JPH0578497A - Production of ptfe polymer alloy - Google Patents
Production of ptfe polymer alloyInfo
- Publication number
- JPH0578497A JPH0578497A JP24352991A JP24352991A JPH0578497A JP H0578497 A JPH0578497 A JP H0578497A JP 24352991 A JP24352991 A JP 24352991A JP 24352991 A JP24352991 A JP 24352991A JP H0578497 A JPH0578497 A JP H0578497A
- Authority
- JP
- Japan
- Prior art keywords
- ptfe
- fluorine
- polymer
- alloy
- inert liquid
- 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
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- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ポリマアロイの製造方
法に係り、特に一方のポリマがPTFEであるようなP
TFE系ポリマアロイの製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polymer alloy, and more particularly to a polymer alloy in which one polymer is PTFE.
The present invention relates to a method for producing a TFE polymer alloy.
【0002】[0002]
【従来の技術】PTFE(ポリテトラフルオロエチレ
ン)は、耐熱性、人体に対する無害性、化学的抵抗性、
さらに自己潤滑性にすぐれ、コゲつき防止表面処理、液
体のもれ防止、ムレ防止アパレル、人工血管、分離膜な
どに巾広い応用分野を有している。2. Description of the Related Art PTFE (polytetrafluoroethylene) is heat resistant, harmless to human body, chemically resistant,
Furthermore, it has excellent self-lubricating properties and has a wide range of application fields such as anti-kogation surface treatment, liquid leakage prevention, stuffiness prevention apparel, artificial blood vessels, and separation membranes.
【0003】[0003]
【発明が解決しようとする課題】ところで、PTFE
は、機械的強度、とりわけ圧縮強度が比較的弱い。この
ため、PTFE単体、又はPTFE多孔質体が薄物とし
て用いられる場合には、その欠点が顕著となる。[Problems to be Solved by the Invention] By the way, PTFE
Has relatively low mechanical strength, especially compressive strength. For this reason, when PTFE alone or a PTFE porous body is used as a thin material, the drawback becomes remarkable.
【0004】そのPTFE単体としての欠点を改良する
方法として、最近急速に発展してきた技術として、ポリ
マアロイ化を考えることができる。ところがPTFEは
融解しても流動性がないこと、又溶剤に対する溶解性が
ないという特異性のためにPTFE系のポリマアロイ化
は大巾な制約を受けることになる。とりわけ、アロイを
構成しようとする2種以上のポリマをそれらの共通溶媒
に溶解させ、しかるのちに溶剤だけを適当な方法を用い
て除去してアロイ化する方法は、相分離の寸法をきわめ
て小さくできるために有用なアロイを得る最良の方法で
あるが、先に述べたようにPTFEの非溶解性という問
題がアロイ化の大きな技術的障害となっている。Polymer alloying can be considered as a technique which has recently been rapidly developed as a method for improving the drawbacks of the PTFE alone. However, since PTFE has no fluidity even when melted, and because of its peculiarity that it is not soluble in a solvent, the polymer alloying of PTFE is greatly restricted. In particular, a method in which two or more kinds of polymers constituting an alloy are dissolved in their common solvent and then only the solvent is removed by an appropriate method to form an alloy, the dimension of phase separation is extremely small. It is the best way to obtain a useful alloy because it is possible, but as mentioned above, the problem of insolubility of PTFE is a major technical obstacle to alloying.
【0005】本発明の目的は、前記した従来技術の問題
点を解消し、機械的強度を大巾に向上させることを可能
にするPTFE系ポリマアロイの製造方法を提供するこ
とにある。It is an object of the present invention to provide a method for producing a PTFE-based polymer alloy which solves the above-mentioned problems of the prior art and makes it possible to greatly improve the mechanical strength.
