JPS63238115A - Production of fluorine-containing copolymer having cyclic structure - Google Patents

Production of fluorine-containing copolymer having cyclic structure

Info

Publication number
JPS63238115A
JPS63238115A JP7177887A JP7177887A JPS63238115A JP S63238115 A JPS63238115 A JP S63238115A JP 7177887 A JP7177887 A JP 7177887A JP 7177887 A JP7177887 A JP 7177887A JP S63238115 A JPS63238115 A JP S63238115A
Authority
JP
Japan
Prior art keywords
fluorine
copolymer
polymerization
monomers
cyclic structure
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
Application number
JP7177887A
Other languages
Japanese (ja)
Inventor
Hitoshi Matsuo
仁 松尾
Isamu Kaneko
勇 金子
Motoi Kanba
基 神庭
Hide Nakamura
秀 中村
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.)
AGC Inc
Original Assignee
Asahi Glass Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP7177887A priority Critical patent/JPS63238115A/en
Publication of JPS63238115A publication Critical patent/JPS63238115A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To suppress secondary occurrence of gelation without adopting an ultrahigh pressure or high dilution condition and smoothly, industrially and advantageously obtain the titled copolymer, by radically polymerizing a specific perfluoro ether with other monomers. CONSTITUTION:A perfluoro ether, expressed by the formula (m and n are 0-5 and m+n is 1-6) and having two terminal double bonds is copolymerized with other radically copolymerizable monomers to afford the aimed copolymer. Furthermore, perfluoroallyl vinyl ether is preferably used as the perfluoro ether expressed by the formula. A fluorine-containing monomer, such as tetrafluoroethylene, is preferably used as the other monomers.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、環状構造を有する含フツ素共重合体の製造法
に関し、更に詳しく言えば、末端二重結合を二つ有する
特定のパーフルオロエーテルと他の共単量体とをラジカ
ル共重合せしめることからなる共重合体主鎖に環構造を
有する含フツ素共重合体の新規製造法に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention relates to a method for producing a fluorine-containing copolymer having a cyclic structure, and more specifically, the present invention relates to a method for producing a fluorine-containing copolymer having a cyclic structure. This invention relates to a new method for producing a fluorine-containing copolymer having a ring structure in the copolymer main chain, which comprises radical copolymerization of an ether and another comonomer.

[従来の技術] 従来、含フツ素共重合体としては種々のものが知られて
おり、含フツ素オレフィンや含フツ素ビニルエーテルの
共重合体としてCF2 J:F2/CF2=CFORf
、 CF2−CF2/ CH2−CH2、CF2−IC
F2/ CF2=CFCF3 、 CF2寞CFCI 
/ CH21lCH2系のように工業的に実用されてい
るものも多い、しかしながら、これらは殆んどがフルオ
ロオレフィンや炭化水素オレフィンもしくは側鎖にフル
オロアルキル基ヲ有するビニルモノマーなとの共重合反
応に基づく直鎖状の主鎖を有する共重合体である。
[Prior Art] Various fluorine-containing copolymers have been known so far, and CF2 J:F2/CF2=CFORf is a copolymer of fluorine-containing olefins and fluorine-containing vinyl ethers.
, CF2-CF2/ CH2-CH2, CF2-IC
F2/ CF2=CFCF3, CF2寞CFCI
/ There are many products that are used industrially, such as the CH21lCH2 system, but most of these are based on copolymerization reactions with fluoroolefins, hydrocarbon olefins, or vinyl monomers that have a fluoroalkyl group in the side chain. It is a copolymer with a linear main chain.

あるいはまた、ヘキサフルオロプロピレンオキシドの開
環重合により得られるパーフルオロポリエーテルの如き
高分子化合物も知られているが、この場合もやはり主鎖
構造は直鎖状であるし、共重合への適用も困難である。
Alternatively, high molecular compounds such as perfluoropolyether obtained by ring-opening polymerization of hexafluoropropylene oxide are also known, but in this case as well, the main chain structure is linear, and the application to copolymerization is also known. is also difficult.

さらン、モリブデン系の触媒を用いて開環メタセシなる
環状構造を主鎖に有する重合体の合成が試みられている
(A、Alimuniar at al、、Polym
er。
Attempts have been made to synthesize a polymer having a ring-opened metathesis, a cyclic structure in the main chain, using a molybdenum-based catalyst (A, Alimuniar at al, Polym
Er.

