JPS60104319A - Polytetrafluoroethylene porous material and manufacture thereof - Google Patents
Polytetrafluoroethylene porous material and manufacture thereofInfo
- Publication number
- JPS60104319A JPS60104319A JP58211737A JP21173783A JPS60104319A JP S60104319 A JPS60104319 A JP S60104319A JP 58211737 A JP58211737 A JP 58211737A JP 21173783 A JP21173783 A JP 21173783A JP S60104319 A JPS60104319 A JP S60104319A
- Authority
- JP
- Japan
- Prior art keywords
- molding
- porous
- less
- molecular weight
- polytetrafluoroethylene
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C67/00—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
- B29C67/20—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 for porous or cellular articles, e.g. of foam plastics, coarse-pored
- B29C67/205—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 for porous or cellular articles, e.g. of foam plastics, coarse-pored comprising surface fusion, and bonding of particles to form voids, e.g. sintering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/22—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length
- B29C43/24—Calendering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/06—Rod-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2027/00—Use of polyvinylhalogenides or derivatives thereof as moulding material
- B29K2027/12—Use of polyvinylhalogenides or derivatives thereof as moulding material containing fluorine
- B29K2027/18—PTFE, i.e. polytetrafluorethene, e.g. ePTFE, i.e. expanded polytetrafluorethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
Abstract
Description
【発明の詳細な説明】
(技術分野)
本発明は、ポリテトラフルオロエチレン(以下PTIE
と略す)からなる多孔質体及びその製造方法に関するも
のである。Detailed Description of the Invention (Technical Field) The present invention relates to polytetrafluoroethylene (hereinafter referred to as PTIE).
The present invention relates to a porous body made of a porous material (hereinafter referred to as "porous body") and a method for manufacturing the same.
(従来技術とそO1問題点)
PTF Eは耐熱性、耐薬品性等にきわめてすぐれたプ
ラスチックであり、この多孔質体は腐食性物質の精密濾
過用フィルター、電解用隔膜、また撥水性を利用しての
各種呼吸弁等、最近広範囲の用途に用いられるようにな
ってきている。(Prior art and its O1 problem) PTF E is a plastic with excellent heat resistance and chemical resistance, and this porous material is used as a filter for precision filtration of corrosive substances, a diaphragm for electrolysis, and for its water repellency. Recently, it has come to be used in a wide range of applications, such as various breathing valves.
このようなPTF E多孔質体を製造する方法としては
、従来から未焼成のPTF E成形体i PTFEの融
点以下で延伸して多孔質化し、このあとP T F E
の結晶融点以上の温度に加熱して焼成する方法が知られ
ている。Conventionally, the method for manufacturing such a PTF E porous body is to stretch an unfired PTF E molded body i at a temperature below the melting point of PTFE to make it porous, and then to make the PTF E porous body.
A method of firing by heating to a temperature higher than the crystal melting point of is known.
この方法は、比較的高い気孔率が得られるという利点が
ある反面、その孔径は0.2μm程度が下限゛であり、
より小さい孔径の多孔質体を得ることは困難であった。Although this method has the advantage of obtaining relatively high porosity, the lower limit of the pore size is approximately 0.2 μm;
It has been difficult to obtain porous bodies with smaller pore sizes.
本発明者らは、このPTFE多孔質体の孔径のさらに小
さいものを得るために種々検討した結果、原料として用
いるPTF Eファインパウダーの数平均分子量(以下
分子量と略す〕の極めて高いものを用いる事によって微
小孔径化が可能となることを見い出した。As a result of various studies in order to obtain a porous PTFE material with an even smaller pore diameter, the inventors of the present invention found that the PTFE fine powder used as a raw material had an extremely high number average molecular weight (hereinafter abbreviated as molecular weight). We have discovered that it is possible to make the pores smaller.
