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JPS647856B2 - - Google Patents
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JPS647856B2 - - Google Patents

Info

Publication number
JPS647856B2
JPS647856B2 JP51049671A JP4967176A JPS647856B2 JP S647856 B2 JPS647856 B2 JP S647856B2 JP 51049671 A JP51049671 A JP 51049671A JP 4967176 A JP4967176 A JP 4967176A JP S647856 B2 JPS647856 B2 JP S647856B2
Authority
JP
Japan
Prior art keywords
tube
tetrafluoroethylene resin
porous
fibers
fiber
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
JP51049671A
Other languages
Japanese (ja)
Other versions
JPS52132078A (en
Inventor
Koichi Okita
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries 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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP4967176A priority Critical patent/JPS52132078A/en
Priority to US05/751,876 priority patent/US4082893A/en
Priority to CA268,375A priority patent/CA1046433A/en
Priority to DE2658656A priority patent/DE2658656C3/en
Priority to FR7639090A priority patent/FR2336622A1/en
Priority to GB5399176A priority patent/GB1577326A/en
Publication of JPS52132078A publication Critical patent/JPS52132078A/en
Priority to US06/047,470 priority patent/US4234535A/en
Publication of JPS647856B2 publication Critical patent/JPS647856B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/30Polyalkenyl halides
    • B01D71/32Polyalkenyl halides containing fluorine atoms
    • B01D71/36Polytetrafluoroethylene
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61FFILTERS IMPLANTABLE INTO BLOOD VESSELS; PROSTHESES; DEVICES PROVIDING PATENCY TO, OR PREVENTING COLLAPSING OF, TUBULAR STRUCTURES OF THE BODY, e.g. STENTS; ORTHOPAEDIC, NURSING OR CONTRACEPTIVE DEVICES; FOMENTATION; TREATMENT OR PROTECTION OF EYES OR EARS; BANDAGES, DRESSINGS OR ABSORBENT PADS; FIRST-AID KITS
    • A61F2/00Filters implantable into blood vessels; Prostheses, i.e. artificial substitutes or replacements for parts of the body; Appliances for connecting them with the body; Devices providing patency to, or preventing collapsing of, tubular structures of the body, e.g. stents
    • A61F2/02Prostheses implantable into the body
    • A61F2/04Hollow or tubular parts of organs, e.g. bladders, tracheae, bronchi or bile ducts
    • A61F2/06Blood vessels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1692Other shaped material, e.g. perforated or porous sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06Tubular membrane modules
    • B01D63/061Manufacturing thereof
    • 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
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/02Moulding by agglomerating
    • B29C67/04Sintering
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/10Filtering material manufacturing

Landscapes

  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Public Health (AREA)
  • Oral & Maxillofacial Surgery (AREA)
  • Biomedical Technology (AREA)
  • Heart & Thoracic Surgery (AREA)
  • Vascular Medicine (AREA)
  • Cardiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Transplantation (AREA)
  • Veterinary Medicine (AREA)
  • Mechanical Engineering (AREA)
  • Pulmonology (AREA)
  • Gastroenterology & Hepatology (AREA)
  • Manufacturing & Machinery (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Materials For Medical Uses (AREA)

Description

【発明の詳細な説明】 本発明は多孔性四弗化エチレン樹脂チユーブに
関するものであり、特にチユーブの繊維組織が外
表面と内表面において異なつた複合構造となつて
いることを特徴とする多孔性四弗化エチレン樹脂
チユーブ及びその製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a porous tetrafluoroethylene resin tube, and in particular, a porous polyethylene resin tube characterized in that the fiber structure of the tube has a different composite structure on the outer surface and inner surface. The present invention relates to a tetrafluoroethylene resin tube and a method for manufacturing the same.

多孔性四弗化エチレン樹脂チユーブの製造方法
に関しては特公昭42−13560号および特開昭46−
7284などが公知である。これらの方法は次のよう
である:液状潤滑剤を含む未焼結の四弗化エチレ
ン樹脂混合物を押出し圧延又は両者を含む方法で
シート、ロツド、チユーブ等に成形したのち未焼
結状態で少なくとも一方向に延伸した状態で約
327℃以上に加熱することを特徴としている。こ
れらの方法で得られた多孔性構造物は延伸した割
合や延伸時の温度、速度等により幾分変化すると
はいうものの、小さい繊維によつて互に連結され
た結節からなるミクロン複合構造を有し、この繊
維と結節とで囲まれた空間が多孔性空孔に一致し
ている。一般的には延伸する割合を増すことによ
つて繊維の長さを大きくし、結節の大きさを小さ
くし、多孔性の割合即ち気孔率が増大する。
Regarding the manufacturing method of porous tetrafluoroethylene resin tubes, please refer to Japanese Patent Publication No. 13560/1973 and Japanese Patent Application Laid-open No. 1973-13560.
7284 etc. are publicly known. These methods are as follows: An unsintered tetrafluoroethylene resin mixture containing a liquid lubricant is formed into a sheet, rod, tube, etc. by extrusion rolling or a method including both, and then at least Approximately when stretched in one direction
It is characterized by heating to over 327℃. Although the porous structures obtained by these methods vary somewhat depending on the stretching ratio, temperature and speed during stretching, they have a micron composite structure consisting of nodules interconnected by small fibers. However, the spaces surrounded by these fibers and nodules correspond to porous pores. Generally, by increasing the degree of stretching, the length of the fibers is increased, the size of the nodules is decreased, and the percent porosity is increased.

結果これらの公知方法ではシート、ロツド、チ
ユーブ等の多孔性構造物が得られることが知られ
ている。
As a result, it is known that porous structures such as sheets, rods and tubes can be obtained using these known methods.