【0006】[0006]
【課題を解決するための手段】本発明は、前記目的を達
成するために、アロイを構成する2種以上のアロイポリ
マを、それらの共通溶媒に溶解した後、溶剤を蒸発させ
て得るPTFE系ポリマアロイの製造方法において、前
記アロイポリマが、PTFEと少なくとも1種のポリマ
とからなり、これらポリマをふっ素系高沸点不活性液体
によって湿潤処理を行い、その後、この湿潤ブレンド系
を170℃以上に加熱されたふっ素系高沸点不活性液体
に投下すると共に、そのふっ素系高沸点不活性液体にふ
っ素系ランダムコポリマーを溶解させるものである。In order to achieve the above object, the present invention solves the above-mentioned problems by dissolving two or more alloy polymers constituting an alloy in their common solvent and then evaporating the solvent to obtain a PTFE-based polymer alloy. In the method for producing, the alloy polymer is composed of PTFE and at least one polymer, the polymers are wet-treated with a fluorine-based high-boiling inert liquid, and then the wet blend system is heated to 170 ° C. or higher. It is a liquid which is dropped into a fluorine-based high boiling point inert liquid, and a fluorine-based random copolymer is dissolved in the fluorine-based high boiling point inert liquid.
【0007】すなわち、本発明は、PTFEの溶剤とし
てふっ素系高沸点不活性液体を用いたこと、PTFEに
湿潤処理をあらかじめ採り入れたこと、溶剤としてのふ
っ素系高沸点不活性液体を170℃以上に加熱したこ
と、及びPTFEの溶解を促進させるためにふっ素系ラ
ンダムコポリマを用いたことにあり、それらの総合的な
作用によって機械的強度が大巾に向上したPTFE系ポ
リマアロイを製造することが可能となる。That is, according to the present invention, a fluorine-based high boiling point inert liquid is used as a solvent for PTFE, a wet treatment is incorporated into PTFE in advance, and the fluorine-based high boiling point inert liquid as a solvent is heated to 170 ° C. or higher. It is due to the fact that it was heated and that the fluorine-based random copolymer was used to accelerate the dissolution of PTFE, and it is possible to produce a PTFE-based polymer alloy with greatly improved mechanical strength due to the overall action of them. Become.
【0008】本発明に用いられるPTFEとして好適で
あるのは、乳化重合によって製造されたディスパージョ
ンから分離・造粒されたペースト押出用ファインパウダ
ーである。又、ホモポリマが望ましいが、加工性を改善
するために3モル%以内で異種モノマを共重合させた変
牲PTFEでもよい。Suitable as the PTFE used in the present invention is a fine powder for paste extrusion separated and granulated from a dispersion produced by emulsion polymerization. Further, a homopolymer is preferable, but a modified PTFE obtained by copolymerizing different kinds of monomers within 3 mol% may be used in order to improve processability.
【0009】PTFEの機械的強度を向上させるポリマ
アロイをつくるための異種ポリマとしては、弗化ビニリ
デンとヘキサフルオロイソブチレンとの1:1交互共重
合体(商品名;CM−X,エニモント社製品)、ETF
E(テトラフルオロエチレン・エチレン共重合体)、P
VdF(ポリビニリデンフルオライド)等が挙げられ、
これらの中でCM−Xが最も好適である。以上挙げたポ
リマの形状は溶剤に溶解させるという必要性から、通常
の成形に好適なペレットは不適当であり、むしろ合成直
後の形状としてのパウダが最適である。As a different polymer for producing a polymer alloy for improving the mechanical strength of PTFE, a 1: 1 alternating copolymer of vinylidene fluoride and hexafluoroisobutylene (trade name; CM-X, product of Enimont), ETF
E (tetrafluoroethylene / ethylene copolymer), P
VdF (polyvinylidene fluoride) and the like,
Of these, CM-X is most suitable. Since the above-mentioned polymer shapes are required to be dissolved in a solvent, pellets suitable for ordinary molding are unsuitable, and powders having a shape immediately after synthesis are most suitable.
