JPS585225A - Method of molding orientated form - Google Patents

Method of molding orientated form

Info

Publication number
JPS585225A
JPS585225A JP56103171A JP10317181A JPS585225A JP S585225 A JPS585225 A JP S585225A JP 56103171 A JP56103171 A JP 56103171A JP 10317181 A JP10317181 A JP 10317181A JP S585225 A JPS585225 A JP S585225A
Authority
JP
Japan
Prior art keywords
die
lubricant
molded body
oriented
temperature
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.)
Granted
Application number
JP56103171A
Other languages
Japanese (ja)
Other versions
JPH0258093B2 (en
Inventor
Hiroshi Kataoka
片岡 紘
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.)
Asahi Dow Ltd
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Dow Ltd
Asahi Chemical Industry 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 Asahi Dow Ltd, Asahi Chemical Industry Co Ltd filed Critical Asahi Dow Ltd
Priority to JP56103171A priority Critical patent/JPS585225A/en
Publication of JPS585225A publication Critical patent/JPS585225A/en
Publication of JPH0258093B2 publication Critical patent/JPH0258093B2/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
    • B29C48/94Lubricating
    • 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
    • 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
    • B29C48/07Flat, e.g. panels
    • 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
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • 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

Abstract

PURPOSE:To mold an orientated form, by extruding or stretching a molded body of a thermoplastic resin having a temperature between the glass transition temperature or above and the melting point or below within a die to which a lubricant has been applied, during which time the molded body is in contact with the die. CONSTITUTION:A thermoplastic resin that has been heated and plasticized in an extrusion molder 1 is molded into a thick molded body at a section A of the die 2, and is cooled to a temperature between the glass transition temperature or above and the melting point or below. A lubricant is delivered through a lubricant introducing passage 3 to openings 4 to go to the surface of the resin molded body so that it is applied to the interface between the molded body surface and the die surface. The molded body is rolled at a section B of the die to be biaxially orientated. Thus, it can readily be molded into a thick walled orientated item.

Description

【発明の詳細な説明】 本発明は熱可塑性樹脂の配向成形品の成形法に係る。[Detailed description of the invention] The present invention relates to a method of molding an oriented molded article of thermoplastic resin.

熱可塑性樹脂の2軸配向された板状成形品は、一般には
1mm厚以下のシートとして製造されている、1mm厚
以下の2軸配向シートは、押出成形した原反シートを連
続的に逐次あるいは同時に2軸に引張ることにより容易
に製造できる。しかし、1mm厚以上の2軸配向シート
は容易に製造できない。製造方法も米■1・雪4−マ$
勢にわずかに示されて−るにす1*hし、そO11造方
法も複雑であp、改嵐された製造W&が要求されている
Biaxially oriented plate-shaped molded thermoplastic resin products are generally manufactured as sheets with a thickness of 1 mm or less. Biaxially oriented sheets with a thickness of 1 mm or less are manufactured by continuously or sequentially extruding original fabric sheets. It can be easily produced by simultaneously pulling it in two axes. However, biaxially oriented sheets with a thickness of 1 mm or more cannot be easily manufactured. The manufacturing method is rice ■1, snow 4-ma$
However, the manufacturing method is complicated and requires modified manufacturing methods.

!軸配向され曳熱可麿性樹脂シートa、無配向シートに
比べ、物罵釣性質及び化学的性質0着るしい向上がある
。41Kli隼強度O肉上が着るし−。
! The axially oriented thermoplastic resin sheet a has significantly improved physical properties and chemical properties compared to a non-oriented sheet. 41Kli Hayabusa strength O meat top is worn.

3軸配崗され九熱可閣性樹脂OII状腫物は従来。The three-axis granite and nine-thermal resin OII-shaped tumor is conventional.

米1Be 意41マ畠等に示されて−る橡な、!軸に引
張って製造され九1軸配向クートから[出して製造され
てh−〉、そOJl造01[雑さ、製造コストO高さ等
多(O問題点を含んでいる0本発明はこれ等O問題点を
鋳決し良−〇である。
Rice 1Be I mean 41 Mahatake et al.'s mistake! It is manufactured by pulling it on the shaft and manufactured by pulling it out from the 91 axially oriented coupe. etc. O Problems have been resolved and it is good.

本発−は熱可履性樹脂Oガ2ス転位温度以上。The thermoplastic resin has a temperature higher than the O gas transition temperature.

