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JPS6134972B2 - - Google Patents
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JPS6134972B2 - - Google Patents

Info

Publication number
JPS6134972B2
JPS6134972B2 JP53108382A JP10838278A JPS6134972B2 JP S6134972 B2 JPS6134972 B2 JP S6134972B2 JP 53108382 A JP53108382 A JP 53108382A JP 10838278 A JP10838278 A JP 10838278A JP S6134972 B2 JPS6134972 B2 JP S6134972B2
Authority
JP
Japan
Prior art keywords
inside mandrel
mandrel
sizing
heat insulating
molding
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
JP53108382A
Other languages
Japanese (ja)
Other versions
JPS5534952A (en
Inventor
Masataka Sakurada
Nobuyuki Iwazawa
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.)
Toppan Inc
Original Assignee
Toppan Printing 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 Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP10838278A priority Critical patent/JPS5534952A/en
Publication of JPS5534952A publication Critical patent/JPS5534952A/en
Publication of JPS6134972B2 publication Critical patent/JPS6134972B2/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
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
    • B29C48/908Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article characterised by calibrator surface, e.g. structure or holes for lubrication, cooling or venting
    • 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
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
    • B29C48/901Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
    • B29C48/902Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies internally
    • 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)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 本発明はパイプ等の中空プロフアイルの製造方
法に関するものであり、従来のインサイドマンド
レルサイジング法により内径規制でパイプ等の中
空プロフアイルの押出成形を行う場合、長期間成
形時にインサイドマンドレルの表面に成形樹脂中
の低分子量成分、添加剤成分あるいはモノマーが
析出し、サイジング不良の原因となる。すなわち
第1図に示すように従来中空プロフアイルの押出
成形において、インサイドマンドレルサイジング
法は冷却されたインサイドマンドレル1の表面に
溶融樹脂を接触、冷却、固化、サイズ及び形状を
規制するものであり、この成形開始においては、
ダイ12′及びコア9′の先端、すなわちリツプ1
4′と称するところからインサイドマンドレル
3′に接する距離は変化しやすい。その為、一般
には通常製造している状態ではインサイドマンド
レル3′とリツプ14′との距離がゼロ又は、かな
り少な目になつているので、溶融樹脂と接触しな
いインサイドマンドレル3′の表面のダイ12′近
くに露出部分が生じ、この露出部分11′は冷却
により、コア13′とインサイドマンドレル3′と
の間に生じた低分子量成分、モノマーあるいは添
加成分率が露出部分11′に析出し、この析出物
の量が次第に多く貯つてくると溶融樹脂とインサ
イドマンドレル3′の隙間に入り、その為にその
部分が厚肉になつたり、溶融樹脂が流れなくなつ
て肉厚の変化が大きくなると共に場合によつて
は、成形(又は樹脂)が完全に止まつて成形品が
切れてしまうという現象が発生する。この対策と
して、低分子量成分やモノマー及び揮発成分の少
ない樹脂を使用することが考えられるが、析出物
を完全になくすことは下可能であり、選択樹脂が
限られてしまい、この析出量は低密度ポリエチレ
ンで2〜100ppm程度であり、その他、共重合樹
脂においては500ppmを、越えるものもある。又
他の対策として、ベント式押出し機や溶剤等で取
り除く方法を用いても2〜10ppm程度の析出物
は残つてしまい、サイジング不良が発生するとい
う問題点がある。 本発明はこのようなサイジング不良という問題
を装置的に解決したものであり、以下図面を用い
て詳細に説明する。 第2図は本発明の成形システムを示す概略図で
あり、溶融樹脂は押出し機1から押し出され、ダ
イヘツド2を通り、インサイドマンドレル3の表
面で冷却され、固化し形状及びサイズが規制さ
れ、中空プロフアイル4として引取機5により引
き取られるシステムである。図面において、6は
インサイドマンドレル3の冷却するための冷却水
を供給する冷却管であり、7はその冷却水の排出
用の冷却管であり、8は揮発成分を排出するエア
管である。 本発明は上記成形システムにおいて第3図に示
すように該インサイドマンドレル3とダイヘツド
2内のコア9との間にインサイドマンドレル3と
の間に間隙及び段差が生じないように断熱固定リ
ング10を設けることにより、インサイドマンド
レル3の内溶融樹脂が接していない部分、すなわ
ち露出部分11を極力少なくしたものである。 その離す量すなわち露出部分11は、成形速
度、成形温度、インサイドマンドレル3の材質及
び肉厚、太さ等により異なるが、インサイドマン
ドレル3の熱伝導性が良い程、又インサイドマン
ドレルの肉厚が薄い程、短くする必要があり、例
えばインサイドマンドレル3の材料として黄銅を
用いるときは、0〜15mmの範囲が良く、好ましく
は3〜5mmにおさえることが望ましい。又断熱固
定リング10の長さは予めダイヘツド2のダイ1
2及びコア9の先端であるリツプ13より出た溶
融樹脂がインサイドマンドレル3に接する点S
(以下サイジング開始点Sという。)を正確に知つ
ておき、理想的には上記のようにインサイドマン
ドレル3の露出部分11の量はゼロであるが、こ
の露出部分11を数mmとし、コア9からサイジン
グ開始点Sの距離を引いた長さが断熱固定リング
10の長さとする。 ここで、断熱固定リング10の材質としては熱
伝導性が小さく、耐熱性があり加工しやすいポリ
4フツ化エチレン等が良く、この断熱固定リング
10は図面に示すように冷却管6を被うように取
り付けられ、溶融樹脂に接触しないようにするこ
とが好ましい。 次にインサイドマンドレル3のサイジング開始
点S付近は第4図に示すように肉厚を薄くするこ
とにより冷却し易くすることが好ましい。 さらにインサイドマンドレル3を冷却するため
冷却管6もタイヘツド2内部においては断熱材を
巻き、ダイヘツド2内の冷却管6に析出物が凝結
したり、落下しないようにすることが好ましい。