本発明はこれらの方法の改良に関するものであ
つて、特にチユーブ状多孔性構造物の繊維の太さ
長さおよびその方向などとこの繊維と連らなつた
結節形状などを含めた繊維組織がチユーブの外表
面と内表面において違つた高次の複合構造を有す
る多孔性四弗化エチレン樹脂チユーブを提供する
ものである。
The present invention relates to improvements in these methods, and in particular, the fiber structure including the thickness and length of the fibers of the tube-like porous structure, the direction thereof, and the shape of the nodules connected to the fibers is The present invention provides a porous tetrafluoroethylene resin tube having different high-order composite structures on its outer and inner surfaces.

更に本発明はチユーブ状に成形したのちチユー
ブの長さ方向に延伸した状態で少なくともチユー
ブの外表面が327℃以上でかつチユーブの内表面
がチユーブの外表面より低い温度によるように加
熱することによつてチユーブ状多孔性構造物の繊
維組織が外表面と内表面において違つた複合構造
となることを特徴とする多孔性四弗化エチレン樹
脂チユーブの製造方法に係るものであり、たとえ
ば四弗化エチレン樹脂の融点である327℃以上に
加熱する時、チユーブ内腔部分に冷却空気を供給
しながら焼結することによつて達成される。
Furthermore, the present invention involves heating the tube so that at least the outer surface of the tube is at a temperature of 327° C. or higher and the inner surface of the tube is lower than the outer surface of the tube when the tube is formed into a tube shape and then stretched in the length direction of the tube. Therefore, the present invention relates to a method for manufacturing a porous tetrafluoroethylene resin tube, which is characterized in that the fiber structure of the tube-like porous structure has a different composite structure on the outer surface and the inner surface. This is achieved by sintering while supplying cooling air to the inner cavity of the tube when heated above 327°C, which is the melting point of ethylene resin.

したがつて本発明の目的はチユーブの外表面と
内表面の繊維組織が違つていることが好ましい用
途、具体的には人工血管、人工気管、人工食道、
人工胆管などの代用補綴物、あるいは工業的過
用途としては気体や液体等がチユーブ多孔性管壁
を過浸透していく時の過抵抗の低下、目詰り
防止を可能とする材料更にはシール用のガスケツ
トパツキング等に経済的な製品を提供することに
ある。
Therefore, the purpose of the present invention is to provide applications in which it is preferable that the outer and inner surfaces of the tube have different fibrous structures, specifically, artificial blood vessels, artificial tracheas, artificial esophagus,
For substitute prostheses such as artificial bile ducts, or for industrial purposes, it is a material that reduces excessive resistance and prevents clogging when gases, liquids, etc. permeate the porous tube wall, and also for seals. Our goal is to provide economical products for gasket packing, etc.

プラスチツクからなる人工蔵器に要請される事
は(1)生体組織液によつて変性しないこと、(2)化学
的に不活性、(3)無炎症性で異物反応がないこと、
(4)発癌性のないこと、(5)組織内で膨潤しないこ
と、(6)抗張力等の機械的性質が経時変化しないこ
と、等が知られているが、四弗化エチレン樹脂は
これらの条件を全て満足しており、最も有望なプ
ラスチツクの一つである。しかるに成型、加工上
にかなりの困難性を伴つているため従来その機能
を充分に発揮することができなかつた。
The requirements for artificial devices made of plastic are (1) not to be denatured by biological tissue fluids, (2) to be chemically inert, (3) to be non-inflammatory and free from foreign body reactions.
It is known that (4) it is not carcinogenic, (5) it does not swell within tissues, and (6) its mechanical properties such as tensile strength do not change over time. It satisfies all the conditions and is one of the most promising plastics. However, since molding and processing are quite difficult, it has not been possible to fully demonstrate its functions in the past.

工業的過用途においても、最近逆浸透膜、超
過膜などが開発されている。これらの膜は過
の機能を果たす極薄表面層は微細孔径からなり、
機械的強度を維持する支持体層は大孔径からなる
複合構造を有しており、平面的な形状のみならず
チユーブ状の形状のものも知られている。しかる
にこの膜の素材はセルロース類やポリアミド類で
あつて四弗化エチレン樹脂についてはこの様な構
造体が全く知られていない。またチユーブ状ガス
ケツトとしては外表面が硬く、内腔表面が柔軟で
圧縮性の良いことを充分に満足することが必要で
ある。
For industrial applications, reverse osmosis membranes, excess membranes, etc. have recently been developed. The ultra-thin surface layer of these membranes has microscopic pores,
The support layer that maintains mechanical strength has a composite structure consisting of large pores, and not only planar shapes but also tube-like shapes are known. However, the material of this membrane is cellulose or polyamide, and no such structure is known for tetrafluoroethylene resin. Further, as a tube-shaped gasket, it is necessary that the outer surface is hard and the inner cavity surface is flexible and has good compressibility.

本発明では未焼結の四弗化エチレン樹脂粉末を
液体潤滑剤と均一混和し、予備圧縮成形を行つて
ラム式押出機によりチユーブ形状に成形する。次
に蒸発または抽出によつて液状潤滑剤を除去した
後で少なくとも一方向、大低の場合はチユーブの
長さ方向に延伸する。この工程までは前述の公知
方法と同一または類似しているが次工程の327℃
以上の温度に加熱する所が公知方法とは違つてお
り、本発明の最も重要な所である。
In the present invention, unsintered tetrafluoroethylene resin powder is uniformly mixed with a liquid lubricant, pre-compression molded, and then molded into a tube shape using a ram extruder. Then, after removing the liquid lubricant by evaporation or extraction, the tube is stretched in at least one direction, or in the case of a long or narrow direction, the length of the tube. Up to this step, the process is the same or similar to the above-mentioned known method, but the temperature in the next step is 327°C.
The heating to the above temperature is different from known methods and is the most important aspect of the present invention.

