JPH0460405B2 - - Google Patents

Info

Publication number
JPH0460405B2
JPH0460405B2 JP60215957A JP21595785A JPH0460405B2 JP H0460405 B2 JPH0460405 B2 JP H0460405B2 JP 60215957 A JP60215957 A JP 60215957A JP 21595785 A JP21595785 A JP 21595785A JP H0460405 B2 JPH0460405 B2 JP H0460405B2
Authority
JP
Japan
Prior art keywords
parison
accumulation
die
cylinder rod
extrusion
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
Application number
JP60215957A
Other languages
Japanese (ja)
Other versions
JPS62202712A (en
Inventor
Shuji Higo
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.)
Kyoraku Co Ltd
Original Assignee
Kyoraku 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 Kyoraku Co Ltd filed Critical Kyoraku Co Ltd
Priority to JP60215957A priority Critical patent/JPS62202712A/en
Publication of JPS62202712A publication Critical patent/JPS62202712A/en
Publication of JPH0460405B2 publication Critical patent/JPH0460405B2/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
    • B29C48/03Extrusion 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
    • B29C48/25Component 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
    • B29C48/25Component 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
    • B29C48/325Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles being adjustable, i.e. having adjustable exit sections
    • 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
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/388Plasticisers, homogenisers or feeders comprising two or more stages using a screw extruder and a ram or piston
    • 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
    • B29C48/475Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pistons, accumulators or press rams
    • 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
    • B29C48/92Measuring, controlling or regulating
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92009Measured parameter
    • B29C2948/92076Position, e.g. linear or angular
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92009Measured parameter
    • B29C2948/92085Velocity
    • B29C2948/92104Flow or feed rate
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92361Extrusion unit
    • B29C2948/92409Die; Nozzle zone
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92466Auxiliary unit, e.g. for external melt filtering, re-combining or transfer between units
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/926Flow or feed rate
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92609Dimensions
    • B29C2948/92647Thickness
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92904Die; Nozzle zone

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、パリスンの押出方法及びその装置に
関するもので、さらに詳しくはパリスンのダイ出
口近傍の押出速度を制御することにより設定プロ
フアイルに応じた正確な肉厚変化が得られかつ肉
厚の差の大きいパリスンの押出も可能なパリスン
の押出方法及びその装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a parison extrusion method and an apparatus thereof, and more specifically, to an extrusion method and an apparatus for extruding a parison, and more specifically, by controlling the extrusion speed near the die exit of the parison, the extrusion speed can be accurately adjusted according to a set profile. The present invention relates to a parison extrusion method and an apparatus for extruding parisons that can obtain a wide change in wall thickness and can also extrude parisons with a large difference in wall thickness.

従来技術 パリスンの押出技術として、パリスンを押出す
際押出ヘツドの出口付近でダイとコアの関隙(所
謂スリツト)を変化させてパリスンの肉厚を変化
させることが知られている。一般にパリスンコン
トロールと呼ばれている(例えば、特開昭58−
42437号公報参照)。
Prior Art As a parison extrusion technique, it is known to change the thickness of the parison by changing the gap between the die and the core (so-called slit) near the exit of the extrusion head when extruding the parison. It is generally called parison control (for example, JP-A-58-
(Refer to Publication No. 42437).

発明が解決しようとする問題点 ダイとコアのスリツトを変化させる従来のパリ
スンコントロールでは、同一パリスンの短い部分
で厚肉部分と薄肉部分を形成することができなか
つた。つまり短い時間で所望の肉厚に応じてスリ
ツトを変化させても、スリツトの調整だけでは、
樹脂の流れを規制できないためである。一般に単
位時間当りの流量は、スリツトの断面積と流速と
の積である。そして断面積を急激に変化させると
流速が変化して所望の肉厚が得られなくなるので
ある。
Problems to be Solved by the Invention With conventional parison control that changes the slits in the die and core, it has not been possible to form thick and thin portions in short portions of the same parison. In other words, even if you change the slit according to the desired wall thickness in a short period of time, adjusting the slit alone will not work.
This is because the flow of resin cannot be regulated. Generally, the flow rate per unit time is the product of the cross-sectional area of the slit and the flow rate. If the cross-sectional area is suddenly changed, the flow velocity will change, making it impossible to obtain the desired wall thickness.

