JPH06143389A - Manufacture of fluorocarbon resin tube - Google Patents
Manufacture of fluorocarbon resin tubeInfo
- Publication number
- JPH06143389A JPH06143389A JP4293453A JP29345392A JPH06143389A JP H06143389 A JPH06143389 A JP H06143389A JP 4293453 A JP4293453 A JP 4293453A JP 29345392 A JP29345392 A JP 29345392A JP H06143389 A JPH06143389 A JP H06143389A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- temperature
- fluororesin
- fluorocarbon resin
- die
- 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
Links
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、フッ素樹脂チューブの
製造方法に関し、特に細径で薄肉であり、なおかつチュ
ーブのカールや径変動の無いの高品質のフッ素樹脂チュ
ーブを製造する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a fluororesin tube, and more particularly to a method for producing a high-quality fluororesin tube which is thin and thin and has no curl or diameter fluctuation.
【0002】[0002]
【従来の技術】フッ素樹脂チューブは、電気絶縁性、耐
熱性、耐薬品性、抗血栓性などに極めて優れているた
め、様々な用途での需要が増加してきており、近年、カ
テーテルなどの医療分野や電子機器分野を中心にチュー
ブの細径化が強く望まれている。従来、これらフッ素樹
脂チューブの押出成形による製造は、溶融樹脂をダイか
らチューブ状に押出した後、水槽中を通過させる水冷方
法によって冷却固化して製品化していた。2. Description of the Related Art Fluororesin tubes are extremely excellent in electrical insulation, heat resistance, chemical resistance, antithrombogenicity, etc., so that demand for them in various applications is increasing. There is a strong demand for thinner tubes, especially in the fields of electronic devices. Conventionally, in the production of these fluororesin tubes by extrusion molding, a molten resin is extruded from a die into a tube shape, and then cooled and solidified by a water cooling method of passing through a water tank to produce a product.
【0003】しかし、この方法では、チューブが細径・
薄肉の場合、冷却後のチューブが湾曲するカール現象を
起こしてしまうという問題があった。これは、薄肉チュ
ーブでは溶融樹脂がダイから押出される際に偏流が起こ
り易く、その偏りが残留したまま急冷されることが原因
になっている。フッ素樹脂の場合、融点が200℃以上
であるため、たとえ冷却水の温度を100℃近くに上げ
たとしても、100度以上の温度差を急冷することとな
り、水冷法を用いる限りそのようなカール現象は防げな
い。また、冷媒としてシリコーンオイルなどを使用して
加熱し、温度差を小さくすることも考えられるが、特に
医療用途では、そのような不純物の残存は許されず、チ
ューブ洗浄を厳格に行なう必要が生じ、コスト的に見合
わないものとなってしまう。However, in this method, the tube has a small diameter.
In the case of a thin wall, there is a problem that the tube after cooling causes a curl phenomenon in which the tube bends. This is because in a thin-walled tube, uneven flow is likely to occur when the molten resin is extruded from the die, and the thin resin is rapidly cooled while the unevenness remains. In the case of a fluororesin, the melting point is 200 ° C or higher, so even if the temperature of the cooling water is raised to near 100 ° C, the temperature difference of 100 ° C or more is rapidly cooled, and as long as the water cooling method is used, such curl The phenomenon cannot be prevented. It is also possible to heat using silicone oil or the like as a refrigerant to reduce the temperature difference, but especially in medical applications, such impurities are not allowed to remain, and tube cleaning must be performed strictly. It will not be worth the cost.
【0004】[0004]
【発明が解決しようとする課題】よって、本発明におけ
る課題は、細径、薄肉であり、なおかつ肉厚や径のばら
つきのない高品質なフッ素樹脂チューブの製造方法を提
供することにある。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a method for producing a high-quality fluororesin tube which has a small diameter and a thin wall and has no variation in the wall thickness or the diameter.