延伸されたチユーブを加熱する時、チユーブ内
部からのみ熱を供給することは不可能ではないが
経済的にはチユーブ外部から加熱する。この時チ
ユーブ内部に空気を流すことによつて冷却しなが
ら外部からの熱供給を行なうことによつてチユー
ブ内腔表面と外表面の多孔性繊維組織を変えるこ
とが可能となる。
When heating a stretched tube, it is not impossible to supply heat only from inside the tube, but it is economical to heat it from outside the tube. At this time, by supplying heat from the outside while cooling the inside of the tube by flowing air, it becomes possible to change the porous fibrous structure of the inner surface and outer surface of the tube.

多孔性繊維組織は小さな繊維とその繊維に互に
連結された結節とからなるミクロ構造を有してい
る。本発明ではたとえば繊維直径はチユーブ内腔
表面では小さく、外表面では少なくとも内腔表面
の2倍以上の太さを持つた高次のミクロ構造を有
するが、結節の大きさはチユブの内腔表面と外表
面ではほとんど変らないといつた様な構造物を第
1の対象とする。結節の大きさや繊維長さは延伸
する条件により変わるものであるが繊維径は一方
向に延伸している限り大巾には変化しない。一
方、二方向以上に延伸するとこの繊維径は急激に
小さくなることは判つているがこの様な多孔性繊
維構造においても、本発明によるチユーブは内腔
表面と外表面では違つた繊維太さ、繊維長さ、結
節形状からなる断面構造を有することを特徴とし
ている。
Porous fibrous tissues have a microstructure consisting of small fibers and nodules interconnected with the fibers. In the present invention, for example, the fiber diameter is small on the inner surface of the tube, and the outer surface has a high-order microstructure that is at least twice as thick as the inner surface of the tube. The first target is a structure whose outer surface remains almost unchanged. Although the size of the nodule and the fiber length vary depending on the drawing conditions, the fiber diameter does not change significantly as long as the fiber is drawn in one direction. On the other hand, it is known that the fiber diameter decreases rapidly when stretched in two or more directions, but even in such a porous fiber structure, the tube according to the present invention has different fiber thicknesses on the inner surface and outer surface. It is characterized by having a cross-sectional structure consisting of fiber length and nodular shape.

更に本発明の対称とする第2の構造物は繊維の
長さや直径はチユーブの内腔表面と外表面で変わ
らないが、結節の形状がチユーブ外表面では細長
い回転楕円体となつているのに対し内腔表面では
この長さ方向に短かく切断されて回転楕円体の長
軸が極端に短かくなりあるものは球体に近い形を
もつてくる。この第2の構造物では回転楕円体と
なす結節形状の長軸がチユーブ内腔表面では小さ
く、外表面では少なくとも内腔表面の2倍以上の
長さを持つことを特徴とする。
Furthermore, in the second structure to which the present invention is directed, the length and diameter of the fibers are the same between the inner and outer surfaces of the tube, but the shape of the nodule is an elongated spheroid on the outer surface of the tube. On the other hand, on the surface of the lumen, the spheroid is cut short in the longitudinal direction, and the long axis of the spheroid becomes extremely short, resulting in a shape close to that of a sphere. This second structure is characterized in that the long axis of the nodular shape forming the spheroid is small on the inner surface of the tube, and has a length at least twice as long as the inner surface on the outer surface.

本発明の第3の構造物は繊維長さのみならず結
節形状ともにチユーブの内腔表面と外表面で異な
るものを対象としている。この時の繊維長さはチ
ユーブ内腔表面で短かく外表面では少なくとも内
腔表面の1.5倍以上の長さを有し、結節形状は外
表面で長軸が幾分短かくなつた回転楕円体を示す
のに対し内腔表面ではほぼ偏平な形状となると同
時に回転体としての構造を有しなくなる。
The third structure of the present invention is directed to a structure in which not only the fiber length but also the nodule shape differs between the inner and outer surfaces of the tube. At this time, the fiber length is short on the inner surface of the tube, and on the outer surface it is at least 1.5 times longer than the inner surface, and the nodule shape is a spheroid whose long axis is somewhat shortened on the outer surface. On the other hand, the inner cavity surface has a substantially flat shape and at the same time does not have a structure as a rotating body.

これらの三つの構造物における繊維組織はそれ
ぞれ独立ではなく第1の対象構造物のチユーブ内
腔表面繊維組織が第2の対象構造物のチユーブ外
表面組織と一致する。
The fiber structures in these three structures are not independent from each other, and the tube inner surface fiber structure of the first target structure matches the tube outer surface structure of the second target structure.

また第2の対象構造物のチユーブ内腔表面繊維
組織が第3の対象構造物のチユーブ外表面組織と
一致している。
Further, the tube inner surface fibrous structure of the second target structure matches the tube outer surface structure of the third target structure.

チユーブ外表面と内腔表面での繊維径が違う構
造体の効果について詳述する。人工臓器のうちで
管状臓器補綴物、具体的には血管、気管、食道、
胆汁管などは生体への移植を受けた時、血液、体
液あるいは胆汁が管壁から漏れない程に微細な孔
径を持つていなければならない。しかるに患者の
回復過程において移植補綴物の外周に結合組織に
包まれて、次いで外周から侵入した繊維組織で置
換されて管内壁に生起する内膜と強固に連絡する
ためには管壁はかなり大きな孔径を持つている必
要がある。
The effect of a structure with different fiber diameters on the tube outer surface and inner lumen surface will be explained in detail. Among artificial organs, tubular organ prostheses, specifically blood vessels, trachea, esophagus,
When a bile duct is transplanted into a living body, the pore size must be so small that blood, body fluids, or bile will not leak from the duct wall. However, during the patient's recovery process, the canal wall must be quite large in order to be wrapped in connective tissue around the outer periphery of the implanted prosthesis, and then replaced by fibrous tissue that invades from the outer periphery to firmly communicate with the intima that forms on the inner canal wall. It must have a pore size.

