment are sufficient. With this type of apparatus of the present invention, an extrusion speed of 80 m/min can be easily obtained.

本発明に用いられる熱硬化性樹脂としては、フェノール
樹脂、メラミン樹脂、尿素樹脂、不飽和ポリエステル樹
脂、エポキシ樹脂、シリコンm脂、アリル樹脂、キシレ
ン樹脂、アニリン樹脂等が挙げられ、なかでもフェノー
ル樹脂およびメラミン樹脂の成形に好適である。
Thermosetting resins used in the present invention include phenolic resins, melamine resins, urea resins, unsaturated polyester resins, epoxy resins, silicon resins, allyl resins, xylene resins, aniline resins, etc. Among them, phenolic resins It is also suitable for molding melamine resin.

而してこれ等の熱硬化性樹脂には必要に応じて熱硬化性
樹脂の成形に於て一般に用いられる充填剤、離型剤、増
粘剤、着色剤、分散剤、発泡剤、あるいはまた重合開始
剤、硬化促進剤、重合禁止剤などを添加することができ
る。また更に他種のポリマーあるいは有機または無機の
繊維状物、例えば硝子等を加えることもできる。
Therefore, these thermosetting resins may contain fillers, mold release agents, thickeners, colorants, dispersants, blowing agents, or other agents commonly used in the molding of thermosetting resins, as necessary. A polymerization initiator, a curing accelerator, a polymerization inhibitor, etc. can be added. Furthermore, other types of polymers or organic or inorganic fibrous materials such as glass can also be added.

上記した本発明のスクリュー型押出成形装置により得ら
れる/熱硬化性樹脂管は耐熱性、耐燃性、耐薬品性、耐
圧性に優れ、各種配管材料、\例えば、流体移送管、保
護管\×シて有用である。
The thermosetting resin pipe obtained by the above-mentioned screw type extrusion molding apparatus of the present invention has excellent heat resistance, flame resistance, chemical resistance, and pressure resistance, and is suitable for various piping materials, such as fluid transfer pipes and protection pipes. This is useful.

作用: 本発明の装置を用いることにより、シリンダー内の背圧
を最適に保持できることにより、平滑部における樹脂の
圧縮融着が充分に行なわれ、肉厚のパイプが安定して生
産性良く得られるのみならず、光沢や表面平滑性の優れ
た直線性の良いパイプが得られ、更にパイプの強度も向
上する。
Effect: By using the device of the present invention, the back pressure inside the cylinder can be optimally maintained, and the resin can be sufficiently compressed and fused in the smooth part, making it possible to obtain thick-walled pipes stably and with high productivity. In addition, a pipe with excellent gloss and surface smoothness and good straightness can be obtained, and the strength of the pipe is also improved.

以下、本発明を実施例により更に説明する。The present invention will be further explained below with reference to Examples.

実施例1 ホッパー下より2Dの長さに水冷ジャケットを備え、続
いて3D〜10D、11D〜16D、17を有する押出
機の先端に第2図に示した背圧付与装置を装着し、供給
部3D、圧縮部14D1スクリュー底部の径が32朋の
計量部に続く先端部に長さ4D、径32..の平滑部を
有するスクリューを使用し、成形材料としてフェノール
樹脂(日本合成化工株式会社製、商品名ニッカライ) 
950−J )を用いて成形を行なった。
Example 1 A water cooling jacket was provided at a length of 2D from below the hopper, and the back pressure applying device shown in FIG. 3D, the compression part 14D1 has a length of 4D and a diameter of 32mm at the tip that continues to the measuring part with a diameter of 32mm at the bottom of the screw. .. A screw with a smooth part is used, and phenol resin (manufactured by Nippon Gosei Kako Co., Ltd., product name Nikkarai) is used as the molding material.
950-J) was used for molding.