【課題を解決するための手段】かかる課題は、フッ素樹
脂またはフッ素樹脂をベースとする樹脂混和物を溶融押
出してチューブ状に成形するフッ素樹脂チューブ製造方
法において、ダイリップからチューブが冷却固化するま
での間にわたって、チューブが通過する近傍の空気の温
度を30℃以上とすることによって解決できる。The object of the present invention is to manufacture a fluororesin tube by melt-extruding a fluororesin or a resin mixture based on the fluororesin to form a tube, from the die lip until the tube is cooled and solidified. This can be solved by setting the temperature of the air in the vicinity of the passage of the tube to 30 ° C. or higher over the period.
【0005】以下に、本発明のフッ素樹脂チューブの製
造方法を図に従って詳述する。図1は本発明の製造方法
を実施するのに好適な装置の一例を示す図である。図中
符号1は押出機本体であり、この押出機本体1の先端に
はチューブ成形用のダイ2が取り付けられている。この
ダイ2の前方には冷却筒3が設けられている。この冷却
筒3は、円筒形の形状のものであって、その中心軸線が
ダイ2の中央のダイリップと一致するように配置されて
いる。また、この冷却筒3の外周壁には水冷管4が螺旋
状に巻き付けられ設けられている。The method for producing the fluororesin tube of the present invention will be described in detail below with reference to the drawings. FIG. 1 is a diagram showing an example of an apparatus suitable for carrying out the manufacturing method of the present invention. In the figure, reference numeral 1 is an extruder body, and a tube molding die 2 is attached to the tip of the extruder body 1. A cooling cylinder 3 is provided in front of the die 2. The cooling cylinder 3 has a cylindrical shape, and is arranged such that its central axis coincides with the center die lip of the die 2. A water cooling pipe 4 is spirally wound around the outer peripheral wall of the cooling cylinder 3.
【0006】上記押出機本体1は、通常の押出成形に使
用されている装置がそのまま使用できる。また、ダイ2
は、通常用いられているものが使用できるが、耐熱耐食
合金製のものを用いるのが好ましい。また、水冷管4
は、図示しない冷却水供給装置に接続され、所定温度の
冷却水が水冷管4に導かれるようになっている。さら
に、冷却筒3は、押出成形されるフッ素樹脂チューブ5
の外径より少なくとも2cm以上大きな内径を有し、か
つその長さはダイリップから溶融樹脂が変形しない温度
まで冷却固化される点までの距離以上であることが好ま
しい。As the extruder main body 1, an apparatus used for ordinary extrusion molding can be used as it is. Also, die 2
As the material, a commonly used material can be used, but it is preferable to use a material made of a heat and corrosion resistant alloy. Also, the water cooling pipe 4
Is connected to a cooling water supply device (not shown) so that cooling water of a predetermined temperature is guided to the water cooling pipe 4. Further, the cooling cylinder 3 is a fluororesin tube 5 that is extruded.
It is preferable that the inner diameter is at least 2 cm or more larger than the outer diameter and the length is at least the distance from the die lip to the point where the molten resin is cooled and solidified to a temperature at which the molten resin is not deformed.
【0007】このような装置を使って、本発明の具体的
な製造法を説明する。まず、冷却筒3周囲に取り付けら
れた水冷管4に所定温度の恒温水を循環させ、冷却筒3
内部のフッ素樹脂チューブ5が通過する近傍の温度が3
0℃以上になるよう調整する。本発明において、チュー
ブが通過する近傍とは、チューブの表面から少なくとも
2cm以内の範囲を指すこととする。A specific manufacturing method of the present invention will be described using such an apparatus. First, constant temperature water at a predetermined temperature is circulated through the water cooling pipe 4 attached around the cooling cylinder 3 to
The temperature in the vicinity where the internal fluororesin tube 5 passes is 3
Adjust so that the temperature is 0 ° C or higher. In the present invention, the vicinity where the tube passes shall mean a range within at least 2 cm from the surface of the tube.
