JPS6250288B2 - - Google Patents

Info

Publication number
JPS6250288B2
JPS6250288B2 JP55039050A JP3905080A JPS6250288B2 JP S6250288 B2 JPS6250288 B2 JP S6250288B2 JP 55039050 A JP55039050 A JP 55039050A JP 3905080 A JP3905080 A JP 3905080A JP S6250288 B2 JPS6250288 B2 JP S6250288B2
Authority
JP
Japan
Prior art keywords
resin
die
extruder
adapter
uneven
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
JP55039050A
Other languages
Japanese (ja)
Other versions
JPS56136344A (en
Inventor
Akira Shimizu
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.)
MODAN MACHINERY
Original Assignee
MODAN MACHINERY
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 MODAN MACHINERY filed Critical MODAN MACHINERY
Priority to JP3905080A priority Critical patent/JPS56136344A/en
Publication of JPS56136344A publication Critical patent/JPS56136344A/en
Publication of JPS6250288B2 publication Critical patent/JPS6250288B2/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
    • 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
    • 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

Landscapes

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

Description

【発明の詳細な説明】 本発明は、合成樹脂押出し方向が異なる合成樹
脂押出機(以下単に押出機という)とダイを接続
して合成樹脂の流れの方向を変えるアダプタの改
良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in an adapter that connects a synthetic resin extruder (hereinafter simply referred to as an extruder) and a die that extrude synthetic resin in different directions to change the flow direction of the synthetic resin.

第1図に示すように、一般に使用されている押
出機用アダプタ106の樹脂流路101は、ダイ
102に向かうに従つて次第に狭められ且つ直角
方向に曲げられたものである。このような樹脂流
路101の場合、ダイ102から引出されるフイ
ルム103に偏肉を生じる。この現象は、回転式
あるいはオシレート式ダイを使用しても発生する
ものであり、又ブロー成形においても防ぎえない
ものである。これはダイ102あるいは押出機1
04の欠陥によるものでなく、樹脂流路101の
屈曲部分Aにおいて溶融樹脂量の片寄りが生じる
ことに基因している。つまり、押出機104のス
クリユー105によつて押出される溶融樹脂が屈
曲部分において前方の面に押しつけられながらそ
の流れの方向を変えることから、流路部分101
の壁に近い箇所に樹脂量の粗な領域或いは密な領
域とが発生してしまう。そして、これがダイ10
2においても解消されずに押出し樹脂量に局部的
不均等を与えてしまう。
As shown in FIG. 1, a resin flow path 101 of a commonly used extruder adapter 106 is gradually narrowed toward a die 102 and bent at right angles. In the case of such a resin flow path 101, uneven thickness occurs in the film 103 drawn out from the die 102. This phenomenon occurs even when a rotary or oscillating die is used, and cannot be prevented even in blow molding. This is die 102 or extruder 1
This is not due to the defect 04, but is caused by the unevenness of the amount of molten resin in the bent portion A of the resin flow path 101. In other words, since the molten resin extruded by the screw 105 of the extruder 104 changes the flow direction while being pressed against the front surface at the bent portion, the flow path portion 101
Areas with a coarse amount of resin or areas with a dense amount of resin occur near the walls. And this is die 10
Even in case 2, the problem is not solved and the amount of extruded resin becomes locally uneven.

本発明は、樹脂量不均等部の発生を阻止するこ
とができる合成樹脂押出機用アダプタを提供する
ことを目的とし、その構成は、合成樹脂押出し方
向が異なる押出機とダイを接続するアダプタにお
いて、合成樹脂の流れの方向を変える樹脂流路を
2本以上形成すると共に前記ダイに直結する対称
形状の樹脂出口室を形成し、該樹脂出口室に前記
複数の樹脂流路を合流せしめたことを特徴とす
る。
An object of the present invention is to provide an adapter for a synthetic resin extruder that can prevent the occurrence of uneven resin amounts. , forming two or more resin flow channels that change the flow direction of the synthetic resin, and forming a symmetrical resin outlet chamber directly connected to the die, and merging the plurality of resin flow channels into the resin outlet chamber. It is characterized by

以下本発明の構成を図面に示す一実施例に基づ
いて詳細に説明する。尚、本実施例はインフレー
シヨン装置に応用したものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The structure of the present invention will be explained in detail below based on an embodiment shown in the drawings. Note that this embodiment is applied to an inflation device.