【0010】共通溶媒として用いられる溶剤としては、
ふっ素系不活性液体(商品名;フロリナート,3M社製
品)として一般に知られるものが好適であり、これらの
中で沸点が170℃以上のフロリナートが最適であるこ
とが実験的検討の結果わかった。このふっ素系高沸点不
活性液体は、PTFEの湿潤処理にも用いられ、その湿
潤処理に用いられる液体と温度170℃以上に加熱され
る液体とは、同一の液体でも、同系の液体でもよい。As the solvent used as the common solvent,
What is generally known as a fluorine-based inert liquid (trade name; Fluorinert, product of 3M Company) is suitable, and it has been found through experiments that Fluorinert having a boiling point of 170 ° C. or higher is the most suitable. This fluorine-based high-boiling-point inert liquid is also used for the wet treatment of PTFE, and the liquid used for the wet treatment and the liquid heated to a temperature of 170 ° C. or higher may be the same liquid or similar liquids.
【0011】本発明でPTFEの溶解性を促進させるた
めに用いられるふっ素系のランダムコポリマとしては、
テトラフルオロエチレンとPDD[パーフルオロ(2,
2−ジメチル−1,3−ジオキソール)]との共重合体
(商品名;テフロンAF,デュポン社製品)が好適であ
る。このふっ素系のランダムコポリマは、170℃以上
に加熱されるふっ素系高沸点不活性液体に予め溶解させ
てもよく、また、PTFE等の湿潤ブレンド系が投入さ
れた温度170℃以上のふっ素系高沸点不活性液体に溶
解させてもよい。The fluorine-based random copolymer used for promoting the solubility of PTFE in the present invention includes:
Tetrafluoroethylene and PDD [Perfluoro (2,
2-dimethyl-1,3-dioxole)] (trade name; Teflon AF, a product of DuPont). This fluorine-based random copolymer may be dissolved in advance in a fluorine-based high boiling point inert liquid heated to 170 ° C. or higher, and a fluorine-based polymer at a temperature of 170 ° C. or higher in which a wet blend system such as PTFE is charged. It may be dissolved in a boiling point inert liquid.
【0012】[0012]
【実施例】以下、本発明の実施例を説明する。EXAMPLES Examples of the present invention will be described below.
【0013】(実施例)PTFEとしてポリフロンTF
E F−104を5.5g,弗化ビニリデンとヘキサフ
ルオロイソブチレンとの1:1交互共重合体(商品名;
CM−X)を4.5g秤量し、これらを200mlの広
口ガラスビンに入れて振とうして十分混合する。次に、
この系に、全体を湿潤させるのに十分な量のフロリナー
トFC−70(bp215℃)を適宜配合し、さらに振
とうして十分混合した後、これを、室温で24時間放置
する(湿潤処理)。(Example) Polyflon TF as PTFE
5.5 g of EF-104, a 1: 1 alternating copolymer of vinylidene fluoride and hexafluoroisobutylene (trade name;
4.5 g of CM-X) is weighed, placed in a 200 ml wide-mouth glass bottle, shaken, and mixed well. next,
To this system, adequate amount of Fluorinert FC-70 (bp 215 ° C.) for wetting the whole was appropriately added, and further shaken and sufficiently mixed, and then allowed to stand at room temperature for 24 hours (wetting treatment). .
【0014】他方、300mlセパラブルフラスコに撹
拌器、温度計、還流管をセットし、これにフロリナート
FC−70を150ml入れて170℃まで加熱する。
尚、この温度は沸点215℃までの範囲で実験の効果に
対しては任意であるが、170℃以上ということが必要
である。また、このフロリナートは沸点近傍では、人体
に有害なPFIB(パーフロロイソブチレン)、フッ化
水素等を発生するので沸点より低い温度が望ましい。し
かし、それも十分な換気下で行えば問題ない程度のもの
である。On the other hand, a 300 ml separable flask is set with a stirrer, a thermometer, and a reflux tube, and 150 ml of Fluorinert FC-70 is put into this and heated to 170 ° C.