この繊維組織が侵入できるために必要な孔径は
少なくとも2μ以上であり、それ以下に小さくな
ると器質化が進まないで停滞してしまうことにな
る。補綴物の管壁が器質化しない限り管壁の内腔
面には内膜が生育し続けることができなくなる。
このため管壁の外表面は5μ以上であることが多
く、さらに大抵はポリエチレンメツシユ、ナイロ
ンメツシユ、ダクロンメツシユ等の織物・編物が
試みられている状態であるが、まだ満足のいくも
のが得られていない。
The pore diameter necessary for this fibrous tissue to penetrate is at least 2 μm or more, and if it becomes smaller than that, the organization will not progress and will stagnate. Unless the canal wall of the prosthesis becomes organized, the intima cannot continue to grow on the lumen surface of the canal wall.
For this reason, the outer surface of the tube wall is often 5μ or more, and in most cases, woven and knitted fabrics such as polyethylene mesh, nylon mesh, and Dacron mesh have been tried, but the results are still not satisfactory. is not obtained.

これらの情況から臓器補綴物としては外表面が
たとえば10μの孔径であり、内腔表面がたとえば
3μ孔径の複合構造物の優位性が了解できるであ
ろう。
Under these circumstances, as an organ prosthesis, the outer surface has a pore diameter of, for example, 10μ, and the inner surface has a pore diameter of, for example, 10μ.
The superiority of the composite structure with a pore size of 3μ can be understood.

工業的用途においても異つた成分の別・濃縮
分割などの機能と同時に大量処理が可能であるこ
とを要求している。別や分割には孔径分布が少
ない程明確に行なえるが、一定時間における処理
量を増加するためには孔の数を増加するかあるい
は管壁の厚みを可能な限り薄くすることが必要と
なる。孔数を大巾に増すことは特定の製造条件の
枠内では非常にむつかしく、また厚みの急激な減
少も機械的強度を悪くするので実用的な手段とな
り得ない欠点を有していた。この様な方面におい
ても内腔表面と外表面の孔径が違なる複合孔径構
造体はその優位性を主張できる。
In industrial applications, it is required to have functions such as separation and concentration division of different components, as well as the ability to process large quantities at the same time. The smaller the pore size distribution, the clearer the separation and division, but in order to increase the throughput in a given time, it is necessary to increase the number of pores or make the tube wall thickness as thin as possible. . It is extremely difficult to significantly increase the number of holes within the framework of specific manufacturing conditions, and a rapid decrease in thickness also impairs mechanical strength, which has the disadvantage that it cannot be a practical means. Even in this field, a composite pore structure in which the pore diameters of the inner and outer surfaces are different can claim its superiority.

もう一つの特性として柔軟性と耐引裂性の関係
についてのべる。
Another characteristic is the relationship between flexibility and tear resistance.

多孔性チユーブの柔軟性はその多孔性の割合に
比例して増加していくが、その時の耐引裂性は逆
に比例して減少していく。引裂強度が低下するこ
とはその使用可能範囲を自ら制限することになつ
てしまう。
The flexibility of a porous tube increases in proportion to its porosity, while its tear resistance decreases in inverse proportion. A decrease in tear strength will limit its usable range.

引裂強度のみを向上させるには多孔性を低下さ
せること、あるいは管壁の厚みを増大することな
どで達成することは不可能ではない。しかしこの
やり方では柔軟性を大巾に低下させてしまうこと
になる。柔軟性を低下させることなく引裂強度を
向上することが本発明の大きな目的であり、チユ
ーブの内腔表面と外表面の繊維構造を変えること
により達成できることが判かつた。
It is not impossible to improve only the tear strength by reducing the porosity or increasing the thickness of the tube wall. However, this approach greatly reduces flexibility. It is a major objective of the present invention to improve tear strength without reducing flexibility, and it has been found that this can be achieved by varying the fiber structure of the inner and outer surfaces of the tube.

特に引裂強度を向上するためには四弗化エチレ
ン樹脂チユーブの管壁を構成する小さな繊維の配
列方向が重要である。小繊維の配列方向はチユー
ブの延伸方向と一致するため、もしチユーブをそ
の長さ方向のにのみ延伸したならば小繊維の方向
もそれと一致する。
In particular, in order to improve the tear strength, the direction in which the small fibers forming the tube wall of the tetrafluoroethylene resin tube are arranged is important. Since the direction in which the fibrils are arranged coincides with the stretching direction of the tube, if the tube is stretched only in its length direction, the direction of the fibrils also coincides with that direction.

もしチユーブの径方向のみの膨張を行なつた時
には小繊維の配列方向もその方向に一致する。そ
れ故引裂強度を向上させる目的のためにはチユー
ブの径方向膨張を可能な限り行なうことによつて
も達成できる。しかし四弗化エチレン樹脂粉末と
液状潤滑剤との混合物を押出機によりチユーブ状
に成形した時、成形金型との接触面で剪断力が発
生しチユーブ押出方向に四弗化エチレン樹脂は繊
維状に配列する。
If the tube is expanded only in the radial direction, the direction in which the fibrils are arranged also coincides with that direction. Therefore, the purpose of increasing the tear strength can also be achieved by expanding the tube in the radial direction as much as possible. However, when a mixture of tetrafluoroethylene resin powder and liquid lubricant is molded into a tube shape using an extruder, shearing force is generated at the contact surface with the mold, and the tetrafluoroethylene resin becomes fibrous in the tube extrusion direction. Arrange in.