【0008】次に押出機本体1のホッパに、原料となる
フッ素樹脂を投入し、所定温度に加熱して樹脂を溶融さ
せる。溶融したフッ素樹脂をシリンダ内からダイ2のダ
イリップを通してチューブ状に成形して押出す。押出条
件は、材料となるフッ素樹脂の性質によって異なるが、
一般にフッ素樹脂チューブの押出成形に使用されている
条件を用いる。Next, a fluororesin as a raw material is charged into the hopper of the extruder main body 1 and heated to a predetermined temperature to melt the resin. The molten fluororesin is extruded from the inside of the cylinder through the die lip of the die 2 into a tube shape. Extrusion conditions differ depending on the properties of the fluororesin used as the material,
The conditions generally used for extrusion molding of fluororesin tubes are used.
【0009】押出された溶融樹脂は、冷却筒3内部の3
0℃以上の温度に保たれた領域を通過する間に、周囲の
空気に熱を放出することによって徐々に冷却され、冷却
筒3を出る時点では変形を起こさない温度まで冷却・固
化される。冷却・固化されたフッ素樹脂チューブ5は、
引取りロール6を通して切断装置などに移送され製品化
される。The molten resin extruded is stored in the cooling cylinder 3 inside
While passing through the region kept at a temperature of 0 ° C. or higher, it is gradually cooled by releasing heat to the surrounding air, and when it leaves the cooling cylinder 3, it is cooled and solidified to a temperature at which it does not deform. The cooled and solidified fluororesin tube 5
It is transferred to a cutting device or the like through the take-up roll 6 and commercialized.
【0010】フッ素樹脂チューブ5の原料となるフッ素
樹脂またはフッ素樹脂をベースとする樹脂混和物は、通
常の押出成形で成形しうるフッ素系樹脂はすべて使用で
き、例としてポリ4フッ化エチレン−パーフルオロビニ
ルエーテル共重合体(PFA)、ポリ4フッ化エチレン
−6フッ化プロピレン共重合体(FEP)、ポリ4フッ
化エチレン−エチレン共重合体(ETFE)などが挙げ
られる。また、これらを2種以上混合したもの、フッ素
樹脂以外の樹脂を混合したものも使用できる。The fluororesin or the fluororesin-based resin mixture used as the raw material for the fluororesin tube 5 may be any fluororesin which can be molded by ordinary extrusion molding. For example, polytetrafluoroethylene-peroxide may be used. Examples thereof include fluorovinyl ether copolymer (PFA), polytetrafluoroethylene-6-fluoropropylene copolymer (FEP), and polytetrafluoroethylene-ethylene copolymer (ETFE). Also, a mixture of two or more of these and a mixture of resins other than fluororesin can be used.
【0011】このような製造方法によれば、ダイ2から
押出された溶融樹脂は、30℃以上の温度に保たれた冷
却筒3内で、熱伝導率の低い空気に徐々に熱を放出しな
がら、押出し時に残った応力の偏りを緩和しつつ冷却固
化する。従って、カール現象も見られず、なおかつ成形
後の洗浄も必要ない。しかも、局所的な温度分布による
チューブの外径や内径にばらつきも無く、冷却固化され
るまでの間にチューブに気流・風などが当り、偏肉した
り径の変動を生じたりするという問題も発生しない。According to such a manufacturing method, the molten resin extruded from the die 2 gradually releases heat to the air having a low thermal conductivity in the cooling cylinder 3 kept at a temperature of 30 ° C. or higher. On the other hand, it is cooled and solidified while alleviating the bias of the stress remaining during the extrusion. Therefore, no curling phenomenon is observed, and cleaning after molding is not necessary. Moreover, there is no variation in the outer diameter or inner diameter of the tube due to the local temperature distribution, and there is a problem that the tube is hit with air flow, wind, etc. until it is cooled and solidified, resulting in uneven thickness and variation in diameter. Does not occur.