This temperature is arbitrary up to the boiling point of 215 ° C. for the effect of the experiment, but it is required to be 170 ° C. or higher. Further, since this fluorinate generates PFIB (perfluoroisobutylene), hydrogen fluoride, etc., which are harmful to the human body, near the boiling point, a temperature lower than the boiling point is desirable. However, if it is done under sufficient ventilation, it will not be a problem.
【0015】次に、このフラスコ内の170℃に加熱・
撹拌されているフロリナートFC−70の中へ前述の湿
潤処理を完了したPTFE/CM−Xブレンド約10g
を投入する。Next, the flask is heated to 170 ° C.
Approximately 10 g of the PTFE / CM-X blend which has been subjected to the above-mentioned wet treatment into the stirred Fluorinert FC-70.
Throw in.
【0016】その結果、PTFE/CM−Xブレンド
は、フラスコ中の強度の弱いゲルを形成する。このゲル
の実体はPTFEフィブリルの集合体にCM−Xが分散
したものである。As a result, the PTFE / CM-X blend forms a weak gel in the flask. The substance of this gel is an aggregate of PTFE fibrils and CM-X dispersed therein.
【0017】次に、この系へテフロンAF1600(T
g160℃)を3g(約1%)添加投入して1時間撹拌
する。これによりブレンドはフロリナート中へ溶解す
る。Next, Teflon AF1600 (T
g 160 ° C.), 3 g (about 1%) is added, and the mixture is stirred for 1 hour. This causes the blend to dissolve into the Fluorinert.
【0018】そして、このフラスコの上部に蒸溜装置を
セットし、フロリナートを蒸発させていく。すると、約
50mlのフロリナートが除去されたところで、PTF
E/CM−X/テフロンAF1600のアロイが凝固し
て生成する。Then, a distillation apparatus is set on the upper part of the flask to evaporate the fluorinate. Then, when about 50 ml of Fluorinert was removed, PTF
An alloy of E / CM-X / Teflon AF1600 is solidified and produced.
【0019】この凝固PTFE系ポリマアロイを200
℃×10分間熱プレスして、2mmのプレスシートを作
製し、このシートについて室温でのショア硬度を測定し
た。その結果、PTFE単独の場合での49に対して7
8と大巾なショア硬度の向上がみられた。This coagulated PTFE-based polymer alloy was added to 200
A 2 mm pressed sheet was prepared by hot pressing at 10 ° C. for 10 minutes, and the Shore hardness of this sheet was measured at room temperature. As a result, 7 compared to 49 when using PTFE alone
A remarkable improvement in Shore hardness of 8 was observed.
【0020】(比較例)前記実施例と全く同じ実験を、
フラスコ中のフロリナートFC−70の温度を150℃
で行ったところ、PTFE/CM−Xブレンドの弱いゲ
ル化(フィブリル化)は生じなかった。この場合、さら
にテフロンAF1600を全く同一量添加し撹拌して
も、PTFE/CM−Xブレンドの溶解も生じなかっ
た。(Comparative Example) The same experiment as the above example
The temperature of Fluorinert FC-70 in the flask was set to 150 ° C.
However, weak gelation (fibrillation) of the PTFE / CM-X blend did not occur. In this case, even if Teflon AF1600 was added in exactly the same amount and stirred, the PTFE / CM-X blend did not dissolve.