ここで断熱材としては成形温度により安定してい
る熱伝導率の低く、成形温度により変形しないも
のであれば良く、フツ化樹脂、石綿セメント材、
磁器、ガラス繊維板等が使用できる。 本発明は以上のような製造方法であり、サイジ
ング開始点とダイヘツドとの間に、インサイドマ
ンドレルとの間に間隙及び段差が生じないように
断熱固定リングを設けたことにより、インサイド
マンドレルのサイジング開始点とダイヘツドの間
に発生した溶融樹脂中の低分子量成分、未反応成
分、添加物等の揮発成分は凝結する事がなくサイ
ジング不良を起こすことがなく、また、サイジン
グ開始点まで位置規制し易く、成形性が優れてい
る。 又、成形開始時には、ヘツドからの伝導熱ある
いはパリソンからの放射熱がないので断熱固定リ
ングも冷えており、たとえ樹脂が接触しても付着
しにくく、仮りに付着しても容易に離す事ができ
るので容易に成形することが可能である。したが
つて本発明の装置により従来収率が97〜98%であ
つたものが99.8%程度に上昇した。 以下本発明の実施例を示す。 実施例 樹脂として低密度ポリエチレン(MI=1.0、d
=0.91)を使用し、成形速度:6m/m、平均肉
厚420μの条件で、ダイ内径42φ、コア外径40φ
で黄銅製30φパイプ用のインサイドマンドレルを
使用して下記の如き結果を得た。 【表】
Detailed Description of the Invention The present invention relates to a method for manufacturing hollow profiles such as pipes, etc. When extrusion molding hollow profiles such as pipes with internal diameter regulation using the conventional inside mandrel sizing method, long-term molding is required. Sometimes, low molecular weight components, additive components, or monomers in the molding resin precipitate on the surface of the inside mandrel, causing poor sizing. That is, as shown in FIG. 1, in the conventional extrusion molding of hollow profiles, the inside mandrel sizing method involves bringing a molten resin into contact with the surface of a cooled inside mandrel 1, cooling it, solidifying it, and regulating the size and shape. At the start of this molding,
The tips of the die 12' and the core 9', that is, the lip 1
The distance from a point called 4' to the inside mandrel 3' is easy to change. Therefore, in general, in normal manufacturing conditions, the distance between the inside mandrel 3' and the lip 14' is zero or very small, so the die 12' on the surface of the inside mandrel 3' that does not come into contact with the molten resin. An exposed portion is formed nearby, and when this exposed portion 11' is cooled, low molecular weight components, monomers, or additive components generated between the core 13' and the inside mandrel 3' are precipitated on the exposed portion 11', and this precipitation As the amount of material gradually accumulates, it enters the gap between the molten resin and the inside mandrel 3', resulting in a thick wall in that area, or the molten resin stops flowing, resulting in a large change in wall thickness and In some cases, the molding (or resin) stops completely and the molded product breaks. As a countermeasure to this, it is possible to use resins with low molecular weight components, monomers, and volatile components, but it is not possible to completely eliminate the precipitates, and the selection of resins is limited, and the amount of precipitates is low. The content of density polyethylene is about 2 to 100 ppm, and some copolymer resins exceed 500 ppm. As another countermeasure, even if a method of removing the precipitate using a vent type extruder or a solvent is used, about 2 to 10 ppm of precipitates remain, resulting in a problem of sizing defects. The present invention solves the problem of such sizing defects in terms of equipment, and will be described in detail below with reference to the drawings. FIG. 2 is a schematic diagram showing the molding system of the present invention, in which the molten resin is extruded from the extruder 1, passes through the die head 2, is cooled on the surface of the inside mandrel 3, solidifies, and regulates the shape and size. This is a system in which the profile 4 is collected by a collection machine 5. In the drawing, 6 is a cooling pipe for supplying cooling water for cooling the inside mandrel 3, 7 is a cooling pipe for discharging the cooling water, and 8 is an air pipe for discharging volatile components. As shown in FIG. 3 in the above molding system, the