、(発明の内容)
本発明の特徴は、原料となるファインパウダーとして分
子量1000万以上のものを用いる事にある。このよう
なファインパウダーを用いることによって、孔径0.1
μm以下で、かつ気孔率が4096以上のPTFE多孔
質体を得る事に成功した。(Contents of the Invention) The feature of the present invention is that a fine powder having a molecular weight of 10 million or more is used as a raw material. By using such fine powder, the pore size can be reduced to 0.1
We succeeded in obtaining a PTFE porous body with a porosity of 4096 or more and a porosity of 4096 or less.
本発明は多孔質体の形状としてフィルムをはじめチュー
ブ、ロッド、ヤーン等に適用することができる。The present invention can be applied to films, tubes, rods, yarns, etc. as porous bodies.
また、このような原料を用いれば孔径が小さくなるとい
うのみならず、引張強度が大きくなるという効果もある
ことが判った。It has also been found that the use of such raw materials not only reduces the pore diameter but also increases the tensile strength.
本発明に於て分子量とは、PTF EをASTM−D−
1457−56T に示された一定の熱処理条件で成形
した試料の比重と次式の関係が成立するものである。In the present invention, molecular weight refers to PTFE as ASTM-D-
1457-56T, the following equation holds true:
SSG == −0,05791ogMn+2.611
3ここでSSGは上記の比重を表わし、Mnは分子量を
表わす。SSG == -0,05791ogMn+2.611
3 Here, SSG represents the above-mentioned specific gravity, and Mn represents the molecular weight.
次に本発明の詳細について説明する。Next, details of the present invention will be explained.
本発明の方法によって多孔質体を得るための第一の工程
は、本発明の特徴である分子量1,0011万以上のP
TFEファインパウダーと液状潤滑剤を混合する工程で
ある。この潤滑剤は従来から公知のものでよく、例えば
ソルベントナフサ等の炭化水素類、トルエン等の芳昏族
炭化水素類等が用いられ、その量はPTFEに対して1
5〜50重量%が適当である。また必要に応じて着色の
ための顔料等の充填剤を加えることもできる。The first step for obtaining a porous body by the method of the present invention is to use P with a molecular weight of 100.11 million or more, which is a feature of the present invention.
This is a process of mixing TFE fine powder and liquid lubricant. This lubricant may be a conventionally known lubricant; for example, hydrocarbons such as solvent naphtha, aromatic hydrocarbons such as toluene, etc. are used, and the amount thereof is 1% relative to PTFE.
5 to 50% by weight is suitable. Further, a filler such as a pigment for coloring can be added if necessary.
次にこの混合物は押出または圧延または両者を組み合わ
せた工程を含む方法で成形される。例えばロッド、チュ
ーブ、ストリップ、シート等はラム式押出機を用いて行
なうことができ、また圧延によってシート、フィルムを
成形することもできる。This mixture is then shaped by a process involving extrusion or rolling or a combination of both. For example, rods, tubes, strips, sheets, etc. can be formed using a ram extruder, and sheets and films can also be formed by rolling.
また、これらは押出、あるいは圧延前に予め圧縮成形す
ることもできる。Moreover, these can also be compression molded before extrusion or rolling.
このようにして得られた潤滑剤を含む未焼成成形品は次
に少くとも一方向に延伸される。この延伸は潤滑剤を含
む状態でもまた蒸発、抽出等によって除去した後でも行
う事ができる。The green molded article containing the lubricant thus obtained is then stretched in at least one direction. This stretching can be carried out with the lubricant present or after its removal by evaporation, extraction, etc.
フィルムの延伸を例にとると、この延伸工程は2本のロ
ールの回転速度を変える事によって行なわれるが、本発
明の目的である0、2μm以下の孔径のものを得るため
には、延伸率200%以上であることが好ましい。Taking film stretching as an example, this stretching process is carried out by changing the rotational speed of two rolls, but in order to obtain a pore size of 0.2 μm or less, which is the objective of the present invention, the stretching rate must be adjusted. It is preferable that it is 200% or more.