1988271281) 、これらはいずれも通常のビ
ニル重合もしくは開環、開環メタセシス重合であって、
直鎖状モノマーから閉環重合によって主鎖に環構造を導
入するものではない。
1988271281), these are all ordinary vinyl polymerization, ring opening, ring opening metathesis polymerization,
A ring structure is not introduced into the main chain by ring-closing polymerization from a linear monomer.

僅かに、一般式CF2−CF4Ch*xCF−CF2 
 (りだし、Xは 1〜5)がγ−線により環化重合す
ることが知られている( L、A、Waal 、Flu
or。
Slightly, general formula CF2-CF4Ch*xCF-CF2
(X is 1 to 5) is known to be cyclized and polymerized by γ-rays (L, A, Waal, Flu
or.

Polymer、 Wiley−Science、 4
. High PressurePolymeriza
tion、 P、127)、また、CF2 =CF−C
F2−CFCI−CF2−CF=CF2が重合し、耐熱
、耐酸化性に優れた透明な強い弾力性のあるフィルムを
与えることが知られている(D、S、Ba1lenti
ne etal、、 U、S、Atomic Ener
gy Com5.B、ML−294(T−50)18.
1954)、 Lかしながら、これらはいずれも1万a
tm以上の高圧を必要とする高圧重合法であり、工業的
に実施するのには困難な重合法であるという難点を有し
ている上、共重合反応への適用例はない。
Polymer, Wiley-Science, 4
.. High Pressure Polymeriza
tion, P, 127), and CF2 = CF-C
It is known that F2-CFCI-CF2-CF=CF2 polymerizes to give a transparent, strong elastic film with excellent heat resistance and oxidation resistance (D, S, Balenti
ne etal,, U, S, Atomic Ener
gy Com5. B, ML-294 (T-50)18.
1954), but these are all 10,000 a
This is a high-pressure polymerization method that requires a high pressure of tm or higher, and has the disadvantage that it is difficult to implement industrially, and there are no examples of its application to copolymerization reactions.

さらに、英国特許第11013344号、米国特許第3
418302号ナトニは、CF2−cF−o−cF2−
CF2−0−CF−CF2なるパーフルオロジメチレン
ビス(パーフルオロビニルエーテル)をモノマーとして
環化重合あるいはフルオロオレフィンやフルオロビニル
エーテルと共重合せしめる方法が記載されている。しか
しながら、この重合法では特定ジビニルエーテルモノマ
ー濃度が12重量%以下の希釈条件下でのみ環化重合す
るという制約がある。モノマー濃度が12%以上の場合
には、する重合体が生成すると記載されている。モノマ
ー濃度を12%以下にしなければならないということは
、主鎖への環構造の導入割合に限界があると共に、大量
の希釈溶媒を使用しなければならないので、工業的実施
に対して不利である。
Furthermore, British Patent No. 11013344, U.S. Patent No. 3
No. 418302 Natoni is CF2-cF-o-cF2-
A method is described in which perfluorodimethylene bis(perfluorovinyl ether), CF2-0-CF-CF2, is cyclized or copolymerized with a fluoroolefin or fluorovinyl ether as a monomer. However, this polymerization method has a restriction that cyclization polymerization can only be carried out under diluted conditions where the specific divinyl ether monomer concentration is 12% by weight or less. It is stated that when the monomer concentration is 12% or more, a polymer is produced. The monomer concentration must be 12% or less, which is disadvantageous for industrial implementation because there is a limit to the ratio of ring structure introduction into the main chain and a large amount of diluting solvent must be used. .

[発明の解決しようとする問題点] 本発明者の研究によれば、含フツ素共重合体、特にパー
フルオロ共重合体に関し、直鎖状モノマーから主鎖に環
構造を有する共重合体を工業的に円滑有利に製造し得る
手段は、前述の通り、これまでのところ殆んど知られて
いない、また、上記パーフルオロジメチレンビス(パー
フルオロビニルエーテル)の如き七ツマ−を用いた環化
重合においては、上記のような大希釈条件下の重合とい
う制約の他、重合反応系におけるゲル化の副生という難
点が認められる。
[Problems to be Solved by the Invention] According to the research of the present inventors, regarding fluorine-containing copolymers, particularly perfluoro copolymers, it is possible to convert copolymers having a ring structure in the main chain from linear monomers. As mentioned above, there is almost no known means for industrially producing it smoothly and advantageously, and there is also a ring method using a heptamine such as the perfluorodimethylene bis(perfluorovinyl ether) mentioned above. In chemical polymerization, in addition to the limitation of polymerization under conditions of large dilution as described above, there is a drawback that gelation is a by-product in the polymerization reaction system.