溶融点温度以下の成形体を、潤滑剤が塗布畜れ良ダイ内
で、グイと接触しつつ押出し、あるいは及び引張ること
により分子配向させることを41111とする配向成形
品の成形法である。
41111 is a method for forming an oriented molded product, in which a molded product having a temperature below its melting point is extruded or stretched in a well-coated die coated with a lubricant, while being in contact with a gooey, or by pulling the molded product to orient its molecules.

本発明を図面により説明する。The present invention will be explained with reference to the drawings.

第1図は本発明の方法によ)電輪配向シートを成形する
装置を示す。第1園Klkて、押出成形機1で加熱可塑
化され九熱可■性樹脂紘ダイ雪Oム部分で一定の厚肉成
形体にされ、ガラス転位温度以上、溶融点温度以下01
11に冷却畜れる。グイ窓の人部分では樹脂を冷却する
丸め冷却されてシシ、樹脂をは埋均−に冷却するためO
長さが&費である。更に大部分O通中に、厚肉成形体o
hmとダイ表wO界面に潤滑剤をamするため、潤滑剤
を浸み出す一連O装置を有する。高圧力O―滑滑剤温潤
滑剤導入路よ多複数の没み出し口4へ導びかれ、樹脂成
形体IIwへ浸み出し、成形体IImとメイ表IIO界
mに潤滑剤をIklsする。
FIG. 1 shows an apparatus for forming an electric wheel orientation sheet (by the method of the present invention). In the first garden, it is heated and plasticized in an extrusion molding machine 1, and made into a molded body with a constant thickness in the thermoplastic resin part, which is above the glass transition temperature and below the melting point temperature.
Refrigerate to 11. In the main part of the window, the resin is cooled in a round shape, and the resin is buried evenly in O2.
The length is & cost. Furthermore, most of the thick-walled molded body o
In order to apply lubricant to the hm and die surface wO interfaces, a series O device is provided to ooze out the lubricant. The high-pressure O-lubricant temperature lubricant introduction path leads to a plurality of seepage ports 4, seeps into the resin molded body IIw, and applies the lubricant Ikls to the molded body IIm and the interface IIO m.

潤滑剤O浸み出し口4紘小さなスシット状、あるいは焼
結金属尋の黴細な連通孔を有する物質でできてお夛、そ
の微細孔より潤滑剤が授与出る。
The lubricant O seepage port 4 is made of a substance with small slit-like or sintered metal holes that have fine communication holes, and the lubricant comes out from the fine holes.

ガラス転位温度以上、溶融点温度以下O温度に冷却され
5表層1に潤滑剤が均−KIkmi[れ九樹庸成形体紘
、グイ内で成形体表層、内核がは!同速度で流動する。
It is cooled to a temperature above the glass transition temperature and below the melting point temperature, and the lubricant is uniformly applied to the surface layer 1 of the molded body. Flow at the same speed.

いわゆるプラグフローになる。次にダイ01部分で、プ
ラグフローOt形体を圧延しして3軸配向させる。グイ
OB部分社樹脂の厚さが小さくなる構造を有する。B部
分O成形体O流動変化を第鵞11に示し良。成形体はプ
ラグフローのま\流動方向、及びその直角方向に同時に
重輪方向に圧JI!され寓軸配肉される。成形体を圧延
する力は押出成形機よ)押出す力によシ行われる。
This results in what is called a plug flow. Next, in the die 01 portion, the plug flow Ot shape is rolled and triaxially oriented. Gui OB Part has a structure in which the thickness of the resin is reduced. The flow change of the molded body O in part B is shown in number 11. The molded body continues to flow in the plug flow direction, and at the same time in the direction perpendicular to the flow direction, in the direction of the heavy wheel! The story is fleshed out. The force for rolling the molded body is exerted by the force of extrusion (from an extrusion molding machine).

!軸配肉畜れ大成形体はダイ00部分で更に冷却され、
好ましくはガラス転位温度以下にまで冷却されてダイ意
を出る。必1FK応じて冷水2等で更に冷却され、引取
)w−ル6で引取られて意軸配肉シーシとなる。重輪配
向シートは更に適11jK加熱された艶付はリール勢に
より艶付けされ、良好な重輪配向シートとなる。
! The shaft-oriented meat large molded body is further cooled in the die 00 part,
Preferably, the die is cooled to below the glass transition temperature before exiting the die. If necessary, it is further cooled with cold water 2 or the like, and then taken out by a wheel 6 to become a sheath with arbitrary thickness distribution. The heavy wheel oriented sheet is further polished by heating at 11JK using a reel, resulting in a good double wheel oriented sheet.