そこで、これらを是正するために、特開昭54−
133562号公報、特開昭56−95650号公報の提案が
されている。
Therefore, in order to correct these problems,
133562 and JP-A-56-95650 have been proposed.

しかし、前者は、スリツト間の圧力を検出して
その変化に応じてそのスリツトを補正するもので
あるが、これに於いてもスリツトの変化のみで肉
厚を規制するので上記と同様急激な変化に対応す
ることは困難であつた。とくに薄肉部分を押出す
場合どうしても流速が速くなりスウエルが発生し
て所望の肉厚を得ることができない。
However, in the former method, the pressure between the slits is detected and the slit is corrected according to the change, but in this case too, the wall thickness is regulated only by the change in the slit, so there is no sudden change like the above. It was difficult to respond to the Particularly when extruding a thin walled portion, the flow rate inevitably becomes high and swell occurs, making it impossible to obtain the desired wall thickness.

また後者は、パリスンとの肉厚の変化(公報中
では重量の変化と記載されている)を押出すごと
にフイードバツクして押出機の回転数を微調整し
て所定の肉厚に調整しようとするものであるが、
パリスン全体としてとらえシヨツト毎の重量の変
化をなくすことを目的とするものでパリスン内の
所望する各部分の肉厚を制御することができず、
厚肉部分と薄肉部分を有するパリスンを押出すこ
とはできない。
In addition, the latter attempts to fine-tune the rotational speed of the extruder by feeding back the change in wall thickness (described as a change in weight in the bulletin) to the parison each time it is extruded to achieve the desired wall thickness. However,
The object is to consider the parison as a whole and eliminate variations in weight from shot to shot, but it is not possible to control the thickness of each part of the parison as desired.
It is not possible to extrude a parison that has thick and thin sections.

問題を解決するための手段及び作用 そこで本発明の製造方法は、 ダイ出口の間〓を変化させて押出すパリスンの
肉厚を制御するパリスンの押出方法において、パ
リスンの厚肉部分ではパリスンの押出し速度を速
くし、逆にパリスンの薄肉部分ではパリスンの押
出し速度を遅くすることにより、前記ダイ出口の
間〓の変化によるパリスンの肉厚制御のずれを補
正することを特徴とするパリスンの押出方法。と
したことにより、パリスンの厚肉部分は正確に所
望の肉厚することができ、また逆に薄肉部分は従
来発生していたスウエルを取り除くことにより正
確に薄くすることができるので、同一パリスン内
の縦方向の短い距離の間で薄肉部分から厚肉部分
へあるいは厚肉部分から薄肉部分へ急激に変化さ
せることが可能である。
Means and Effects for Solving the Problems Therefore, the manufacturing method of the present invention is a parison extrusion method in which the thickness of the parison to be extruded is controlled by changing the distance between the die exits. A parison extrusion method characterized by correcting deviations in parison wall thickness control due to changes in the distance between the die exits by increasing the parison extrusion speed and conversely slowing the parison extrusion speed in thin-walled portions of the parison. . By doing this, the thick parts of the parison can be precisely made to the desired thickness, and conversely, the thin parts can be made exactly thinner by removing the swell that conventionally occurs. It is possible to make an abrupt change from a thin section to a thick section or from a thick section to a thin section over a short longitudinal distance.