このような方法によって0.2μm以下の微小な孔径の
多孔質体が得られるが、さらにこの多孔質構造を安定・
強固にするため、このあと熱収縮防止状態にて約327
°C以上に加熱・焼成することが好ましい。Although a porous body with a minute pore size of 0.2 μm or less can be obtained by such a method, it is possible to further stabilize and stabilize this porous structure.
To make it stronger, it will be heated to about 327mm in a heat shrinkage prevention state.
It is preferable to heat and bake at a temperature of .degree. C. or higher.
ここで、熱収縮防止状態とは収縮を完全に防止した状態
だけでなく一部収縮を許す状態をも含むものとする。Here, the state of preventing heat shrinkage includes not only a state where shrinkage is completely prevented but also a state where some shrinkage is allowed.
(実施例1)
数平均分子量2000万のPTFE ファインパウダー
1000g に石油留分(沸点150〜250”に)を
200g加え混合した後、予備成形し、次いで押出圧5
゜Ky/an”の圧力で中3QQm、厚さ15su の
板状成形体を得た。(Example 1) 200 g of petroleum fraction (boiling point 150-250'') was added to 1000 g of PTFE fine powder with a number average molecular weight of 20 million, mixed, preformed, and then extruded under an extrusion pressure of 5
A plate-shaped molded product having a medium size of 3QQm and a thickness of 15su was obtained under a pressure of .degree.Ky/an''.
このものを押出方向とは直角方向にカレンダーロールに
通し、厚さ0.3飢の未焼成フィルムを得た。This material was passed through a calender roll in a direction perpendicular to the extrusion direction to obtain an unfired film with a thickness of 0.3 mm.
次いでこのフィルムをトリクレンに3時間浸漬しオイル
を除去した。Next, this film was immersed in trichlene for 3 hours to remove the oil.
さらにこのあとこの未焼成フィルムをロールによって延
伸した。このときロール温度は300″C,ロー ル間
隔は1〃晶、延伸倍率は600%、サプライ側ロールス
ピードは6 m 7分 とした。Furthermore, this unfired film was then stretched using a roll. At this time, the roll temperature was 300''C, the roll interval was 1 crystal, the stretching ratio was 600%, and the supply side roll speed was 6 m 7 minutes.
次いでこの延伸フィルムを鏡面のステンレス板に密着さ
せ380°Cで20分熱処理し、焼結した。Next, this stretched film was brought into close contact with a mirror-finished stainless steel plate and heat-treated at 380°C for 20 minutes to sinter it.
このフィルムの孔径を水銀圧入法によって測定した所平
均孔径は0.05μmであった。また気孔率は50%で
あった。The average pore diameter of this film was measured by mercury porosimetry and was found to be 0.05 μm. Moreover, the porosity was 50%.
(比較例1)
数平均分子量200万のポリテトラフルオロエチレンフ
ァインパウダー1000 gに石油留分(沸点150〜
250 ’C)を200g加え、以下実施例1と同様の
方法で焼結フィルムを製作した。(Comparative Example 1) Petroleum distillate (boiling point 150~
A sintered film was produced in the same manner as in Example 1 by adding 200 g of 250'C).
このフィルムの平均孔径は0.30μm、気孔率は55
%であった。The average pore size of this film is 0.30 μm, and the porosity is 55
%Met.