本発明は、熱可■性樹脂Oガ2ス転位温度以上。In the present invention, the thermoplastic resin has a temperature higher than the O gas transition temperature.

溶融点以下O成形体を、潤滑剤がm廖されえグイ内で、
グイと接触しクク押出し、ああ−は及び引張ることKよ
り分子配向させる仁とを轡徴とする配向成形&の成形法
であり1本発明方法紘第1IIOダイのB部分に於ゆる
成形状態を示す0分子配向は1軸配向でも喪い。配向は
、適度な粘WIO樹脂を圧延して行われるが、圧延状樹
脂を押し出す力、あるいは及び引張る力によ)行われる
。押し出す力は第1図に示す押出機O押出し力で行われ
る場會41り、あるいはあらかじめ成形され、適度な温
度に調整され大成形体をme機械力v′c稈し出す、パ
ッチ式成形法も使用でlる。潤滑剤am脂威形体表面に
均−Klk布す為ことが好ましく、潤滑剤を樹脂成形体
とダイ*imo界画に連続的に吐出することKより達成
できる。
The O molded body below the melting point is placed in a container where lubricant is applied.
It is an oriented molding & molding method in which the extrusion is brought into contact with the material, and the molecular orientation is caused by pulling. The zero molecular orientation shown is also absent even in uniaxial orientation. Orientation is carried out by rolling a moderately viscous WIO resin (by means of extrusion force or pulling force) on the rolled resin. The extrusion force is applied using the extrusion force of the extruder shown in Figure 1, or there is also a patch-type molding method in which the large molded product is pre-formed, adjusted to an appropriate temperature, and then extruded through a mechanical force. It will be used. It is preferable to spread the lubricant evenly over the surface of the molded body, and this can be achieved by continuously discharging the lubricant onto the resin molded body and the die area.

第3図は同様の方法によ少パイプを成形する方法を示す
、第3図に於て、押出機1で加熱可■化された熱可塑性
樹脂はダイマOD部分で一定O厚肉パイグ状にされ%ガ
ラス転位温度以上 S融点温度以下の温度に冷却される
。メイマOD部分紘*iitを冷却するため冷却されて
お〕、樹脂をはソ均一に冷却する良めO長さが必要であ
る。更[D部分O途中に、厚内パイプの表両とグイ表面
の界IIK潤滑剤を塗布するため潤滑剤を浸み出す一連
O装置を有する。パイプO外*W、内表面のいずれKも
潤滑剤を塗布する。高圧力の潤滑剛線潤滑剤導入路$よ
り、パイプの外表面、内嵌@0複数の浸み出しローへ導
びかれ、パイプ表面へ浸み出し、パイプとグイ11面の
界面に潤滑剤を塗布する。
Fig. 3 shows a method of forming a small pipe using the same method. It is cooled to a temperature above the glass transition temperature and below the S melting point temperature. The resin is cooled to cool down the resin, and a good length is required to uniformly cool the resin. In addition, in the middle of part D, there is a series of O devices that ooze out lubricant in order to apply the interface IIK lubricant to both surfaces of the inner pipe and the inner surface of the inner pipe. Apply lubricant to both the outside *W and inner surface of the pipe. The high-pressure lubricating rigid wire lubricant introduction path $ leads to the outer surface of the pipe, the inner fitting @ 0 multiple seepage rows, seeps out to the pipe surface, and the lubricant is applied to the interface between the pipe and the 11th surface of the guide. Apply.