この繊維状配列はチユーブの長さ方向には充分
進行してかなりの強度を有するようになるが、チ
ユーブ径方向にはほとんど繊維状配列が進行して
おらずそのために強度は長さ方向に比較して1/3
〜1/5程度しか持つていない。この結果チユーブ
の径方向のみの膨張によつて多孔性チユーブを得
ることは不可能ではないが、割れたりするかなり
の不良品の発生を覚悟しなければならない。
This fibrous arrangement progresses sufficiently in the length direction of the tube and has considerable strength, but almost no fibrous arrangement progresses in the radial direction of the tube, so the strength is lower than that in the length direction. then 1/3
I only have ~1/5 of it. As a result, although it is not impossible to obtain a porous tube by expanding only in the radial direction of the tube, one must be prepared for the occurrence of a considerable number of defective products that may be cracked.

本発明ではまずチユーブの長さ方向に一定の割
合で延伸することによりチユーブ長さ方向の小繊
維をつくり、次いで径方向の膨張を行つてチユー
ブ径方向の小繊維を発生させることにより柔軟性
と引裂強度の優れた多孔性チユーブが得られる。
勿論径方向の膨張を先に行つたのち長さ方向の延
伸を行つても同一構造物が得られるが、長さ方向
の延伸を先にする方が品質的には安定したものが
得られる。
In the present invention, the tube is first stretched at a constant rate in the length direction of the tube to create small fibers in the length direction of the tube, and then expanded in the radial direction to generate small fibers in the radial direction of the tube, thereby improving flexibility. A porous tube with excellent tear strength is obtained.
Of course, the same structure can be obtained by expanding in the radial direction first and then stretching in the length direction, but a product with more stable quality can be obtained by stretching in the length direction first.

径方向の膨張はチユーブの周囲を減圧にするこ
とによつて連続的に行なえる。
Radial expansion can be achieved continuously by creating a vacuum around the tube.

長さ方向と径方向の延伸・膨張の程度に応じて
その方向に生ずる小繊維の数・長さ・太さ等が変
化するのは当然であり、所望する多孔度・孔径・
柔軟性・耐引裂強度の値に応じて適宜選択するこ
とが出来る。この延伸と膨張の割合が拮抗すると
球状の結節を中心に小繊維の方向は放射状に均一
分布する。それにもかかわらず繊維の方向はチユ
ーブの内腔表面と外表面で違つた方向となる。
It is natural that the number, length, thickness, etc. of fibrils produced in the longitudinal and radial directions change depending on the degree of stretching/expansion in that direction, and the desired porosity, pore diameter, etc.
It can be appropriately selected depending on the values of flexibility and tear resistance. When the rates of stretching and expansion are balanced, the direction of the fibrils is uniformly distributed radially around the spherical nodule. Nevertheless, the orientation of the fibers will be different on the inner and outer surfaces of the tube.

延伸又は膨張の一方が他方より大きい時にはそ
の大きい方向の小繊維が長くかつ数も多いがその
直角方向は逆に短かく数も少ない。
When one of the stretching and expansion is larger than the other, the fibrils in the larger direction are longer and more numerous, but conversely the fibrils in the right direction are shorter and fewer in number.

延伸と膨張の二方向に処理を行つたものの結節
の大きさ及び繊維の太さは延伸又は膨張のみの一
方向処理を行つたものと比較すると非常に変化し
ていることが電子顕微鏡による観察で確認でき
る。特にその繊維方向は内腔表面の方が外表面よ
りも強く放射状に分布していることがわかる。
Observation using an electron microscope shows that the size of nodules and the thickness of fibers treated in two directions (stretching and expansion) are significantly different compared to those treated in one direction only by stretching or expansion. Can be confirmed. In particular, it can be seen that the fiber direction is more strongly distributed radially on the inner surface than on the outer surface.

延伸する割合によつて結節の大きさは順次小さ
くなつていくが、その形状は一方向のみの時には
細長い回転楕円体をしているが二方向への処理を
受けた時には結節の大きさが一方向の時の1/3〜
1/10にも小さくなると同時にほゞ球状の形態をと
ることが多い。
The size of the nodule gradually decreases depending on the rate of stretching, but when it is stretched in only one direction, it is an elongated spheroid, but when it is stretched in two directions, the size of the nodule becomes uniform. 1/3 of the direction
It often becomes smaller by 1/10 and at the same time takes a nearly spherical shape.

繊維の太さは一方向の時には延伸する割合によ
らずほゞ0.5〜1μの一定値を示しているが、これ
を二方向に処理することにより1/3〜1/5の値にま
で細くなりその分だけ数多くの繊維が存在するこ
とになる。
When the fibers are stretched in one direction, they exhibit a constant value of 0.5 to 1μ regardless of the stretching ratio, but by processing the fibers in two directions, the thickness can be reduced to 1/3 to 1/5 of that value. Therefore, there will be a correspondingly large number of fibers.

このように本発明の第1の対象構造物は柔軟性
と耐引裂性において非常に秀れた特性を有し、従
来全く知られていなかつた構造物である。
As described above, the first target structure of the present invention has extremely excellent properties in terms of flexibility and tear resistance, and is a structure completely unknown heretofore.

第2、第3の対象構造物も秀れた柔軟性を示し
外径6.0mm、内径5.0mmのチユーブでは20g以下の
荷重で、大抵の時は10gの荷重下で完全に圧縮体
に変形してしまう。この圧縮物の気体や液体に対
するシール性は従来の耐熱、耐薬品性のガスケツ
トやパツキングの用途に充分耐えるものであり大
径フランジ面のシール用材料として有用である。
銅やアルミ製の金属パツキングは耐熱性において
秀れているがシール性を獲得するためには数Kg以
上の荷重で締める必要があり、またこの荷重によ
り塑性流動が生じるため数回の使用を行つたもの
は締めつけによるシール性が極端に悪くなる。
The second and third target structures also showed excellent flexibility, and a tube with an outer diameter of 6.0 mm and an inner diameter of 5.0 mm completely deformed into a compressed body under a load of 20 g or less, and in most cases under a load of 10 g. I end up. The sealing properties of this compressed product against gas and liquid are sufficient to withstand the use of conventional heat-resistant and chemical-resistant gaskets and packing, and it is useful as a sealing material for large-diameter flange surfaces.
Metal packing made of copper or aluminum has excellent heat resistance, but in order to achieve sealing properties, it is necessary to tighten it with a load of several kilograms or more, and this load causes plastic flow, so it may be necessary to use it several times. If the material is tight, the sealing performance will be extremely poor.