本発明者は、上記問題点の認識に基づいて、主鎖に環構
造を有する含フツ素共重合体の製造について鋭意研究、
検討を重ねた結果、パーフルオロアリルビニルエーテル
の如き特定のモノマーを採用しラジカル共重合せしめる
ことにより、驚くべきことに、超高圧条件や大希釈条件
を採用しなくても、ゲル化の副生を抑えて円滑有利に目
的とする含フツ素共重合体を製造し得ることを見出すに
至った。
Based on the recognition of the above-mentioned problems, the present inventor conducted extensive research on the production of fluorine-containing copolymers having a ring structure in the main chain.
As a result of repeated studies, we found that by radical copolymerization using specific monomers such as perfluoroallyl vinyl ether, it was surprisingly possible to eliminate gelation by-products without using ultra-high pressure conditions or large dilution conditions. It has been found that the desired fluorine-containing copolymer can be produced smoothly and advantageously.

[問題点を解決するための手段] かくして本発明は、前述の如き新規知見にに基いて完成
されたものであり、一般式CFzlICF(CF2)n
o(CF2)scF==cF2(ただし、nは0〜5、
層は0〜5であり、n+mは1〜6である)で表わされ
る末端二重結合を二つ有するパーフルオロエーテルとラ
ジカル共重合可能な他の単量体とをラジカル共重合せし
め、共重合体主鎖に環構造を有する共重合体を生成せし
めることを特徴とする環状構造を有する含フッ素共重合
体の製造法を新規に提供するものである。
[Means for Solving the Problems] Thus, the present invention has been completed based on the above-mentioned new findings, and has the general formula CFzlICF(CF2)n
o(CF2)scF==cF2 (where n is 0 to 5,
The perfluoroether having two terminal double bonds represented by 0 to 5 (layers are 0 to 5, and n+m is 1 to 6) is radically copolymerized with other monomers capable of radical copolymerization. The present invention provides a novel method for producing a fluorine-containing copolymer having a cyclic structure, which is characterized by producing a copolymer having a cyclic structure in its main chain.

本発明においては、特定のパーフルオロエーテルを使用
することが重要であり、例えば、CF2雪CF−0−C
F2−CF−CF2を用いてCF2−CF2などとラジ
カル共重合せしめることにより、共重合体含フツ素共重
合体を円滑有利に製造し得るものである。
In the present invention, it is important to use specific perfluoroethers, for example CF2 snow CF-0-C
By radical copolymerizing F2-CF-CF2 with CF2-CF2 or the like, a fluorine-containing copolymer can be produced smoothly and advantageously.

上記一般式中のn、mはそれぞれ0〜5の整数であり、
1+11が1〜6となる組み合せの中から選ばれる整数
である。好ましくはn、mがそれぞれ0〜3の整数で、
n+mが1〜4、さらに好ましくはn、mがそれぞれθ
〜2の整数で、n +raが1〜3のものが採用される
n and m in the above general formula are each an integer of 0 to 5,
1+11 is an integer selected from a combination of 1 to 6. Preferably, n and m are each integers of 0 to 3,
n+m is 1 to 4, more preferably n and m are each θ
An integer of ~2 and n+ra of 1 to 3 is adopted.