【0021】[0021]
【発明の効果】以上要するに本発明によれば、PTFE
と少なくとも1種のポリマをふっ素系高沸点不活性液体
によって湿潤処理を行い、その後、この湿潤ブレンド系
を170℃以上に加熱されたふっ素系高沸点不活性液体
に投下すると共に、そのふっ素系高沸点不活性液体にふ
っ素系ランダムコポリマーを溶解させることで、機械的
強度が大巾に向上したPTFE系ポリマアロイを製造で
きるという優れた効果を発揮する。In summary, according to the present invention, the PTFE
And at least one polymer are wet-treated with a fluorine-based high-boiling inert liquid, and then the wet blend system is dropped into a fluorine-based high-boiling inert liquid heated to 170 ° C. or higher and the fluorine-based high-boiling inert liquid is added. Dissolving the fluorine-based random copolymer in the boiling point-inert liquid exerts an excellent effect that a PTFE-based polymer alloy having significantly improved mechanical strength can be produced.
Claims (1)
マを、それらの共通溶媒に溶解した後、溶剤を蒸発させ
て得るPTFE系ポリマアロイの製造方法において、前
記アロイポリマが、PTFEと少なくとも1種のポリマ
とからなり、これらポリマをふっ素系高沸点不活性液体
によって湿潤処理を行い、その後、この湿潤ブレンド系
を170℃以上に加熱されたふっ素系高沸点不活性液体
に投下すると共に、そのふっ素系高沸点不活性液体にふ
っ素系ランダムコポリマーを溶解させることを特徴とす
るPTFE系ポリマアロイの製造方法。1. A method for producing a PTFE-based polymer alloy obtained by dissolving two or more alloy polymers constituting an alloy in a common solvent thereof, and then evaporating the solvent, wherein the alloy polymer is PTFE and at least one polymer. Wet these polymers with a fluorine-based high-boiling inert liquid, then drop the wet blend system into the fluorine-based high-boiling inert liquid heated to 170 ° C or higher, and A method for producing a PTFE-based polymer alloy, which comprises dissolving a fluorine-based random copolymer in an inert liquid having a boiling point.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24352991A JPH0578497A (en) | 1991-09-24 | 1991-09-24 | Production of ptfe polymer alloy |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24352991A JPH0578497A (en) | 1991-09-24 | 1991-09-24 | Production of ptfe polymer alloy |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0578497A true JPH0578497A (en) | 1993-03-30 |
Family
ID=17105261
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24352991A Pending JPH0578497A (en) | 1991-09-24 | 1991-09-24 | Production of ptfe polymer alloy |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0578497A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5518563A (en) * | 1994-12-29 | 1996-05-21 | E. I. Du Pont De Nemours And Company | Adhesion of high-melting perfluoroplastic materials |
US5874171A (en) * | 1996-08-09 | 1999-02-23 | E. I. Dupont De Nemours And Company | Compositions and assemblies of high-melting perfluoroplastic materials |
JP2003523436A (en) * | 2000-02-16 | 2003-08-05 | オムリドン テクノロジーズ エルエルシー | Melt-processable poly (tetrafluoroethylene) |
JP2012153766A (en) * | 2011-01-24 | 2012-08-16 | Daikin Industries Ltd | Fluororesin composition, and method for manufacturing the same |
US8329839B2 (en) | 1998-08-06 | 2012-12-11 | Eidgenossische Technische Hochschule | Melt-processible poly(tetrafluoroethylene) |
-
1991
- 1991-09-24 JP JP24352991A patent/JPH0578497A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5518563A (en) * | 1994-12-29 | 1996-05-21 | E. I. Du Pont De Nemours And Company | Adhesion of high-melting perfluoroplastic materials |
US5874171A (en) * | 1996-08-09 | 1999-02-23 | E. I. Dupont De Nemours And Company | Compositions and assemblies of high-melting perfluoroplastic materials |
US8329839B2 (en) | 1998-08-06 | 2012-12-11 | Eidgenossische Technische Hochschule | Melt-processible poly(tetrafluoroethylene) |
JP2003523436A (en) * | 2000-02-16 | 2003-08-05 | オムリドン テクノロジーズ エルエルシー | Melt-processable poly (tetrafluoroethylene) |
JP2012153766A (en) * | 2011-01-24 | 2012-08-16 | Daikin Industries Ltd | Fluororesin composition, and method for manufacturing the same |
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