【0012】なお、上記の説明では、ダイリップからチ
ューブが冷却固化するまでの間にわたって、チューブが
通過する近傍の空気の温度を30℃以上とする恒温手段
として、外周に螺旋状に形成された水冷管を持つ冷却筒
を使用したが、その恒温手段としては、目的に合致する
ものならば、形状、材料などは特に限定されず、種々の
ものが用いられる。In the above description, as a constant temperature means for keeping the temperature of the air in the vicinity of the tube at 30 ° C. or higher from the die lip until the tube is cooled and solidified, the water cooling spirally formed on the outer circumference. Although a cooling cylinder having a pipe was used, the constant temperature means is not particularly limited in shape, material and the like as long as it meets the purpose, and various ones can be used.
【0013】例えば、冷却筒自体を二重筒とし、内筒と
外筒の間を水冷部としてもよいし、螺旋状の水冷管を間
隔があかないよう密に巻き、内筒なしで上述の説明と同
様に使用してもよい。さらに、チューブが通過する領域
を取り囲むような形状のセラミック・ヒーターやラバー
・ヒーターなどを使用してもよい。いずれの場合も、冷
却固化する前のチューブに気流や塵等が当たらないよ
う、チューブを取り囲んだ形態で設けるのが好ましい。For example, the cooling cylinder itself may be a double cylinder, and a water cooling section may be provided between the inner cylinder and the outer cylinder, or a spiral water cooling pipe may be densely wound so that there is no space between the inner cylinder and the outer cylinder. It may be used as described. Further, a ceramic heater or a rubber heater having a shape surrounding the region through which the tube passes may be used. In any case, it is preferable that the tube is provided so as to surround the tube so that airflow, dust, etc. do not hit the tube before being cooled and solidified.
【0014】また、上記恒温手段の内部に温度検出手段
を設けておき、その出力に応じて循環させる水の温度
や、ヒーターに供給する電力を調節するような手段を設
けてもよい。また、それら恒温手段は、ダイ2から押出
された溶融樹脂が、即座に内部に入る位置に配置される
ものであって、押出機に直接固定してもよいし、他の固
定手段を用いて固定してもよい。Further, temperature detecting means may be provided inside the constant temperature means, and means for adjusting the temperature of the water to be circulated and the electric power supplied to the heater according to the output thereof may be provided. Further, the constant temperature means is arranged at a position where the molten resin extruded from the die 2 immediately enters the inside, and may be directly fixed to the extruder, or other fixing means may be used. You may fix it.
【0015】以下に本発明の製造法を、具体例を挙げて
説明する。 (実施例1)押出機に外径2mmのニップル、内径3m
mのチューブ成形用ダイを取り付けた。外径15cm、
内径10cm、長さ1mの鉄管の周囲に螺旋状に鉄製水
冷管を巻いた冷却筒を用意し、その円筒の中心線が、お
よそ樹脂の押出方向と一致するよう押出機に固定した。
冷却筒の水冷管に15℃の水を循環させて冷却筒内が3
0℃となるよう温度調節した。押出機のホッパにPFA
を投入し、シルンダ温度を360℃、ヘッド温度を38
0℃として加熱溶融させた。50g/minの速度で溶
融樹脂を押出し、冷却筒内を通して引き取り機に引き取
った。成形されたチューブを適当な位置で垂直に切断
し、ルーペで断面チューブ外径を測定した。同様に、F
EP,ETFEを用いてチューブを成形し、断面の外径
を測定した。結果を表1に示す。The production method of the present invention will be described below with reference to specific examples. (Example 1) A nipple having an outer diameter of 2 mm and an inner diameter of 3 m is used in an extruder.
m tube forming die was attached. Outer diameter 15 cm,
A cooling cylinder was prepared by spirally winding an iron water-cooled pipe around an iron pipe having an inner diameter of 10 cm and a length of 1 m, and the cooling cylinder was fixed to an extruder so that the center line of the cylinder approximately coincided with the resin extrusion direction.