アダプタ6は、ダイ2と押出機4とを連結する
もので、押出機バレル7の前端面に取付けられ、
ダイ2を上方に載置する。該アダプタ6には、押
出機4から押出される溶融樹脂をダイ2に導く樹
脂流路1が2本以上穿孔されている。前記樹脂入
口室8と押出機バレル7とは直接繋がれておら
ず、スクリーンパツク9およびブレーカプレート
10を介して連通状態とされている。しかし、第
3図に示すようにブレーカプレート10を使用せ
ずに樹脂入口室8に直接スクリーンパツク9を配
置することもある。他方、樹脂出口室11側には
ダイ2がねじ込まれている。この樹脂出口室11
は、各樹脂流路1を通つてきた溶融樹脂が合流す
る部分で、均一な状態で樹脂をダイ2内へ押込ま
せるために対称形状とされている。
The adapter 6 connects the die 2 and the extruder 4, and is attached to the front end surface of the extruder barrel 7.
Place die 2 above. The adapter 6 is provided with two or more resin channels 1 for guiding the molten resin extruded from the extruder 4 to the die 2. The resin inlet chamber 8 and the extruder barrel 7 are not directly connected, but communicated through a screen pack 9 and a breaker plate 10. However, as shown in FIG. 3, the screen pack 9 may be placed directly in the resin inlet chamber 8 without using the breaker plate 10. On the other hand, a die 2 is screwed into the resin outlet chamber 11 side. This resin outlet chamber 11
is a part where the molten resin that has passed through each resin flow path 1 joins, and has a symmetrical shape in order to force the resin into the die 2 in a uniform state.

以上のように構成されているので、溶融樹脂は
次の如く流れる。まず、加熱・冷却装置によつて
一定温度に保たれた押出機バレル7内の溶融樹脂
はスクリユー5によつて混練されながらアダプタ
6側へ押し込まれる。この溶融樹脂はスクリーン
パツク9並びにブレーカプレート10間を通過し
てアダプタ6の樹脂入口室8に流れ込んでから更
に各樹脂流路1に分かれてダイ2へと向かう。各
樹脂流路1内を流れる合成樹脂には流路屈曲部A
より樹脂量不均等箇所が夫々発生するが、樹脂出
口室11において合流した溶融樹脂にはフイルム
の偏肉を伴う樹脂量不均等の発生は少ない。これ
は個々の樹脂流路1においては樹脂量不均等は生
じるものの全体に分散されているので、合流した
状態では全体に偏在する小さな不均等箇所は問題
とならない。つまり、従来の如く大きな不均等部
分が局所的に存在する場合には、ダイ2内におけ
る分流・噴出時にも溶融樹脂量の不均等を招いて
偏肉を惹起するが、本発明による全体に小さな不
均等部分が存在するぶんには局部的偏肉には影響
しない。
With the above structure, the molten resin flows as follows. First, the molten resin in the extruder barrel 7, which is kept at a constant temperature by the heating/cooling device, is pushed into the adapter 6 side while being kneaded by the screw 5. The molten resin passes between the screen pack 9 and the breaker plate 10, flows into the resin inlet chamber 8 of the adapter 6, and then further divides into resin flow paths 1 and heads toward the die 2. The synthetic resin flowing in each resin flow path 1 has a flow path bent portion A.
As a result, uneven resin amounts occur at different locations, but the molten resin that merges in the resin outlet chamber 11 rarely has uneven resin amounts that are accompanied by uneven thickness of the film. Although the amount of resin is uneven in each resin flow path 1, it is dispersed throughout, so in the merged state, small uneven spots unevenly distributed throughout the resin flow path do not pose a problem. In other words, if there is a large uneven part locally as in the conventional case, the amount of molten resin will become uneven even when the flow is divided or ejected in the die 2, causing uneven thickness. As long as there are uneven parts, there is no effect on local thickness unevenness.

このことは、第4図a,bに示す実験結果によ
つて実証される。第4図aの実験結果は第1図に
示す従来のアダプタを使用したもので、 押出機:50mm押出機 ダイ:円形ダイ 樹脂:低密度ポリエチレン 押出し量:35Kg/h の条件で稼動した場合、B点に局部的偏肉が生じ
ている。しかも、全体の偏肉は60ミクロンのフイ
ルム厚に対して+4ミクロン、−6.5ミクロンであ
る。
This is demonstrated by the experimental results shown in FIGS. 4a and 4b. The experimental results shown in Figure 4a were obtained using the conventional adapter shown in Figure 1.Extruder: 50mmExtruder die: Circular dieResin: Low density polyethyleneExtrusion rate: 35Kg/h Local thickness unevenness occurs at point B. Moreover, the overall thickness deviation is +4 microns and -6.5 microns for a film thickness of 60 microns.