ガラス転位温度以上、溶融点温度以下の温度に冷却され
、lI函に潤滑剤が均一にih*され九厚肉)くイブは
、グイ内で樹脂表層、内核がはぼ同速度で流動する。い
わゆるプラグフローになる。次にダイ01部分で、プラ
グフローのパイプの径を拡大し、内厚を薄くして霊軸配
向させる。厚内パイプはプラグフローOま一押出成形機
からO押出圧力によシ径を拡大され圧延されて、流動方
向と直径方向に同時VCN軸配肉される。3軸配向され
たパイプはグイの1部分で更に冷却され、好ましくはガ
ラス転位温度以下Klで冷却されてダイ丁を出る。必l
!に応じて冷水1・勢でl!に冷却され、引取多ロール
11で引取られて冨軸配向パイグとなる。
The tube is cooled to a temperature above the glass transition temperature and below the melting point temperature, and the lubricant is uniformly applied to the lI box.The resin surface layer and inner core of the tube flow at approximately the same speed within the tube. This results in what is called a plug flow. Next, in the die 01 part, the diameter of the plug flow pipe is expanded, the inner thickness is reduced, and the spiritual axis is oriented. The thick inner pipe is expanded in diameter and rolled by O extrusion pressure from a plug flow O-hole extrusion molding machine, and is simultaneously walled in the VCN shaft in the flow direction and the diameter direction. The triaxially oriented pipe is further cooled in one section of the die, preferably at Kl below the glass transition temperature, before exiting the die. must
! Depending on the situation, add 1.5 liters of cold water! The pipe is cooled to a temperature of 100 degrees, and is taken off by a take-up multi-roll 11 to become a fux-oriented pipe.

本発1jlK述べる熱可■性樹脂とは一般に押出成形あ
るーは射出成形Kl用される熱可■性樹脂が全て便用て
き、更に押出成形機で加熱回議化し得る熱可塑性樹脂が
使用できる。伺えばポ9スチレン。
The thermoplastic resin mentioned in the present invention can be any thermoplastic resin that is generally used for extrusion molding or injection molding, and thermoplastic resins that can be heated and recycled in an extrusion molding machine can also be used. If you ask me, it's Po9 Styrene.

スチレン−アクリロニトリル共重合体、−8樹脂。Styrene-acrylonitrile copolymer, -8 resin.

ポリ塩化ビニル、ポリメチルメタクリレート、ポリカー
ボネート、ポリエステル、ナイロン、ポリフェニレンエ
ーテル、あるいはζし等f141Mtoフvンド、共重
合体等である。第1図及び第3図では1種の樹脂を用い
た例で説明したが、!種以上の樹脂の多層成形品も同様
に成形できる0例えば第1図に験て1表層がポリメチル
メタクリレート。
These include polyvinyl chloride, polymethyl methacrylate, polycarbonate, polyester, nylon, polyphenylene ether, f141Mto funds, copolymers, etc. In Fig. 1 and Fig. 3, an example using one type of resin was explained, but! Multi-layer molded products made of more than one type of resin can be molded in the same way. For example, as shown in Figure 1, one surface layer is polymethyl methacrylate.

内核がポリカーボネートより威る3層O厚肉成形体を圧
抵意軸配向させ良好なln軸配配向−トが得られる。こ
の様な3層成形品O場合1表層機脂の軟化温度は内核樹
脂の軟化温度よ〕低いことが好ましい。すたわち、第1
図、A部分で厚内成形体を表面から冷却する丸め1表層
が冷え中すい。
A three-layer O thick-walled molded body whose inner core is more powerful than polycarbonate is oriented in the piezoresistance axis, and a good ln-axis alignment can be obtained. In the case of such a three-layer molded product O, the softening temperature of the first surface layer resin is preferably lower than that of the inner core resin. Stand, 1st
In the figure, in part A, the inner molded body is cooled from the surface.1 The surface layer is cooling down.

厚内成形体がプラダ7p−するため表層と内核が均一な
粘虚を保つには表層OIk北点が低い方が好ましくなる
Since the thick inner molded body exhibits Prada 7p, it is preferable that the surface layer OIk north point be lower in order to maintain uniform viscosity between the surface layer and the inner core.

本発明に述べる潤滑剤には、流動パラフィン、ポリメチ
ルシロキナ7等の各種シリコーン油、ステアリン酸等0
4)1111肪駿、各種界面活性剤等である。これ等潤
滑剤を樹脂表面とグイとの界WJK塗布する。更にこれ
等潤滑剤を多量配合した樹脂を表層に用いて潤滑剤の働
きをさせることもできる。潤滑剤を樹脂表面とグイとの
界mに塗布するには、潤滑剤は通過できるが樹脂は通過
できないスリット、微細孔を有する多孔体等から潤滑剤
を吐出する方法、あるいは多層シート、多層パイプ等の
マルチマニホールドグイ類似のグイ管用い。
The lubricants described in the present invention include liquid paraffin, various silicone oils such as polymethylsilokina 7, stearic acid, etc.
4) 1111 Fatsun, various surfactants, etc. These lubricants are applied to the interface WJK between the resin surface and the goo. Furthermore, a resin containing a large amount of these lubricants can be used in the surface layer to function as a lubricant. In order to apply lubricant to the interface between the resin surface and the goo, there are two methods: discharging the lubricant from a porous body with slits or micropores through which the lubricant can pass but not the resin, or using a multilayer sheet or a multilayer pipe. Uses a gou pipe similar to a multi-manifold gouie such as.