By circulating water at 15 ° C through the water cooling pipe of the cooling cylinder,
The temperature was adjusted to 0 ° C. PFA in the hopper of the extruder
, And the Siranda temperature is 360 ° C and the head temperature is 38
It was heated to melt at 0 ° C. The molten resin was extruded at a rate of 50 g / min, passed through the inside of the cooling cylinder, and taken into a take-out machine. The formed tube was vertically cut at an appropriate position, and the cross-section tube outer diameter was measured with a loupe. Similarly, F
A tube was molded using EP and ETFE, and the outer diameter of the cross section was measured. The results are shown in Table 1.
【0016】[0016]
【表1】 [Table 1]
【0017】(実施例2)水冷管に流す水の温度を45
℃として冷却筒内が60℃となるよう温度調節した以外
は実施例1と同様の実験を行った。結果を表2に示す。(Embodiment 2) The temperature of the water flowing through the water cooling pipe is set to 45
The same experiment as in Example 1 was carried out except that the temperature was adjusted so that the temperature inside the cooling cylinder was 60 ° C. The results are shown in Table 2.
【0018】[0018]
【表2】 [Table 2]
【0019】(比較例1)水冷管に流す水の温度を10
℃として冷却筒内が20℃となるよう温度調節した以外
は実施例1と同様の実験を行った。結果を表3に示す。(Comparative Example 1) The temperature of the water flowing through the water cooling tube was adjusted to 10
The same experiment as in Example 1 was performed except that the temperature was adjusted so that the temperature inside the cooling cylinder was 20 ° C. The results are shown in Table 3.
【0020】[0020]
【表3】 [Table 3]
【0021】(比較例2)実施例1の装置から冷却筒を
取り外し、温度制御することなしに、その他は実施例1
と同条件でチューブを成形し、切断してチューブ外径を
測定した。結果を表4に示す。(Comparative Example 2) The cooling cylinder was removed from the apparatus of Example 1 and the temperature was not controlled.
A tube was molded under the same conditions as above, cut and the tube outer diameter was measured. The results are shown in Table 4.
【0022】[0022]
【表4】 [Table 4]
【0023】以上の結果から明らかなように、いずれの
フッ素樹脂においても、冷却筒の温度を20℃とした場
合には冷却速度が大きすぎ、水中で急冷したものと同様
にチューブがカールしてしまい、冷却筒を設けないもの
は、大きな外径変動を起こしている。それに対して、3
0℃以上の温度に保たれた冷却筒を設けた場合には、チ
ューブがカールすることもなく、外径変動もほとんど無
い。As is clear from the above results, in any of the fluororesins, when the temperature of the cooling cylinder was 20 ° C., the cooling rate was too high and the tube curled like the one rapidly cooled in water. Therefore, in the case where the cooling cylinder is not provided, a large fluctuation in outer diameter occurs. On the other hand, 3
When the cooling cylinder maintained at a temperature of 0 ° C. or higher is provided, the tube does not curl and the outer diameter hardly changes.
【0024】[0024]
【発明の効果】本発明のフッ素樹脂チューブの製造方法
では、溶融樹脂がダイから押出された後、30℃以上の
温度に保たれた冷却筒内で空冷されるため、熱伝導率の
低い空気中で徐々に熱を放出しながら、チューブに残っ
た応力の偏りを緩和しつつ冷却固化する。従って、カー
ル現象も見られず、成形後の洗浄も必要ない。しかも、
局所的な温度分布によるチューブの外径や内径にばらつ
きも無く、冷却固化されるまでの間に、チューブに気流
・風などが当り、偏肉したり径の変動を生じたりすると
いう問題も発生しない。よって、径変動がほとんど無い
高品質なチューブを作製することができる。また、通常
の押出成形機をそのまま応用できるため、設備費等のコ
ストもかからない。According to the method for producing a fluororesin tube of the present invention, since the molten resin is extruded from the die and then air-cooled in the cooling cylinder maintained at a temperature of 30 ° C. or higher, air having a low thermal conductivity is obtained. While gradually releasing heat in the tube, it cools and solidifies while alleviating the bias of the stress remaining in the tube. Therefore, the curl phenomenon is not observed and cleaning after molding is not necessary. Moreover,
There is no variation in the outer diameter or inner diameter of the tube due to the local temperature distribution, and there is also a problem that the tube is hit with air flow, wind, etc. before it is cooled and solidified, causing uneven thickness and fluctuation in diameter. do not do. Therefore, it is possible to manufacture a high-quality tube with almost no diameter variation. Moreover, since an ordinary extrusion molding machine can be applied as it is, there is no cost such as equipment cost.