上記特定のパーフルオロエーテルとしては、パーフルオ
ロアリルビニルエーテルCCF2 =CFOCF2CF
−CF2 )、パー7 ル:t elジアリルビニルエ
ーテル(CF21=CFCF20CF2CF−CF2)
 、パーフルオロブテニルビニルエーテル(C:F2−
CFOCF2 CF2CF−CF2) 、パーフルオロ
ブテニルアリルビニルエーテ)1.yCCF2−CFC
F20ChCF2CF−CF2)、パーフルオロジブテ
ニルビニルエーテル(CF2−CFCF2CF20CF
2CF2 CF −CF2 )などが例示されるが、本
発明においては、n、++のいずれか一方が0のもの、
すなわちCF2 =CFO−なるビニルエーテル基を一
つ有するものが共重合反応性、閉環重合性、ゲル化抑制
などの点で好ましく採用され、特にパーフルオロアリル
ビニルエーテル(CF2−111:FOCF2 CF=
CF2 )が好適な例として挙げられる。
The above specific perfluoroether is perfluoroallyl vinyl ether CCF2=CFOCF2CF
-CF2), par7le:tel diallyl vinyl ether (CF21=CFCF20CF2CF-CF2)
, perfluorobutenyl vinyl ether (C:F2-
CFOCF2 CF2CF-CF2), perfluorobutenyl allyl vinyl ether)1. yCCF2-CFC
F20ChCF2CF-CF2), perfluorodibutenyl vinyl ether (CF2-CFCF2CF20CF
2CF2 CF -CF2 ), etc., but in the present invention, one in which either n or ++ is 0,
That is, those having one vinyl ether group such as CF2=CFO- are preferably employed in terms of copolymerization reactivity, ring-closing polymerization, and gelation suppression, and in particular, perfluoroallyl vinyl ether (CF2-111: FOCF2 CF=
CF2) is mentioned as a suitable example.

而して、上記特定のパーフルオロエーテルと共重合せし
める他の単量体としては、ラジカル重合性を有するモノ
マーであれば特に限定されずに、含フッ素系、炭化水素
系その他が広範囲にわたって例示され得る。当然のこと
であるが、これら他の単量体は一種単独で特定パーフル
オロエーテルとラジカル共重合せしめても良く、あるい
は適宜の2種類以上を併用して上記共重合反応を行なわ
せても良い0本発明においては、特定パーフルオロエー
テルの特性を最大限に生かすために、通常は他の単量体
としてフルオロオレフィン、フルオロビニルエーテルな
どの含フツ素系モノマーを選定するのが望ましい0例え
ば、テトラフルオロエチレン、パーフルオロビニルエー
テルなどは好適な具体例であり、弗化ビニリデン、弗化
ビニル、クロロトリフルオロエチレンなども例示され得
る。
Other monomers to be copolymerized with the above-mentioned specific perfluoroether are not particularly limited as long as they are radically polymerizable monomers, and a wide range of examples include fluorine-containing monomers, hydrocarbon monomers, and others. obtain. Of course, these other monomers may be used alone in radical copolymerization with the specific perfluoroether, or two or more appropriate types may be used in combination to carry out the above copolymerization reaction. 0 In the present invention, in order to make the most of the properties of the specific perfluoroether, it is usually desirable to select fluorine-containing monomers such as fluoroolefins and fluorovinyl ethers as other monomers. Fluoroethylene, perfluorovinyl ether, etc. are preferred specific examples, and vinylidene fluoride, vinyl fluoride, chlorotrifluoroethylene, etc. may also be exemplified.