表層用マニホールドより潤滑剤を表層に押出す方法等が
使用できる。
A method such as extruding the lubricant to the surface layer from a surface layer manifold can be used.

本発明に述べゐガラス転位温度以上、溶融点温度以下と
は、一般に合成樹脂を配向させるに適した温度であり、
樹11によシ好ましい温度範囲は異る。結晶性樹脂では
結晶化が起る温度以上、結晶が溶融する温度以下が好ま
しい。非結晶性樹層では、一般の射出成形、押出成形等
Ol!浄温度以下で、好ましくは(該成形温度−一℃)
以下で。
In the present invention, the glass transition temperature or higher and the melting point temperature or lower is generally a temperature suitable for orienting a synthetic resin,
The preferred temperature range varies depending on the tree 11. For crystalline resins, the temperature is preferably higher than the temperature at which crystallization occurs and lower than the temperature at which the crystals melt. For amorphous tree layers, general injection molding, extrusion molding, etc. below the molding temperature, preferably (the molding temperature - 1°C)
Below.

(ガラス転位温度+10℃)以上の範IIが好ましい。(Glass transition temperature +10° C.) or higher range II is preferred.

本発明の方法は厚肉O成形品、好ましくはl■厚以上、
更に好ましく a 1.S■厚以上の成形品O成形に適
している。I/Itに厚内シート、パイプOs軸配向成
形品の成形に適している゛。
The method of the present invention is a thick-walled O-molded product, preferably 1 thick or more,
More preferably a1. Suitable for O molding of molded products with thickness of S■ or more. Suitable for molding I/It, thick inner sheets, and pipe Os axis oriented molded products.

本発明の方法により、任意の延伸倍率の配向成形品が得
られるが、延伸による効果等から1.!6倍から10倍
(厚み比)の延伸倍率が好ましい。
By the method of the present invention, an oriented molded product with an arbitrary stretching ratio can be obtained, but due to the effects of stretching, etc. ! A stretching ratio of 6 to 10 times (thickness ratio) is preferred.

本発明法により、従来成形が困離であった厚内配向成形
品が容易に成形でき、その経済的効果は大きい。
By the method of the present invention, it is possible to easily mold a thickly oriented molded product, which has been difficult to mold in the past, and its economical effects are significant.