四弗化エチレン樹脂のヒモ状シール材を使われ
ているが、これは熱処理を全く行つていないた
め、シール用途に一回利用するだけの使い捨て製
品といわざるを得ない。
A string-shaped sealing material made of tetrafluoroethylene resin is used, but as it has not undergone any heat treatment, it must be considered a disposable product that can only be used once for sealing purposes.

本発明の第2、第3の対象構造物はチユーブ外
表面を少なくとも327℃以上の熱処理を行つてい
るので、シール用途に利用した後もその構造の変
化が少なく、またわずかの締めつけ力によつて完
全なシールを達成できるという特徴を有してい
る。
Since the second and third target structures of the present invention have undergone heat treatment on the outer surface of the tube at a temperature of at least 327°C, there is little change in the structure even after they are used for sealing purposes, and even with a small tightening force. It has the characteristic that a perfect seal can be achieved.

ここで延伸・膨張および焼結の際の温度につい
て述べる必要がある。
Here, it is necessary to mention the temperatures during stretching, expansion, and sintering.

延伸や膨張においてはその操作によつてチユー
ブは少なくとも処理前とは違つた寸法・形状とな
るが、この変形を生ぜしめるため少なくとも外部
から力を加えねばならない。この外力はチユーブ
の温度が高い程少なくなり、低い程大きくなつて
いく傾向は一般の熱加塑プラスチツクと同様であ
る。この変形に要する外力はチユーブ自身が押出
成形された時繊維状に配向することに依り保有す
る強度と比較されるものである。
In stretching or expanding, the tube becomes at least in a different size and shape than before the treatment, and at least an external force must be applied to cause this deformation. This external force decreases as the temperature of the tube increases, and increases as the tube temperature decreases, as in general thermoplastic plastics. The external force required for this deformation is compared to the strength that the tube itself possesses due to its fibrous orientation when extruded.

押出成形によつて蓄積された強度は押出成形の
条件には大きく依存するが成型後の温度雰囲気な
どにはあまり依存しない。
The strength accumulated through extrusion molding largely depends on the conditions of extrusion molding, but it does not depend much on the temperature and atmosphere after molding.

チユーブの延伸や膨張などの変形を行なう温度
がある一定の値以下では変形に要する外力の方が
チユーブの強度よりも大きく、そのため変形中に
破損するものが増えて来る。一方ある温度以上に
なると変形のための外力がチユーブの強度よりも
小さくなり破損する割合は急激に減少していく。
When the temperature at which the tube undergoes deformation such as stretching or expansion is below a certain value, the external force required for deformation is greater than the strength of the tube, and as a result, more parts break during deformation. On the other hand, when the temperature exceeds a certain point, the external force for deformation becomes smaller than the strength of the tube, and the rate of breakage rapidly decreases.

このためチユーブの変形を行なうには押出成形
条件に応じて下限の温度が存在することになる。
Therefore, there is a lower temperature limit for deforming the tube depending on the extrusion molding conditions.

同じ傾向が延伸・膨張などの変形速度にも存在
する。変形速度が大きくなると変形に要する外力
が大きくなり、そのためチユーブを破損せしめな
いためには更に高い温度に加熱することが必要と
なる。
The same tendency exists for deformation rates such as stretching and expansion. As the deformation rate increases, the external force required for deformation increases, and therefore it is necessary to heat the tube to a higher temperature in order to prevent it from being damaged.

チユーブの押出成形条件に応じてチユーブの保
有強度が変わるので変形における最低温度を明確
に指定できないが、当業界の専問家には容易に判
定できるものである。
Since the retained strength of the tube changes depending on the extrusion molding conditions of the tube, the minimum temperature at which deformation occurs cannot be clearly specified, but it can be easily determined by experts in the industry.

焼結という工程は延伸されたあるいは延伸と膨
張処理を受けたチユーブを収縮しない様に固定し
ながら少なくとも327℃以上の温度に加熱するこ
とを意味している。この時チユーブ内腔部分に空
気を流すことによつて内表面を冷却しながら外部
加熱することによつてチユーブ内腔表面と外表面
の多孔性繊維構造を変えることが出来る。チユー
ブ内腔表面を流す空気の量を増加するか、あるい
は空気の温度を下げることによつてチユーブの外
表面は327℃以上に加熱されるが、内腔表面を327
℃以下の加熱状態にすることも出来る。この様な
チユーブは外表面のみは焼結されているものの内
腔表面は未焼結状態であり、繊維と結節の形状や
大きさが内・外表面で大きく違つてくる。
The process of sintering means heating the stretched or stretched and expanded tube to a temperature of at least 327° C. while fixing it so that it does not shrink. At this time, the porous fiber structure of the inner surface and outer surface of the tube can be changed by externally heating the inner surface while cooling the inner surface by flowing air into the inner surface of the tube. By increasing the amount of air flowing over the tube lumen surface or lowering the temperature of the air, the outer surface of the tube can be heated above 327°C, but the lumen surface can be heated to 327°C or higher.
It can also be heated to temperatures below ℃. Although only the outer surface of such a tube is sintered, the inner surface is unsintered, and the shape and size of the fibers and nodules differ greatly between the inner and outer surfaces.