また本方法を利用する装置として、 樹脂を貯留して押出すアキユーム部分とダイと
コアマンドレルとの軸線方向の相対的位置を変化
させてダイとコアとのスリツトを変化させる部分
とを有するパリスンの押出装置において、上記ダ
イとコアとのスリツトを変化させる部分が コアマンドレルを摺動させるサーボシリンダー
と コアマンドレルの位置を検出する検出器とサー
ボシリンダーを制御する弁と 弁を制御する信号を出力する制御系とより構成
され、 かつ上記アキユーム部分が 樹脂を押出すアキユームシリンダーと アキユームシリンダーのシリンダーロツドの位
置を検出する検出器と アキユームシリンダーロツドを摺動させる油圧
駆動部と 油圧駆動部を制御する弁と この弁を制御する制御系と より構成され、アキユームシリンダーロツドの位
置を検出する検出器からの信号に応じて予め設定
されたプロフアイルを与えるコントローラーがそ
れぞれプロフアイルに応じた信号をダイとコアと
のスリツトを変化させる部分の制御系とアキユー
ム部分の制御系へ入力することとしたパリスンの
押出装置。
In addition, as an apparatus using this method, there is a parison having an accumulation part for storing and extruding resin, and a part for changing the relative position of the die and core mandrel in the axial direction to change the slit between the die and the core. In the extrusion device, the part that changes the slit between the die and the core has a servo cylinder that slides the core mandrel, a detector that detects the position of the core mandrel, a valve that controls the servo cylinder, and a signal that outputs a signal that controls the valve. The above-mentioned accumulation part is composed of an accumulation cylinder that extrudes resin, a detector that detects the position of the cylinder rod of the accumulation cylinder, a hydraulic drive unit that slides the accumulation cylinder rod, and a hydraulic drive. The cylinder rod consists of a valve that controls the cylinder rod and a control system that controls the valve. A parison extrusion device in which a corresponding signal is input to the control system of the part that changes the slit between the die and the core, and the control system of the storage part.

としたことにより、ダイとコアとのスリツトを変
化させてパリスンの肉厚を制御する機構とアキユ
ームシリンダーのシリンダーロツドの摺動とを同
期させることができシリンダーロツドの摺動速度
を制御することにより肉厚を容易に制御できる。
またアキユームシリンダーを利用することにより
流速を急激にかつ敏速に反応できるのである。
By doing this, the mechanism that controls the wall thickness of the parison by changing the slit between the die and core can be synchronized with the sliding movement of the cylinder rod of the accumulation cylinder, and the sliding speed of the cylinder rod can be controlled. By doing so, the wall thickness can be easily controlled.
Also, by using an accumulation cylinder, it is possible to react rapidly and quickly to the flow rate.

実施例 本発明を図面に基づき説明する。1は押出頭、
2はアキユームレーターである。押出頭1の中心
には上下に摺動可能なシリンダーロツド7を有
し、このシリンダーロツド7の下端には円錐台状
のコア6を備え、このコア6をとりまくように押
出頭1の下端にダイ5を有する。シリンダーロツ
ド7の上方にはサーボシリンダー3を形成してシ
リンダーロツド7を上下に摺動させることができ
る。アキユームレーター2にはそのチヤンバー2
a内に溶融混練した樹脂を送り込む押出機4及び
スクリユウ8を有する。アキユームレーター2
は、チヤンバー2aの内容量を変化させるアキユ
ームシリンダーロツド9を有し、そのアキユーム
シリンダーロツト9の一方端には油圧シリンダー
10を形成してアキユームシリンダーロツド9を
摺動させる。シリンダーロツド7にはその位置を
検出する検出器11を有しシリンダーロツド7の
位置を制御系12に入力する。アキユームシリン
ダーロツド9の後端にはアキユームシリンダーロ
ツド9の位置を検出する検出器17を有しその位
置をコントローラー15へ入力する。コントロー
ラー15では予め設定された所望のプロフアイル
に従つて検出器17より入力されたアキユームシ
リンダーロツド9の位置とその比較で制御系1
2,16へ出力し、制御系12,16にて、制御
及び増巾された命令をサーボシリンダー3及び油
圧シリンダー10の油圧系統を制御する弁13,
18へ伝える。ダイ出口近傍には、パリスンの押
出速度を測定する押出速度検出手段20を有す
る。押出速度検出手段20は、マーカー21とマ
ーク検出素子22とより成り、マーカー21より
一定時間の間隔でマークを付し、マーク検出素子
22にてそのマーク通過時間を測定し、コントロ
ーラー15へフイードバツクする。
EXAMPLE The present invention will be explained based on the drawings. 1 is the extrusion head,
2 is an accumulator. At the center of the extrusion head 1 is a cylinder rod 7 that can be slid up and down, and at the lower end of the cylinder rod 7 is a truncated conical core 6. It has a die 5 at the lower end. A servo cylinder 3 is formed above the cylinder rod 7 so that the cylinder rod 7 can be slid up and down. Accumulator 2 has its chamber 2
It has an extruder 4 and a screw 8 that feed the melted and kneaded resin into the inside of a. Accumulator 2
has an accumulation cylinder rod 9 for changing the internal capacity of the chamber 2a, and a hydraulic cylinder 10 is formed at one end of the accumulation cylinder rod 9 to allow the accumulation cylinder rod 9 to slide. The cylinder rod 7 has a detector 11 for detecting its position, and the position of the cylinder rod 7 is input to a control system 12. A detector 17 for detecting the position of the accumulation cylinder rod 9 is provided at the rear end of the accumulation cylinder rod 9, and the position is inputted to the controller 15. The controller 15 compares the position of the accumulation cylinder rod 9 input from the detector 17 with the position of the accumulator rod 9 according to a preset desired profile, and controls the control system 1.
2, 16, and in the control systems 12, 16, the control and amplified commands are outputted to the valves 13, 13, which control the hydraulic systems of the servo cylinder 3 and the hydraulic cylinder 10.
Tell 18. Near the die exit, there is an extrusion speed detection means 20 for measuring the extrusion speed of the parison. The extrusion speed detection means 20 is composed of a marker 21 and a mark detection element 22, which attaches marks from the marker 21 at fixed time intervals, measures the mark passing time by the mark detection element 22, and sends the feedback to the controller 15. .