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

第1図及び第3図は本発明法により2軸配向成形品を成
形する装置の断面図、第2図成形体の流動変化を説明す
る部分斜視図である。 1・・・・・・・・・・・・・・・押出成形機2、7・
・・・・・・・・・ダイ 4、9・・・・・・・・・潤滑剤浸み出し口6、11・
・・・・・・・・引取りロール特許出願人 旭ダウ株式
会社 手続補正書(幽−) 昭和暮マ年S月/−日 特許庁長官 島−春樹 殿 L 事件の表示  昭和s6年特許原第1881マ1号
2 発明の名称 配向虞膠晶O虞III鉄 a 補正をする者 事件との関係  特許出願人 東京都千代田区有東町1丁目1番2号 −一書「−−fi@II−J晟び「発−・−1龜飄−」
・―@ho内審 (1)特許請求O範−會*moとお伽補正する◇t2)
)次64)X4)ffOr1?ス転t11m1以上、」
を「lツメ転位温度付近から」と補正する。 ―制置の第3頁jIse行、第4頁jIn行、jlll
)[jlllllff、gs頁gis行、菖$頁館饅行
。 −−一書O第1頁、第8行と第1行と0間に、つ「・文
章を挿入する。 [嬉五目、第3■で紘、押出機よ拳押出された熱可塑性
樹■を連続的に押出ダイに圧入して翼軸配向させゐ例を
説明し良が、本発明紘、あらかじめ成形された厚内型物
を押出ダイに圧入して機械的力で押出して電輪配向させ
ることもできゐ◇例えば、あらかじめセル中ヤスト法で
成形された超高分子量ポ!メチルメタクシレート0型物
を、潤滑剤がaSSれたダイ内へ押込み、油圧シリンダ
ー等の力で押出して雪−配向させることもできる。」 (41同、第$頁aS行と第4行とO関に、つぎの文章
を挿入する。 「又、同一樹脂の鳩舎には、表層の分子量が4−さく、
内被O分子量が大きいことが、プラダ7w−する丸めに
好ましい。」 (5)同、第會頁第魯行と第1行と01MIK、つぎの
文章を挿入する。 「又、本発明法により押出された翼軸配向シートを引続
き、連続的に壺種ナイジンダダイに送り4rll影状に
加工することも!能であゐ。例えば、jlEIm、74
!0BileO次Kml[0949yグダイを連結し、
液板状にしえ後に冷却固化させて取〉出すことがで龜る
。」 以上 特許請求の範− L 熱可履性樹脂O声ツス転位温度付近から溶融点温度
以下OII!形体を、潤滑剤がIk布1れたダイ内で、
ダイと接触しり\押出し、あるいは及び引張ることによ
)分子配向させ為ヒとを善黴とする配向威廖晶OSm法 IL  翼軸配向さ−1,&ことを特徴とする特許請求
の範■第1項記載O′j!j法 龜 配向成形晶がパイプ状であることを特徴とする特許
請求O範■第1項記載の方法 未 配向成形品がシート状であることを特徴とする特許
請求011L11第1項記載O方法翫 押出成影機か6
11F幽されえ樹脂を連続して分子配向ダイに圧入す:
hことを特徴とする特許請求のIII!l第1項記第1
方記 載O
1 and 3 are a sectional view of an apparatus for molding a biaxially oriented molded product by the method of the present invention, and FIG. 2 is a partial perspective view illustrating changes in flow of the molded product. 1...Extrusion molding machine 2, 7.
......Die 4, 9...Lubricant seepage port 6, 11.
・・・・・・・・・Take-back roll patent applicant Asahi Dow Co., Ltd. Procedural amendment (Yu-) S/-, 1945/- Director General of the Japan Patent Office Haruki Shima L. Case indication Original patent in 1939 No. 1881 Ma1 No. 2 Name of the invention Orientation Go Glue Crystal O Go III Iron a Relationship with the person making the amendment Patent applicant 1-1-2 Yuto-cho, Chiyoda-ku, Tokyo - Issho "--fi@II -J Akirabi ``Hatsu-・-1 Kashiwa-''
・-@ho Internal Trial (1) Patent Claim O Scope - Meeting *mo and fairy tale amendment ◇t2)
)Next64)X4)ffOr1? More than 11 m1 of slip.”
is corrected to ``from around the l-nail transition temperature.'' -Page 3 jIse line, page 4 jIn line, jllll
) [jlllllff, gs page gis line, iris $ page hall feast. --Issho O, page 1, line 8, insert a sentence between line 1 and 0. An example of continuously press-fitting into an extrusion die to orient the blade axis is good, but in the present invention, a pre-formed thick inner mold is press-fitted into the extrusion die and extruded by mechanical force to orient the blade axis. ◇For example, an ultra-high molecular weight polymethylmethacrylate type 0 product previously formed by the cast method in a cell is pushed into a die coated with aSS lubricant, and extruded using the force of a hydraulic cylinder, etc. It is also possible to make the snow oriented.'' (41, same page, insert the following sentence in line aS, line 4, and section O. fence,
A large molecular weight of O is preferred for Prada 7w- rounding. (5) Insert the following sentence in the same page, page 1, row 1, line 01MIK. "Also, it is also possible to continuously feed the wing axis oriented sheet extruded by the method of the present invention to a pot type die to process it into a 4rll shadow shape. For example, jlEIm, 74
! 0BileO next Kml[0949y connect Gudai,
This makes it easier to cool and solidify the material after it has been turned into a liquid plate and then taken out. ” Claims -L Thermoplastic resin OII from around the transition temperature to below the melting point temperature! The shape is placed in a die containing lubricant with Ik cloth,
Oriented crystal OSm method IL in which molecules are oriented (by extrusion or pulling) in contact with a die, and the axial orientation is -1,& Claims: Paragraph 1 stated O'j! J method Patent claim O, characterized in that the oriented molded crystal is in the shape of a pipe, the method described in item 1, Patent claim 011L11, characterized in that the oriented molded product is in the form of a sheet. Extrusion imaging machine or 6
Continuously press the 11F resin into the molecular orientation die:
Claim III characterized in that h! l Item 1 Item 1
Method description O