シリンダー各部の温度は、 C□(0〜2D)・・・・水冷 C2(3D〜10D)・・・・ 80℃C3(’11D
〜16D)・・・・ 95℃C4(17D〜20D)・
・・・115℃C5(21D〜24D)・・・・125
℃に設定し、背圧付与装置の割り型内径を錦6朋にしぼ
りスクリュー回転数35 rpmで押出しを行なった。
The temperature of each part of the cylinder is C□ (0~2D)...Water-cooled C2 (3D~10D)...80℃C3 ('11D)
~16D)...95℃C4(17D~20D)・
...115℃C5 (21D~24D)...125
℃, the inner diameter of the split mold of the back pressure applying device was reduced to 6 mm, and extrusion was performed at a screw rotation speed of 35 rpm.

結果を第1表に示した。The results are shown in Table 1.

比較例1 実施例N1と同じ押出機、スクリュー、成形材料を使用
し、背圧付与装置を付けずに同条件で押出成形を行なっ
た。
Comparative Example 1 Using the same extruder, screw, and molding material as in Example N1, extrusion molding was performed under the same conditions without adding a back pressure applying device.

結果を第1表に示した。The results are shown in Table 1.

実施例2 実施例1と同じ装置を用い、成形材料としてフェノール
樹脂(商品名0N−4400、松下電工株式会社製)を
使用して成形を行なった。
Example 2 Using the same equipment as in Example 1, molding was performed using phenol resin (trade name: 0N-4400, manufactured by Matsushita Electric Works, Ltd.) as a molding material.

シリンダー各部の温度は、C□・・・・水冷、C2・・
・・80℃、C3・・・・100℃、C4・・・・12
0℃、C5・・・・130℃に設定し、背圧付与装置の
割り型内径を39.8mmにしばってスクリュー回転数
35 rpmで押出しを行なった。
The temperature of each part of the cylinder is C□...water cooling, C2...
...80℃, C3...100℃, C4...12
The temperature was set at 0°C, C5...130°C, the inner diameter of the split mold of the back pressure applying device was set to 39.8 mm, and extrusion was performed at a screw rotation speed of 35 rpm.

結果を第1表に示した。The results are shown in Table 1.

比較例2 実施例2と同じ押出機、スクリュー、成形材料 −を使
用し背圧付与装置を用いずに同条件で押出成形を行なっ
た。結果を第1表に示した。
Comparative Example 2 Extrusion molding was carried out using the same extruder, screw, and molding material as in Example 2 under the same conditions without using a back pressure applying device. The results are shown in Table 1.

実施例3 実施例1と同じ装置を用い、成形材料としてメラミン樹
脂(商品名 0N−600,オタライト株式会社製)を
使用して成形を行なった。
Example 3 Using the same equipment as in Example 1, molding was performed using melamine resin (trade name: 0N-600, manufactured by Otalite Co., Ltd.) as a molding material.

シリンダー各部の温度は、C□・・・・水冷、C2・・
・・85℃、C3・・・・105℃、C4・・・・12
5℃、C5・・・・140℃に設定し、背圧付与装置の
割り型内径を697朋にしぼってスクリュー回転数32
 rpmで押出を行なったb結果を第1表に示した。
The temperature of each part of the cylinder is C□...water cooling, C2...
...85℃, C3...105℃, C4...12
Set the temperature to 5℃, C5...140℃, reduce the inner diameter of the split mold of the back pressure applying device to 697mm, and set the screw rotation speed to 32mm.
Table 1 shows the results for extrusion at rpm.

比較例6 実施例3と同じ押出機、スクリュー、成形材料を使用し
、背圧付与装置を付けずに、同じ条件で押出成形を行な
った。結果を第1表に示した。
Comparative Example 6 Using the same extruder, screw, and molding material as in Example 3, extrusion molding was carried out under the same conditions without adding a back pressure applying device. The results are shown in Table 1.