Claims (1)
オロエチレンから成り、平均孔径が0.2μm以下であ
ることを特徴とするポリテトラフルオロエチレン多孔質
体。 (2、特許請求の範囲第1項記載の多孔質体を製造する
方法であって、数平均分子量が1000万以上のポリテ
トラフルオロエチレン・ファインパウダーと液状潤滑剤
との混合物を押出及び/又は圧延を含む方法にて成形し
た後、液状潤滑剤を除去しあるいは除去せずして、該成
形体を約327°C以下の温度で少なくとも一方向シて
延伸し、その後必要に応じ、熱収縮防止状態にて約32
7°C以上の温度で焼成することを特徴とするポリテト
ラフルオロエチレン多孔質体の製造方法。 (3)延伸率が200%以上であることを特徴とする特
許請求の範囲第2項記載のポリテトラフルオロエチレン
多孔質体の製造方法。Scope of Claims: (1) A polytetrafluoroethylene porous material comprising polytetrafluoroethylene having a number average molecular weight of 10 million or more and having an average pore diameter of 0.2 μm or less. (2. A method for producing a porous body according to claim 1, comprising extruding and/or After forming by a method including rolling, the formed object is stretched in at least one direction at a temperature of about 327°C or less, with or without removing the liquid lubricant, and then, if necessary, heat-shrinked. Approximately 32 in prevention state
A method for producing a polytetrafluoroethylene porous body, which comprises firing at a temperature of 7°C or higher. (3) The method for producing a porous polytetrafluoroethylene material according to claim 2, wherein the stretching ratio is 200% or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58211737A JPS60104319A (en) | 1983-11-10 | 1983-11-10 | Polytetrafluoroethylene porous material and manufacture thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58211737A JPS60104319A (en) | 1983-11-10 | 1983-11-10 | Polytetrafluoroethylene porous material and manufacture thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60104319A true JPS60104319A (en) | 1985-06-08 |
Family
ID=16610749
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58211737A Pending JPS60104319A (en) | 1983-11-10 | 1983-11-10 | Polytetrafluoroethylene porous material and manufacture thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60104319A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5026513A (en) * | 1987-10-19 | 1991-06-25 | W. L. Gore & Associates, Inc. | Process for making rapidly recoverable PTFE |
US5308664A (en) * | 1987-10-19 | 1994-05-03 | W. L. Gore & Associates, Inc. | Rapidly recoverable PTFE and process therefore |
JPH0832791B2 (en) * | 1989-02-02 | 1996-03-29 | ダブリュ.エル.ゴア アンド アソシエーツ,インコーポレイティド | Highly breathable stretched polytetrafluoroethylene membrane and method for producing the same |
JP2011178970A (en) * | 2010-03-04 | 2011-09-15 | Nitto Denko Corp | Method of manufacturing polytetrafluoroethylene porous film and air-permeable member |
JP2012514549A (en) * | 2009-01-09 | 2012-06-28 | ニンボ スーパーブライト テクノロジー カンパニー リミテッド | Seamless edge sealing method of fluororesin coating |
EP3632971A4 (en) * | 2017-05-31 | 2021-03-03 | Nitto Denko Corporation | Polytetrafluoroethylene porous film |
-
1983
- 1983-11-10 JP JP58211737A patent/JPS60104319A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5026513A (en) * | 1987-10-19 | 1991-06-25 | W. L. Gore & Associates, Inc. | Process for making rapidly recoverable PTFE |
US5308664A (en) * | 1987-10-19 | 1994-05-03 | W. L. Gore & Associates, Inc. | Rapidly recoverable PTFE and process therefore |
JPH0832791B2 (en) * | 1989-02-02 | 1996-03-29 | ダブリュ.エル.ゴア アンド アソシエーツ,インコーポレイティド | Highly breathable stretched polytetrafluoroethylene membrane and method for producing the same |
JP2012514549A (en) * | 2009-01-09 | 2012-06-28 | ニンボ スーパーブライト テクノロジー カンパニー リミテッド | Seamless edge sealing method of fluororesin coating |
JP2011178970A (en) * | 2010-03-04 | 2011-09-15 | Nitto Denko Corp | Method of manufacturing polytetrafluoroethylene porous film and air-permeable member |
EP3632971A4 (en) * | 2017-05-31 | 2021-03-03 | Nitto Denko Corporation | Polytetrafluoroethylene porous film |
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