Claims (1)

【特許請求の範囲】 1、熱可塑性樹脂のガラス転位温度以上、溶融点温度以
下OS形体を、潤滑剤がIkIM−sれ九ダイ内で、グ
イと接触しり\押出し−あるいは及び引張ることによ〉
分子配向させることを特徴とする配向成形品O成形法 i 3軸配向させることを特徴とする特許請求の範囲第
illll記載法 i 配向成形品がパイプ状であることを特徴とする特許
請求の範囲第1項記載の方法 也 配向成彫晶がシート状であることをIF#黴とする
特許請求0m1m1第1項記載の方法翫 押出成形機か
ら*mされた樹脂を連続して分子配向ダイに圧入すゐこ
とを特徴とする特許請求の範囲第1項記載o2法
[Claims] 1. By extruding or pulling the OS shape of a thermoplastic resin between the glass transition temperature and above and the melting point temperature in a die in which a lubricant is in contact with a gooey. 〉
Oriented molded product O molding method i characterized by molecular orientation Claim No. illll description method i characterized by triaxial orientation Claim characterized in that the oriented molded product is pipe-shaped The method according to paragraph 1 The method according to paragraph 1 The method according to paragraph 1, in which the oriented crystalline crystal is in the form of a sheet is continuously passed through a molecularly oriented die. O2 method described in claim 1, characterized in that it is press-fitted.
JP56103171A 1981-07-03 1981-07-03 Method of molding orientated form Granted JPS585225A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56103171A JPS585225A (en) 1981-07-03 1981-07-03 Method of molding orientated form

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56103171A JPS585225A (en) 1981-07-03 1981-07-03 Method of molding orientated form

Publications (2)

Publication Number Publication Date
JPS585225A true JPS585225A (en) 1983-01-12
JPH0258093B2 JPH0258093B2 (en) 1990-12-06

Family

ID=14347054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56103171A Granted JPS585225A (en) 1981-07-03 1981-07-03 Method of molding orientated form

Country Status (1)

Country Link
JP (1) JPS585225A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4804510A (en) * 1987-06-30 1989-02-14 The Dow Chemical Company Filtering system for use in coextrusion apparatus and method of use
US4842791A (en) * 1987-06-30 1989-06-27 The Dow Chemical Company Extrusion apparatus and process for production of multilayer film containing an inner barrier layer
JPH081311U (en) * 1986-04-14 1996-08-20 エル イクス エス カーベルガルニトゥーレン ゲゼルシヤフト ミット ベシュレンクテル ハフツング Equipment for manufacturing plastic molded products with shape memory
EP1223023A1 (en) * 2001-01-16 2002-07-17 Zahir Bashir Method of solventless processing PAN homopolymers or high acrylonitrile content PAN copolymers
CN112045965A (en) * 2020-08-10 2020-12-08 海宁市宏鹰装饰材料有限公司 PVC buckle production processingequipment

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5421460A (en) * 1977-07-20 1979-02-17 Nippon Petrochemicals Co Ltd Method of manufacturing thermosetting resinous tube article able to spread or shrink by heat

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5421460A (en) * 1977-07-20 1979-02-17 Nippon Petrochemicals Co Ltd Method of manufacturing thermosetting resinous tube article able to spread or shrink by heat

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH081311U (en) * 1986-04-14 1996-08-20 エル イクス エス カーベルガルニトゥーレン ゲゼルシヤフト ミット ベシュレンクテル ハフツング Equipment for manufacturing plastic molded products with shape memory
JPH081310U (en) * 1986-04-14 1996-08-20 エル イクス エス カーベルガルニトゥーレン ゲゼルシヤフト ミット ベシュレンクテル ハフツング Plastic molded product with shape memory
US4804510A (en) * 1987-06-30 1989-02-14 The Dow Chemical Company Filtering system for use in coextrusion apparatus and method of use
US4842791A (en) * 1987-06-30 1989-06-27 The Dow Chemical Company Extrusion apparatus and process for production of multilayer film containing an inner barrier layer
EP1223023A1 (en) * 2001-01-16 2002-07-17 Zahir Bashir Method of solventless processing PAN homopolymers or high acrylonitrile content PAN copolymers
CN112045965A (en) * 2020-08-10 2020-12-08 海宁市宏鹰装饰材料有限公司 PVC buckle production processingequipment

Also Published As

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