なお、押出速度検出手段20は、非接触による
検出手段を利用することも可能である。このよう
にすればパリスンにマークを打つことなく検出で
きる。
In addition, the extrusion speed detection means 20 can also utilize a non-contact detection means. In this way, the parison can be detected without marking it.

本発明の製造方法を説明する。原料供給口(図
示せず)より押出機4内に投入された合成樹脂は
スクリユウ8にて加圧供給されるにつれて加熱溶
融されチヤンバー2a内に供給され貯留される。
この時アキユームシリンダーロツド9は貯留にし
たがつて後退する。アキユームシリンダーロツド
9の位置は位置検出器17によりコントローラー
15へ入力される。樹脂がチヤンバー2a内に貯
留され、アキユームシリンダーロツド9が予め設
定された位置まで後退すると、コントローラー1
5より出力された信号により制御系16,12が
働き、弁18,13が作動する。コントローラ1
5内では、予め設定された出力のプロフアイルに
従つて信号が出力される。この信号は、アキユー
ムシリンダーロツド9の位置信号(つまりコント
ローラー15内の横向きの直線)に応じた設定プ
ロフアイル(つまり図中コントローラー15内の
波線)の高さの値が出力される。この信号に応じ
て弁18が作動し、管19aを通じて送られる油
圧が制御され、設定プロフアイルが高い値の位置
ではアキユームシリンダーロツド9の摺動速度が
速くなり、逆に設定プロフアイルが低い値を示す
位置では、アキユームシリンダーロツド9の摺動
速度が遅くなる。またこの弁18の動きと同期し
てシリンダーロツド7が作動する。このシリンダ
ーロツド7は位置検出器11でその位置を制御系
12へ絶えずフイードバツクしてコントローラー
15の設定プロフアイルの値に応じた位置を示し
ているかどうか確認しながら弁13へ信号を送
り、サーボシリンダー3を作動させる。このよう
に肉厚部分を押出す際にサーボシリンダーを作動
させてダイとコアのスリツトの間隔を広げるとと
もにアキユームシリンダーロツド9の摺動速度を
速くして合成樹脂の押出速度を速くすると、せん
断速度が高くなつてパリスンの径をより大きくす
ることができる。これを一般にスウエルと呼んで
いる。スウエルの機構について多くの研究がされ
ているが現在のところ明確に解明されていない。
一般に流動する間に受ける弾性的変形によるもの
と信じられており、実際にせん断速度の増加とと
もにスウエルが大きくなることがわかつている。
アキユームレーターによる押出速度は、急激に変
化させることが可能であるので、せん断速度の変
化によりスウエルを発生させてスリツトに対応す
るパリスンの肉厚以上の厚肉のパリスンを押出す
ことができる。そこで求めるパリスンの最高肉厚
をta最低肉厚をtbとしたときの、パリスンに肉厚
tを与えるパリスン押出速度vはパリスンが厚肉
である場合、 (つまりt>ta+tb/2) v≧{t−ta+tb/2}×vp+Vav ここで、Vavはパリスンの平均肉厚の押出時の
押出速度、vpは樹脂の粘性によつて決定される定
数である。尚押出速度は押出速度検出手段20に
より測定し、この値をコントローラー15にフイ
ートバツクして油圧シリンダー10を制御する。
The manufacturing method of the present invention will be explained. The synthetic resin introduced into the extruder 4 through a raw material supply port (not shown) is supplied under pressure by the screw 8, heated and melted, and supplied into the chamber 2a and stored therein.
At this time, the storage cylinder rod 9 moves back as the water is stored. The position of the accumulation cylinder rod 9 is input to the controller 15 by a position detector 17. When the resin is stored in the chamber 2a and the storage cylinder rod 9 is retracted to a preset position, the controller 1
Control systems 16 and 12 are actuated by the signal output from 5, and valves 18 and 13 are actuated. controller 1
5, a signal is output according to a preset output profile. This signal outputs the height value of the set profile (ie, the wavy line inside the controller 15 in the figure) according to the position signal of the accumulation cylinder rod 9 (ie, the horizontal straight line inside the controller 15). In response to this signal, the valve 18 is actuated to control the hydraulic pressure sent through the pipe 19a, and the sliding speed of the accumulation cylinder rod 9 becomes faster at the position where the setting profile is high, and conversely when the setting profile is high. At a position where the value is low, the sliding speed of the accumulation cylinder