一方チユーブ内腔表面を流す空気量を減少する
かあるいはその空気の温度を上昇する(具体的に
は炉の長さを増す又は炉の温度上昇)ことによつ
てチユーブ内腔部分を327℃以上に加熱すること
も出来るが、この時には外表面の樹脂繊維が327
℃以上の温度に長時間さらされることとなつて内
表面と同じ繊維構造ー特に太さーであつたものが
少なくとも2本以上合体して次第に太くなつてい
く。
On the other hand, by reducing the amount of air flowing over the surface of the tube lumen or increasing the temperature of the air (specifically, by increasing the length of the furnace or increasing the temperature of the furnace), it is possible to It is also possible to heat the resin fibers on the outer surface to 327
As it is exposed to temperatures above ℃ for a long period of time, at least two or more fibers that have the same fiber structure as the inner surface, especially the thickness, coalesce and gradually become thicker.

内腔部分を流す冷却空気量と外部からの熱供給
量を変化させることによつてチユーブの内表面構
造部分と外表面構造部分の厚さが変わつて来る。
By changing the amount of cooling air flowing through the inner cavity and the amount of heat supplied from the outside, the thicknesses of the inner and outer surface structures of the tube can be varied.

繊維の太さや結節の形状の前述の様にチユーブ
の温度に依つて非常に変化する。延伸や膨張を受
けているチユーブの温度が327℃以下の状態を第
1図に示している。チユーブ管壁の全面にわたり
小さな亀裂1が多数発生している。その亀裂1の
中には数多くの繊維2が延伸や膨張の方向と平行
にみられる。第1図およびその後の電子顕微鏡写
真は400倍の倍率に対応している。
As mentioned above, the thickness of the fibers and the shape of the nodules vary greatly depending on the temperature of the tube. Figure 1 shows a state where the temperature of the tube undergoing stretching and expansion is below 327°C. Many small cracks 1 have occurred over the entire surface of the tube wall. A large number of fibers 2 are seen in the crack 1 parallel to the direction of stretching and expansion. Figure 1 and subsequent electron micrographs correspond to a magnification of 400x.

327℃以上への加熱処理を受けない結節3はそ
の界面を亀裂1によつて仕切られわている様に非
常に突起の多い複雑な形状をしている。
Nodules 3 which are not subjected to heat treatment at 327° C. or higher have a complex shape with many protrusions, as if their interfaces are partitioned by cracks 1.

第2図は延伸や膨張を受けたチユーブが327℃
以上まで加熱されているが未だ完全には四弗化エ
チレン樹脂を融解させていない状態を示してい
る。この状態になると327℃以下では複雑な形状
をして結節3がかなり融解して丸味を示している
が、それでも繊維2との接着面はまだ溶着してい
ないで圧着されたような状態にすぎない。しかし
繊維2の長さは第1図よりもはるかに成長して長
くなつている。
Figure 2 shows the tube that has been stretched and expanded at 327°C.
This shows a state in which the tetrafluoroethylene resin has not been completely melted even though it has been heated to the above level. In this state, below 327°C, the nodule 3 has a complex shape and is considerably melted and has a rounded appearance, but the bonding surface with the fiber 2 has not yet been welded and is only in a crimped state. do not have. However, the length of the fiber 2 has grown much longer than in FIG.

そのため第1図の「亀裂1が生じた」状態から
「繊維2が結節3によつて互に連絡された」状態
へと変化している。
Therefore, the state in which "a crack 1 has occurred" in FIG. 1 changes to the state in which "fibers 2 are interconnected by knots 3."

第3図は結節3が完全に溶解しそのため繊維2
との接着部分も溶着して繊維2が延伸や膨張を受
けた方向に整然と配列する。
Figure 3 shows that nodule 3 has completely dissolved and therefore fibers 2
The adhesive portions are also welded, and the fibers 2 are arranged in an orderly manner in the direction in which they are stretched or expanded.

繊維の長さや太さについては第2図と第3図の
間でほとんど変わらないが、結節部分の形状には
かなりの相違が認められる。
Although the length and thickness of the fibers are almost the same between Figures 2 and 3, there is a considerable difference in the shape of the nodule.

第4図は更に長時間327℃以上の熱処理を行つ
た状態であり結節3は第3図とほとんど変わらな
いが、繊維2の太さが第3図の時よりも太くなつ
ており、かつ繊維2の数も減少している。
Figure 4 shows a state where the heat treatment was performed at 327°C or higher for an even longer period of time, and the knot 3 is almost the same as in Figure 3, but the thickness of the fiber 2 is thicker than in Figure 3, and the fiber The number of 2 is also decreasing.

本発明の対象とするチユーブ状多孔性構造物は
外表面と内腔表面が第2図と第1図、第3図と第
2図、第4図と第3図のそれぞれの状態になつた
複合繊維構造物を全て包含している。
The tubular porous structure that is the subject of the present invention has its outer surface and inner cavity surface in the states shown in FIGS. 2 and 1, FIG. 3 and 2, and FIG. 4 and 3, respectively. Includes all composite fiber structures.

第5図は第3図と同じ熱処理を受けた状態であ
るが延伸と膨張を受けたために結節3の間に張ら
れた繊維2の方向が結節3を中心に放射状に分布
している。
FIG. 5 shows the same heat treatment as in FIG. 3, but because the fibers 2 have been stretched and expanded, the directions of the fibers 2 stretched between the nodules 3 are distributed radially around the nodules 3.

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

第1図〜第5図は本発明の多孔性四弗化エチレ
ン樹脂チユーブの電子顕微鏡写真である。 1は亀裂、2は繊維、3は結節である。
1 to 5 are electron micrographs of porous tetrafluoroethylene resin tubes of the present invention. 1 is a crack, 2 is a fiber, and 3 is a nodule.