present invention provides a heat insulating fixing ring 10 between the inside mandrel 3 and the core 9 in the die head 2 so that no gap or step is created between the inside mandrel 3 and the inside mandrel 3. As a result, the portion of the inside mandrel 3 that is not in contact with the molten resin, that is, the exposed portion 11 is minimized. The amount of separation, that is, the exposed portion 11, varies depending on the molding speed, molding temperature, material, wall thickness, thickness, etc. of the inside mandrel 3, but the better the thermal conductivity of the inside mandrel 3, the thinner the wall thickness of the inside mandrel. For example, when brass is used as the material for the inside mandrel 3, it is preferably in the range of 0 to 15 mm, preferably 3 to 5 mm. Also, the length of the heat insulating fixing ring 10 is determined in advance from the die 1 of the die head 2.
2 and the point S where the molten resin coming out from the lip 13 which is the tip of the core 9 contacts the inside mandrel 3
(hereinafter referred to as the sizing starting point S). Ideally, the amount of the exposed portion 11 of the inside mandrel 3 is zero as described above, but this exposed portion 11 is set to several mm, and the core 9 The length obtained by subtracting the distance from the sizing start point S is the length of the heat insulating fixing ring 10. Here, a good material for the heat insulating fixing ring 10 is polytetrafluoroethylene, which has low thermal conductivity, heat resistance, and is easy to process.This heat insulating fixing ring 10 covers the cooling pipe 6 as shown in the drawing. It is preferable to attach it so that it does not come into contact with the molten resin. Next, it is preferable that the inside mandrel 3 near the sizing start point S be made thinner to facilitate cooling as shown in FIG. Furthermore, in order to cool the inside mandrel 3, it is preferable that the cooling pipe 6 is also wrapped with a heat insulating material inside the tie head 2 to prevent precipitates from condensing or falling on the cooling pipe 6 inside the die head 2.
Here, the heat insulating material may be any material with low thermal conductivity that is stable depending on the molding temperature and does not deform due to the molding temperature, such as fluoride resin, asbestos cement material, etc.
Porcelain, glass fiber board, etc. can be used. The present invention is a manufacturing method as described above, in which a heat insulating fixing ring is provided between the sizing start point and the die head to prevent a gap or step from occurring between the inside mandrel and the inside mandrel. Volatile components such as low molecular weight components, unreacted components, and additives in the molten resin generated between the point and the die head do not condense and cause sizing defects, and it is easy to control the position up to the sizing starting point. , excellent moldability. Furthermore, at the start of molding, there is no conductive heat from the head or radiant heat from the parison, so the heat insulating fixing ring is also cold, so even if the resin comes into contact with it, it is unlikely to stick, and even if it does, it will be easy to separate. Therefore, it can be easily molded. Therefore, with the apparatus of the present invention, the conventional yield of 97 to 98% was increased to about 99.8%. Examples of the present invention will be shown below. Example Low density polyethylene (MI=1.0, d
= 0.91), molding speed: 6m/m, average wall thickness 420μ, die inner diameter 42φ, core outer diameter 40φ
Using an inside mandrel for a 30φ brass pipe, I obtained the following results. 【table】