rod 9 becomes slow. Furthermore, the cylinder rod 7 operates in synchronization with the movement of the valve 18. This cylinder rod 7 constantly feeds back its position to the control system 12 using a position detector 11, and sends a signal to the valve 13 while checking whether the position corresponds to the value of the setting profile of the controller 15. Activate cylinder 3. In this way, when extruding a thick part, the servo cylinder is operated to widen the gap between the die and the core slit, and the sliding speed of the accumulation cylinder rod 9 is increased to increase the extrusion speed of the synthetic resin. The higher the shear rate, the larger the diameter of the parison. This is generally called a swell. Although much research has been carried out on the mechanism of swell, it has not been clearly elucidated at present.
It is generally believed that this is due to the elastic deformation experienced during flow, and it has been found that swell actually increases as the shear rate increases.
Since the extrusion speed by the accumulator can be changed rapidly, a swell can be generated by changing the shear rate, and a thicker parison can be extruded than the thickness of the parison corresponding to the slit. When the maximum wall thickness of the parison to be determined is t and the minimum wall thickness is t b , the parison extrusion speed v that gives the parison the wall thickness t is as follows: (In other words, t > t a + t b / 2) v≧{t-t a +t b /2}×v p +V av Here, V av is the extrusion speed during extrusion of the average wall thickness of the parison, and v p is a constant determined by the viscosity of the resin. It is. The extrusion speed is measured by the extrusion speed detection means 20, and this value is fed back to the controller 15 to control the hydraulic cylinder 10.

以上は、パリスンが厚肉の場合について述べた
が、次にパリスンが薄肉の場合について述べる。
スウエルは、同じ流速の場合、スリツトの断面積
の変化によつても発生する。流速を一定にしても
スリツトが小さくなつたことによりパリスンの肉
厚を抑えることはできず、パリスンの肉厚を急激
に薄肉化させる場合の障害となつていた。実施例
は、スウエルが発生しないように、あるいはさら
に進んで逆スウエル(ダイとコアで形成されたス
リツト形状よりも小さいパリスンを押出すこと)
を形成させるものである。このときのパリスンの
押出速度vは、 (つまりt<ta+tb/2のとき) v≦Vav+(t−ta+tb/2)×vp で与えられる。
The case where the parison is thick has been described above, but next, the case where the parison is thin will be described.
Swell also occurs due to a change in the cross-sectional area of the slit at the same flow rate. Even if the flow velocity was kept constant, the thickness of the parison could not be suppressed due to the smaller slit, which was an obstacle to rapidly reducing the thickness of the parison. Examples include preventing swell from occurring or even going further to prevent reverse swell (extruding a parison smaller than the slit shape formed by the die and core).
is formed. The parison extrusion speed v at this time is given by v≦V av + (t−t a +t b /2)×vp (that is, when t<t a +t b /2).