【0025】[0025]
【図1】 本発明の製造方法を実施するのに好適な装置
の一例を側面からみた概略構成図である。FIG. 1 is a schematic configuration view of an example of an apparatus suitable for carrying out the manufacturing method of the present invention when viewed from the side.
1…押出機、2…ダイ、3…冷却筒、4…水冷管、5…
フッ素樹脂チューブ、6…引き取り機1 ... Extruder, 2 ... Die, 3 ... Cooling tube, 4 ... Water cooling tube, 5 ...
Fluororesin tube, 6 ... Take-up machine
Claims (1)
する樹脂混和物を溶融押出してチューブ状に成形するフ
ッ素樹脂チューブ製造方法において、ダイリップからチ
ューブが冷却固化するまでの間にわたって、チューブが
通過する近傍の空気の温度を30℃以上に保つことを特
徴とするフッ素樹脂チューブの製造方法。1. A method for producing a fluororesin tube in which a fluororesin or a resin mixture containing a fluororesin as a base is melt-extruded to form a tube shape, in the vicinity of the passage of the tube from the die lip until the tube is cooled and solidified. The method for producing a fluororesin tube, characterized in that the temperature of the air is kept at 30 ° C. or higher.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29345392A JP3529396B2 (en) | 1992-10-30 | 1992-10-30 | Method for manufacturing fluororesin tube |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29345392A JP3529396B2 (en) | 1992-10-30 | 1992-10-30 | Method for manufacturing fluororesin tube |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06143389A true JPH06143389A (en) | 1994-05-24 |
JP3529396B2 JP3529396B2 (en) | 2004-05-24 |
Family
ID=17794958
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29345392A Expired - Fee Related JP3529396B2 (en) | 1992-10-30 | 1992-10-30 | Method for manufacturing fluororesin tube |
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JP (1) | JP3529396B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1086205A (en) * | 1996-09-11 | 1998-04-07 | Asahi Glass Co Ltd | Tube molded product |
WO2008143035A1 (en) | 2007-05-10 | 2008-11-27 | Gunze Limited | Fluororesin tube and process for producing the same |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105922545A (en) * | 2016-05-31 | 2016-09-07 | 宁波方力科技股份有限公司 | Water circulation system for vacuum setting machine |
-
1992
- 1992-10-30 JP JP29345392A patent/JP3529396B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1086205A (en) * | 1996-09-11 | 1998-04-07 | Asahi Glass Co Ltd | Tube molded product |
WO2008143035A1 (en) | 2007-05-10 | 2008-11-27 | Gunze Limited | Fluororesin tube and process for producing the same |
EP2143541A1 (en) * | 2007-05-10 | 2010-01-13 | Gunze Limited | Fluororesin tube and process for producing the same |
US8097314B2 (en) | 2007-05-10 | 2012-01-17 | Gunze Limited | Fluororesin tube and process for producing the same |
EP2143541A4 (en) * | 2007-05-10 | 2012-12-05 | Gunze Kk | FLUORORA TUBE AND MANUFACTURING METHOD THEREFOR |
Also Published As
Publication number | Publication date |
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JP3529396B2 (en) | 2004-05-24 |
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