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

第1図は本発明に用いられる好ましい装置の14〜6図
は平滑部を有するスクリューの1例を示すものであシ、
第7図乃至12図は各実施例及び各比較例により得られ
たパイプの表面平滑性を示したチャートである。 1・・・・ホッパー 2・・・・シリンダー 3・・・
・ヒーター 4・・・・スクリュー 5・・・・平滑部
6・・・・背圧付与装置 7・・・・成形品 8・・・
・割り型 9・・・・締め付は具 10・・・・アダプ
ター11・・・・供給部 12・・・・圧縮部 13・
・・・計量部
FIG. 1 shows an example of a screw having a smooth portion, and FIG.
FIGS. 7 to 12 are charts showing the surface smoothness of the pipes obtained in each Example and each Comparative Example. 1...Hopper 2...Cylinder 3...
・Heater 4...Screw 5...Smooth part 6...Back pressure applying device 7...Molded product 8...
- Split mold 9... Tightening tool 10... Adapter 11... Supply section 12... Compression section 13.
...Measuring part

Claims (1)

【特許請求の範囲】[Claims] 1)供給部、圧縮部、計量部および平滑部から成るスク
リュー、該供給部、圧縮部および計量部に対応する熱制
御機構を有するシリンダー部分、該計量部の最終スクリ
ュー径に等しいか又は異なる径を有する該平滑部に対応
する熱供給機能を有するシリンダー部分、およびシリン
ダーの先端に装着された背圧付与装置より成り、該平滑
部とそれに対応するシリンダー部分とによつて形成され
る間隙部において硬化反応を促進させ押出後自己形状を
保持できる程度にまで賦形する様にした熱硬化性樹脂の
スクリュー型押出成形装置。
1) A screw consisting of a feeding section, a compression section, a metering section and a smooth section, a cylinder section having a thermal control mechanism corresponding to the feeding section, compression section and metering section, and a diameter equal to or different from the final screw diameter of the metering section. and a back pressure applying device attached to the tip of the cylinder, and in the gap formed by the smooth part and the corresponding cylinder part. A screw type extrusion molding device for thermosetting resin that accelerates the curing reaction and shapes the resin to the extent that it can maintain its own shape after extrusion.
JP59136580A 1984-07-03 1984-07-03 Screw type extruding apparatus for thermosetting resin Pending JPS6116828A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59136580A JPS6116828A (en) 1984-07-03 1984-07-03 Screw type extruding apparatus for thermosetting resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59136580A JPS6116828A (en) 1984-07-03 1984-07-03 Screw type extruding apparatus for thermosetting resin

Publications (1)

Publication Number Publication Date
JPS6116828A true JPS6116828A (en) 1986-01-24

Family

ID=15178597

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59136580A Pending JPS6116828A (en) 1984-07-03 1984-07-03 Screw type extruding apparatus for thermosetting resin

Country Status (1)

Country Link
JP (1) JPS6116828A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63278062A (en) * 1987-05-09 1988-11-15 Mitsui Toatsu Chem Inc Continuous production of photosensitive drum
JPS63278064A (en) * 1987-05-09 1988-11-15 Mitsui Toatsu Chem Inc Continuous production of photosensitive drum
JPS63278061A (en) * 1987-05-09 1988-11-15 Mitsui Toatsu Chem Inc Continuous production of photosensitive drum
JPS6428655A (en) * 1987-07-24 1989-01-31 Mitsui Toatsu Chemicals Cylinder for electrostatic latent image formation drum
JPH054268A (en) * 1990-11-27 1993-01-14 Mitsui Toatsu Chem Inc Extrusion molding method of phenolic resin pipe and device therefor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63278062A (en) * 1987-05-09 1988-11-15 Mitsui Toatsu Chem Inc Continuous production of photosensitive drum
JPS63278064A (en) * 1987-05-09 1988-11-15 Mitsui Toatsu Chem Inc Continuous production of photosensitive drum
JPS63278061A (en) * 1987-05-09 1988-11-15 Mitsui Toatsu Chem Inc Continuous production of photosensitive drum
JPS6428655A (en) * 1987-07-24 1989-01-31 Mitsui Toatsu Chemicals Cylinder for electrostatic latent image formation drum
JPH054268A (en) * 1990-11-27 1993-01-14 Mitsui Toatsu Chem Inc Extrusion molding method of phenolic resin pipe and device therefor

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