このような押出しを行うと、スウエルが必要な
厚肉部分はスウエルが得られ、逆にスウエルが発
生するために肉厚制御を阻害されていた薄肉部分
ではスウエルを抑さえあるいは逆スウエルにより
逆に薄肉化がはかられるという特別の効果を期待
することができる。
When such extrusion is performed, swell can be obtained in thick-walled areas that require swell, and conversely, swell can be suppressed or reversed in thin-walled areas where wall thickness control has been inhibited due to swell. A special effect of thinning can be expected.

発明の効果 本発明方法によれば、ダイ出口付近の押出速度
をパリスンの厚肉部分ではパリスンの押出し速度
を速くし、逆にパリスンの薄肉部分ではパリスン
の押出し速度を遅くするという制御をするのでパ
リスン全体として1シヨツト、1シヨツト1各に
重量を均一にできるばかりでなくスリツトの変化
にともなう押出速度の変化により発生していた肉
厚のバラツキに対応できる。さらに特に厚肉部分
と薄肉部分を正確に押出すことが可能となつた。
Effects of the Invention According to the method of the present invention, the extrusion speed near the die exit is controlled such that the extrusion speed of the parison is increased in the thick portion of the parison, and conversely, the extrusion speed of the parison is decreased in the thin portion of the parison. Not only can the weight of the parison as a whole be made uniform for each shot, but also it is possible to cope with variations in wall thickness caused by changes in extrusion speed due to changes in the slit. Furthermore, it has become possible to extrude particularly thick and thin parts accurately.

本発明装置によれば、アキユームシリンダーロ
ツドにより押出すので押出速度を急激に変化させ
あるいは制御することが可能である。ダイとコア
とのスリツトの変化による合成樹脂の流速の変化
を、スリツトの変化と同期して改善できるのでパ
リスンの肉厚を正確にかつ短時間で変えることが
可能である。
According to the apparatus of the present invention, since extrusion is performed using an accumulation cylinder rod, it is possible to rapidly change or control the extrusion speed. Changes in the flow velocity of the synthetic resin due to changes in the slits between the die and core can be improved in synchronization with changes in the slits, making it possible to change the thickness of the parison accurately and in a short time.

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

第1図は本発明の実施例に係る説明図、第2図
は本発明により得られたパリスンの一部断面図で
ある。 1……押出頭、2……アキユームレーター、3
……サーボシリンダー、5……ダイ、6……コ
ア、7……シリンダーロツド、9……アキユーム
シリンダーロツド、10……油圧シリンダー、1
1,17……位置検出器、12,16……制御
系、13,18……弁、15……コントローラ
ー、20……押出速度検出手段。
FIG. 1 is an explanatory diagram of an embodiment of the present invention, and FIG. 2 is a partial sectional view of a parison obtained by the present invention. 1... Extrusion head, 2... Accumulator, 3
... Servo cylinder, 5 ... Die, 6 ... Core, 7 ... Cylinder rod, 9 ... Acquisition cylinder rod, 10 ... Hydraulic cylinder, 1
1, 17... position detector, 12, 16... control system, 13, 18... valve, 15... controller, 20... extrusion speed detection means.