Claims (1)

【特許請求の範囲】 1 多孔性四弗化エチレン樹脂よりなるチユーブ
において、該多孔性四弗化エチレン樹脂は繊維に
よつて互に連結された結節よりなるミクロ構造を
有し、かつ該チユーブの内表面の繊維方向が外表
面の繊維方向よりも放射状に分布している ことを特徴とする多孔性四弗化エチレン樹脂チユ
ーブ。 2 多孔性四弗化エチレン樹脂チユーブの外表面
における結節の長軸が、内表面における結節の長
軸よりも少なくとも2倍以上の長さを持つことを
特徴とする特許請求の範囲第1項の多孔性四弗化
エチレン樹脂チユーブ。 3 液状潤滑剤を含む未焼結の四弗化エチレン樹
脂混和物をチユーブ状に成形したのち、少なくと
もチユーブの長さ方向に延伸した状態で少なくと
もチユーブの外表面が327℃以上で、かつチユー
ブの内表面がチユーブの外表面よりも低い温度に
なるように加熱することを特徴とする多孔性四弗
化エチレン樹脂チユーブの製造方法。 4 少なくともチユーブの長さ方向に延伸された
状態で、少なくともチユーブの外表面が327℃以
上に加熱される時、該チユーブの外側を減圧する
ことを特徴とする特許請求の範囲第3項の多孔性
四弗化エチレン樹脂チユーブの製造方法。 5 チユーブの外表面より加熱し、チユーブの内
腔部分に冷却空気を供給することを特徴とする特
許請求の範囲第3項の多孔性四弗化エチレン樹脂
チユーブの製造方法。
[Scope of Claims] 1. A tube made of porous tetrafluoroethylene resin, wherein the porous tetrafluoroethylene resin has a microstructure consisting of nodes interconnected by fibers, and A porous tetrafluoroethylene resin tube characterized in that the fiber direction on the inner surface is distributed more radially than the fiber direction on the outer surface. 2. The long axis of the nodules on the outer surface of the porous tetrafluoroethylene resin tube is at least twice as long as the long axis of the nodules on the inner surface. Porous tetrafluoroethylene resin tube. 3. After molding an unsintered tetrafluoroethylene resin mixture containing a liquid lubricant into a tube shape, at least the outside surface of the tube is at least 327°C when stretched in the length direction of the tube, and the temperature of the tube is A method for producing a porous tetrafluoroethylene resin tube, the method comprising heating the inner surface to a lower temperature than the outer surface of the tube. 4. The porous tube according to claim 3, characterized in that when at least the outer surface of the tube is heated to 327° C. or higher while the tube is stretched in the longitudinal direction, the outside of the tube is depressurized. A method for producing polytetrafluoroethylene resin tubes. 5. The method for producing a porous tetrafluoroethylene resin tube according to claim 3, which comprises heating from the outer surface of the tube and supplying cooling air to the inner cavity of the tube.
JP4967176A 1975-12-24 1976-04-29 Porous ethylene tetrafluoride resin tube and method of its manufacturing Granted JPS52132078A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP4967176A JPS52132078A (en) 1976-04-29 1976-04-29 Porous ethylene tetrafluoride resin tube and method of its manufacturing
US05/751,876 US4082893A (en) 1975-12-24 1976-12-17 Porous polytetrafluoroethylene tubings and process of producing them
CA268,375A CA1046433A (en) 1975-12-24 1976-12-21 Porous polytetrafluoroethylene tubings and process of producing them
DE2658656A DE2658656C3 (en) 1975-12-24 1976-12-23 Process for producing a porous polytetrafluoroethylene tube
FR7639090A FR2336622A1 (en) 1975-12-24 1976-12-24 POROUS POLYTETRAFLUOROETHYLENE TUBING, AND PROCESS FOR PREPARATION
GB5399176A GB1577326A (en) 1976-04-29 1977-01-17 Porous polytetrafluoroethylene tubing
US06/047,470 US4234535A (en) 1976-04-29 1979-06-11 Process for producing porous polytetrafluoroethylene tubings

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4967176A JPS52132078A (en) 1976-04-29 1976-04-29 Porous ethylene tetrafluoride resin tube and method of its manufacturing

Publications (2)

Publication Number Publication Date
JPS52132078A JPS52132078A (en) 1977-11-05
JPS647856B2 true JPS647856B2 (en) 1989-02-10

Family

ID=12837624

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4967176A Granted JPS52132078A (en) 1975-12-24 1976-04-29 Porous ethylene tetrafluoride resin tube and method of its manufacturing

Country Status (2)

Country Link
JP (1) JPS52132078A (en)
GB (1) GB1577326A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4743480A (en) * 1986-11-13 1988-05-10 W. L. Gore & Associates, Inc. Apparatus and method for extruding and expanding polytetrafluoroethylene tubing and the products produced thereby
JP5204384B2 (en) * 2006-05-19 2013-06-05 富士フイルム株式会社 Crystalline polymer microporous membrane, method for producing the same, and filter for filtration
JP5220369B2 (en) * 2007-09-04 2013-06-26 富士フイルム株式会社 Crystalline polymer microporous membrane, method for producing the same, and filter for filtration
JP2009066552A (en) * 2007-09-14 2009-04-02 Chung Yuan Christian Univ Method and apparatus for forming asymmetric membrane material
KR102218062B1 (en) * 2018-10-18 2021-02-19 주식회사 엘지화학 Porous fluorine resin film and method for preparing the same

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA962021A (en) * 1970-05-21 1975-02-04 Robert W. Gore Porous products and process therefor
JPS5755063Y2 (en) * 1974-01-30 1982-11-29

Also Published As

Publication number Publication date
GB1577326A (en) 1980-10-22
JPS52132078A (en) 1977-11-05

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