上記特定のパーフルオロエーテルと他の単量体は、比較
的温和な条件下で共重合し、主鎖に環状構造を有する共
重合体を与えるという驚くべき事実が見出され、本発明
に至ったものである。すなわち、重合方法としては、ラ
ジカル的に進行するものであれば手段は何ら制限されな
いが、例えば有機、無機ラジカル開始剤、光、電離性放
射線あるいは熱による重合などが挙げられる。ラジカル
開始剤としては、2.2′−アゾビス(N、N’−ジメ
チレンイソブチルアミジン)ジハイドロクロライド、2
.2′−アゾビス(2−アミジノプロパン)ジハイドロ
クロライド、2.2′−アゾビス(N、N’−ジメチレ
ンインブチルアミジン) 、 4.4′−アゾビス(4
−シアノペンタノイックアシッド) 、 2.2’−ア
ゾビス(2−メチル−N−[1,1−ビス(ヒドロキシ
メチル)−2−ヒドロキシエチル]プロピオンアミド)
 、 2.2′−アゾビス(2−メチル−N−[1,1
−ビス(ヒドロキシメチル)エチル]プロピオンアミド
) 、 2.2′−アゾビス[2−メチル−N−(2−
ヒドロキシエチル)プロピオンアミド] 、 2.2’
−アゾビス(インブチルアミド)シバイドレート、2,
2′−アゾビス(4−メトキシ−2,4−ジメチルバレ
ロニトリル)、2.2′−アゾビス(2,4−ジメチル
バレロニトリル)、(1−フェニルエチル)アゾジフェ
ニルメタン、2,2゛−アゾビスイソブチロニトリル、
ジメチル2.2′−アゾビスイソブチレート、2.2′
−アゾビス(2−メチルブチロニトリル) 、 1.1
’−アゾビス(1−シクロヘキサンカルボニトリル)、
2−(カルバモイルアゾ)−イソブチロニトリル、2,
2′−アゾビス(2,4,4−)リメチルペブタノ)、
2−フェニルアゾ−2,4−ジメチル−4−メトキシバ
レロニトリル、2,2′−アゾビス(2−メチルプロパ
ン)の如きアゾ化合物、ステアロイルパーオキシド、ジ
イソプロピルパーオキシジカーボネート、ベンゾイルパ
ーオキシド、2.4−ジクロロベンゾイルパーオキシド
、アセチルパーオキシド、t−ブチルハイドロパーオキ
シド、クメンハイドロパーオキシド、ジ−イソプロピル
ベンゼンハイドロパーオキシド、パラ−メンタンハイド
ロパーオキシド、2,5−ジメチルヘキサン−2,5−
シバイドロバ−オキシド、メチルエチルケトンパーオキ
シド、シクロヘキサノンパーオキシド、ジ−t−ブチル
パーオキシド、ジクミルパーオキシド、t−ブチルクミ
ルパーオキシド、2,5−ジメチル−2,5−ジ(t−
ブチルパーオキシ)ヘキサン、2.5−ジメチル−2,
5−ジ(1−ブチルパーオキシ)ヘキシン−3、オクタ
ノイルパーオキシド、デカノイルパーオキシド、ラウロ
イルパーオキシド、t−ブチルパーベンゾエート、t−
ブチルパーアセテート、t−ブチルパーピバレート、t
−ブチルパーインブチレート、t−プチルパーオキシイ
ソブロビルカーポネート、ジ−t−ブチルシバ−フタレ
ート、t−ブチルパーラウレート、2.5−ジメチル−
2,5−ジ(ベンゾイルパーオキシ)ヘキサン、ジ−パ
ーフルオロブタノイックパーオキシド、ジ−パーフルオ
ロ−3−オキサ−2−メチルヘキサノイックパーオキシ
ド、ジーパーフルオロノナノイックパーオキシドの如き
有機パーオキシド、K2 S20s 。
The surprising fact was discovered that the specific perfluoroether and other monomers copolymerize under relatively mild conditions to give a copolymer having a cyclic structure in the main chain, which led to the present invention. It is something that That is, the polymerization method is not particularly limited as long as it proceeds in a radical manner, and examples thereof include polymerization using an organic or inorganic radical initiator, light, ionizing radiation, or heat. As the radical initiator, 2,2'-azobis(N,N'-dimethyleneisobutyramidine) dihydrochloride, 2
.. 2'-azobis(2-amidinopropane) dihydrochloride, 2.2'-azobis(N,N'-dimethyleneinbutyramidine), 4.4'-azobis(4
-cyanopentanoic acid), 2,2'-azobis(2-methyl-N-[1,1-bis(hydroxymethyl)-2-hydroxyethyl]propionamide)
, 2.2'-azobis(2-methyl-N-[1,1
-bis(hydroxymethyl)ethyl]propionamide), 2,2'-azobis[2-methyl-N-(2-
hydroxyethyl)propionamide], 2.2'
-Azobis(inbutyramide)cybiderate, 2,
2'-azobis(4-methoxy-2,4-dimethylvaleronitrile), 2,2'-azobis(2,4-dimethylvaleronitrile), (1-phenylethyl)azodiphenylmethane, 2,2'-azobis isobutyronitrile,
Dimethyl 2.2'-azobisisobutyrate, 2.2'
-azobis(2-methylbutyronitrile), 1.1
'-azobis(1-cyclohexanecarbonitrile),
2-(carbamoylazo)-isobutyronitrile, 2,
2'-azobis(2,4,4-)limethylpebutano),
Azo compounds such as 2-phenylazo-2,4-dimethyl-4-methoxyvaleronitrile, 2,2'-azobis(2-methylpropane), stearoyl peroxide, diisopropyl peroxydicarbonate, benzoyl peroxide, 2.4 -dichlorobenzoyl peroxide, acetyl peroxide, t-butyl hydroperoxide, cumene hydroperoxide, di-isopropylbenzene hydroperoxide, para-menthane hydroperoxide, 2,5-dimethylhexane-2,5-
Cibidroba-oxide, methyl ethyl ketone peroxide, cyclohexanone peroxide, di-t-butyl peroxide, dicumyl peroxide, t-butylcumyl peroxide, 2,5-dimethyl-2,5-di(t-
butylperoxy)hexane, 2,5-dimethyl-2,
5-di(1-butylperoxy)hexyne-3, octanoyl peroxide, decanoyl peroxide, lauroyl peroxide, t-butyl perbenzoate, t-
Butyl peracetate, t-butyl perpivalate, t
-Butylperyne butyrate, t-butylperoxyisobrobyl carbonate, di-t-butylshiba-phthalate, t-butylperlaurate, 2.5-dimethyl-
Organic peroxides such as 2,5-di(benzoylperoxy)hexane, diperfluorobutanoic peroxide, diperfluoro-3-oxa-2-methylhexanoic peroxide, diperfluorononanoic peroxide , K2 S20s.