Claims (1)

【特許請求の範囲】 1 ダイ出口の間〓を変化させて押出すパリスン
の肉厚を制御するパリスンの押出方法において、
パリスンの厚肉部分ではパリスンの押出し速度を
速くし、逆にパリスンの薄肉部分ではパリスンの
押出し速度を遅くすることにより、前記ダイ出口
の間〓の変化によるパリスンの肉厚制御のずれを
補正することを特徴とするパリスンの押出方法。 2 樹脂を貯留して押出すアクキユーム部分とダ
イとコアマンドレルとを軸線方向の相対的位置を
変化させてダイとコアとのスリツトを変化させる
部分とを有するパリスンの押出装置において、 上記ダイとコアとのスリツトを変化させる部分
が コアマンドレルを摺動させるサーボシリンダー
と コアマンドレルの位置を検出する検出器とサー
ボシリンダーを制御する弁と 弁を制御する信号を出力する制御系と より構成され、 かつ上記アキユーム部分が 樹脂を押出すアキユームシリンダーと アキユームシリンダーのシリンダーロツドの位
置を検出する検出器と アキユームシリンダーロツドを摺動させる油圧
駆動部と 油圧駆動部を制御する弁と この弁を制御する制御系と より構成され、アキユームシリンダーロツドの位
置を検出する検出器からの信号に応じ予め設定さ
れたプロフアイルを与えるコントローラーがそれ
ぞれプロフアイルに応じた信号をダイとコアとの
スリツトを変化させる部分の制御系とアキユーム
部分の制御系へ入力することを特徴とするパリス
ンの押出装置。
[Claims] 1. A method for extruding a parison in which the wall thickness of the extruded parison is controlled by changing the distance between the die exits,
By increasing the extrusion speed of the parison in the thick part of the parison and slowing down the extrusion speed of the parison in the thin part of the parison, the deviation in the control of the thickness of the parison due to the change in the distance between the die exits is corrected. A parison extrusion method characterized by: 2. A parison extrusion device having an accumulation part for storing and extruding resin, and a part for changing the relative position of the die and core mandrel in the axial direction to change the slit between the die and the core. The part that changes the slit of the core mandrel is composed of a servo cylinder that slides the core mandrel, a detector that detects the position of the core mandrel, a valve that controls the servo cylinder, and a control system that outputs a signal that controls the valve, and The above accumulation part includes an accumulation cylinder that extrudes resin, a detector that detects the position of the cylinder rod of the accumulation cylinder, a hydraulic drive unit that slides the accumulation cylinder rod, a valve that controls the hydraulic drive unit, and this valve. The controller provides a preset profile according to the signal from the detector that detects the position of the accumulation cylinder rod, and the controller sends a signal corresponding to the profile to the die and core. A parison extrusion device characterized by input to a control system for a part that changes the slit and a control system for an accumulation part.
JP60215957A 1985-09-28 1985-09-28 Method of extruding parison and its device Granted JPS62202712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60215957A JPS62202712A (en) 1985-09-28 1985-09-28 Method of extruding parison and its device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60215957A JPS62202712A (en) 1985-09-28 1985-09-28 Method of extruding parison and its device

Publications (2)

Publication Number Publication Date
JPS62202712A JPS62202712A (en) 1987-09-07
JPH0460405B2 true JPH0460405B2 (en) 1992-09-28

Family

ID=16681042

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60215957A Granted JPS62202712A (en) 1985-09-28 1985-09-28 Method of extruding parison and its device

Country Status (1)

Country Link
JP (1) JPS62202712A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2798160B2 (en) * 1991-06-07 1998-09-17 宇部興産株式会社 Blow molding machine
JP3669116B2 (en) * 1997-06-25 2005-07-06 東洋製罐株式会社 Method and apparatus for controlling wall thickness of parison
US7179073B2 (en) * 2003-03-04 2007-02-20 Davis-Standard, Llc Pressure-reducing valve and a controller for a blow-molding machine and method thereof
JP4511492B2 (en) * 2006-05-11 2010-07-28 株式会社タハラ Blow molding method
DE102012112110A1 (en) 2012-12-11 2014-06-12 Kautex Maschinenbau Gmbh Extrusion blow molding and apparatus for its implementation

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5842437A (en) * 1981-09-08 1983-03-11 Ishikawajima Harima Heavy Ind Co Ltd Method of controlling distribution of sectional area of parison for blow molding

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5842437A (en) * 1981-09-08 1983-03-11 Ishikawajima Harima Heavy Ind Co Ltd Method of controlling distribution of sectional area of parison for blow molding

Also Published As

Publication number Publication date
JPS62202712A (en) 1987-09-07

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