これに対し、第4図bに示された本発明のアダ
プタ6を使用したものは顕著な偏肉を呈さなかつ
た。つまり、押出機、ダイ、樹脂を同条件にして
押出し量を46.2Kg/hとした場合、全体の偏肉は
60ミクロンのフイルム厚に対し+4ミクロン、−
2ミクロンである。但し、樹脂流路はφ6mm×37
個である。
On the other hand, the adapter using the adapter 6 of the present invention shown in FIG. 4b did not exhibit any noticeable uneven thickness. In other words, if the extruder, die, and resin are used under the same conditions and the extrusion rate is 46.2 kg/h, the overall thickness deviation is
+4 microns for a film thickness of 60 microns, -
It is 2 microns. However, the resin flow path is φ6mm x 37
It is individual.

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

第1図は従来の合成樹脂押出機用アダプタの一
例を一部断面して示す側面図である。第2図は本
発明の合成樹脂押出機用アダプタの一実施例を一
部断面して示す側面図、第3図は押出機とアダプ
タの接続状態を説明する中央縦断側面図である。
第4図aは第1図に示す従来のアダプタを用いた
場合の偏肉テスト結果を示す偏肉チヤート、第4
図bは本発明のアダプタを用いた場合の偏肉テス
ト結果を示す偏肉チヤートである。 図面中、1は樹脂流路、2はダイ、3はフイル
ム、4は押出機、6はアダプタ、8は樹脂入口
室、11は樹脂出口室、Aは樹脂流路の屈曲部
分、Bは局部的偏肉箇所である。
FIG. 1 is a partially sectional side view of an example of a conventional adapter for a synthetic resin extruder. FIG. 2 is a partially sectional side view showing an embodiment of the adapter for a synthetic resin extruder of the present invention, and FIG. 3 is a central vertical sectional side view illustrating the state of connection between the extruder and the adapter.
Figure 4a is a thickness unevenness chart showing the thickness unevenness test results when using the conventional adapter shown in Figure 1.
FIG. b is a thickness unevenness chart showing the results of a thickness unevenness test when using the adapter of the present invention. In the drawing, 1 is a resin flow path, 2 is a die, 3 is a film, 4 is an extruder, 6 is an adapter, 8 is a resin inlet chamber, 11 is a resin outlet chamber, A is a bent part of the resin flow path, and B is a local part. This is a spot with uneven thickness.

Claims (1)

【特許請求の範囲】[Claims] 1 合成樹脂押出し方向が異なる押出機とダイを
接続するアダプタにおいて、合成樹脂の流れの方
向を変える樹脂流路を2本以上形成すると共に前
記ダイに直結する対称形状の樹脂出口室を形成
し、該樹脂出口室に前記複数の樹脂流路を合流せ
しめたことを特徴とする合成樹脂押出機用アダプ
タ。
1. In an adapter that connects an extruder and a die that extrude synthetic resin in different directions, two or more resin channels are formed to change the flow direction of the synthetic resin, and a symmetrical resin outlet chamber is formed that is directly connected to the die, An adapter for a synthetic resin extruder, characterized in that the plurality of resin channels are merged into the resin outlet chamber.
JP3905080A 1980-03-28 1980-03-28 Adaptor for extruder for synthetic resin Granted JPS56136344A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3905080A JPS56136344A (en) 1980-03-28 1980-03-28 Adaptor for extruder for synthetic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3905080A JPS56136344A (en) 1980-03-28 1980-03-28 Adaptor for extruder for synthetic resin

Publications (2)

Publication Number Publication Date
JPS56136344A JPS56136344A (en) 1981-10-24
JPS6250288B2 true JPS6250288B2 (en) 1987-10-23

Family

ID=12542293

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3905080A Granted JPS56136344A (en) 1980-03-28 1980-03-28 Adaptor for extruder for synthetic resin

Country Status (1)

Country Link
JP (1) JPS56136344A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0120107Y2 (en) * 1984-12-17 1989-06-13
DE102005043096A1 (en) * 2005-09-10 2007-03-15 Kreyenborg Verwaltungen Und Beteiligungen Gmbh & Co. Kg Device for filtering a fluid, in particular for plastics processing plants

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4922170U (en) * 1972-05-30 1974-02-25

Also Published As

Publication number Publication date
JPS56136344A (en) 1981-10-24

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