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

第1図は従来の中空プロフアイルの製造方法を
示す概略図であり、第2図は本発明の成形システ
ムを示す概略図であり、第3図は本発明の一実施
例を示す概略図であり、第4図は他の実施例を示
す製造方法を示す概略図である。 1…押出し機、2…ダイヘツド、3,3′…イ
ンサイドマンドレル、4…中空プロフアイル、5
…引取機、6…冷却管、7…排出用の冷却管、8
…エア管、9,9′…コア、10…断熱固定リン
グ、11,11′…露出部分、12,12′…ダ
イ、13,13′…リツプ、S…サイジング開始
点。
FIG. 1 is a schematic diagram showing a conventional hollow profile manufacturing method, FIG. 2 is a schematic diagram showing a molding system of the present invention, and FIG. 3 is a schematic diagram showing an embodiment of the present invention. 4 is a schematic diagram showing a manufacturing method showing another embodiment. 1... Extruder, 2... Die head, 3, 3'... Inside mandrel, 4... Hollow profile, 5
...Taking machine, 6...Cooling pipe, 7...Discharge cooling pipe, 8
...Air pipe, 9,9'...Core, 10...Insulating fixing ring, 11,11'...Exposed portion, 12,12'...Die, 13,13'...Rip, S...Sizing starting point.

Claims (1)

【特許請求の範囲】[Claims] 1 内径を規制するインサイドマンドレルサイジ
ング法を使用して、中空プロフアイルを製造する
方法において、インサイドマンドレルとダイヘツ
ドの間に、インサイドマンドレルとの間に間隙及
び段差が生じないように断熱固定リングから成る
断熱材を設け、インサイドマンドレルの露出部分
を少なくしたことを特徴とする中空プロフアイル
の製造方法。
1 In a method of manufacturing a hollow profile using the inside mandrel sizing method that regulates the inside diameter, a heat insulating fixing ring is provided between the inside mandrel and the die head to prevent gaps and steps from forming between the inside mandrel and the die head. A method for manufacturing a hollow profile characterized by providing a heat insulating material and reducing the exposed portion of the inside mandrel.
JP10838278A 1978-09-04 1978-09-04 Method of manufacturing a hollow profile Granted JPS5534952A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10838278A JPS5534952A (en) 1978-09-04 1978-09-04 Method of manufacturing a hollow profile

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10838278A JPS5534952A (en) 1978-09-04 1978-09-04 Method of manufacturing a hollow profile

Publications (2)

Publication Number Publication Date
JPS5534952A JPS5534952A (en) 1980-03-11
JPS6134972B2 true JPS6134972B2 (en) 1986-08-11

Family

ID=14483346

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10838278A Granted JPS5534952A (en) 1978-09-04 1978-09-04 Method of manufacturing a hollow profile

Country Status (1)

Country Link
JP (1) JPS5534952A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5798328A (en) * 1980-12-12 1982-06-18 Toppan Printing Co Ltd Manufacture of tubular vessel
TW254883B (en) * 1991-04-03 1995-08-21 Mitsui Petroleum Chemicals Ind

Also Published As

Publication number Publication date
JPS5534952A (en) 1980-03-11

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