(NH4) 2 S20gの如き無機パーオキシドなど
が例示される。光としては、可視光、紫外線などが例示
され、光増感剤を併用することもできる。電離性放射線
としては60(:(1,+92ir、1707z、13
70sなどの放射性同位元素からのγ線、β線、α線な
どや、電子線加速器による電子線などが例示される。
Examples include inorganic peroxides such as 20 g of (NH4) 2 S. Examples of the light include visible light and ultraviolet light, and a photosensitizer can also be used in combination. Ionizing radiation is 60 (: (1, +92ir, 1707z, 13
Examples include γ rays, β rays, α rays, etc. from radioactive isotopes such as 70S, and electron beams from an electron beam accelerator.

重合の方法もまた特に限定されるものではなく、モノマ
ーをそのまま重合に供するいわゆるバルク重合、モノマ
ーを溶解する弗化炭化水素、塩化炭化水素、弗塩化炭化
水素、アルコール、ハイドロカーボン、その他の有機溶
媒中で行なう溶液重合、水性媒体中で適当な有機溶剤の
存在下或いは非存在下に行なう懸濁重合、水性媒体に乳
化剤を添加して行なう乳化重合などが例示される0重合
を行なう温度や圧力も特に限定されるものではないが、
モノマーの沸点、所用加熱源1重合熱の除去等の諸因子
を考慮して適宜設定することが望ましい0例えば、0℃
〜200℃の間で好適な温度の設定を行なうことができ
、室温〜100℃程度ならば実用的にも好適な温度設定
を行なうことができる。また重合圧力としては減圧下で
も加圧下でも良く、実用的には常圧〜100気圧程度、
更には常圧〜50気圧程度でも好適な重合を実施できる
The polymerization method is also not particularly limited, and includes so-called bulk polymerization in which the monomer is directly subjected to polymerization, and fluorinated hydrocarbons, chlorinated hydrocarbons, fluorochlorinated hydrocarbons, alcohols, hydrocarbons, and other organic solvents in which the monomers are dissolved. Examples include solution polymerization carried out in an aqueous medium, suspension polymerization carried out in the presence or absence of an appropriate organic solvent in an aqueous medium, and emulsion polymerization carried out by adding an emulsifier to an aqueous medium. Although not particularly limited,
It is desirable to set the temperature appropriately in consideration of various factors such as the boiling point of the monomer, the required heat source 1, and the removal of the heat of polymerization. For example, 0°C.
A suitable temperature can be set between 200°C and 200°C, and a practically suitable temperature can be set between room temperature and 100°C. In addition, the polymerization pressure may be under reduced pressure or increased pressure, and practically, it is about normal pressure to 100 atmospheres,
Furthermore, suitable polymerization can be carried out at normal pressure to about 50 atmospheres.

本発明においては、上記特定のパーフルオロエーテルの
共重合割合についても特に限定される理由はないが、主
鎖に環構造を導入して後述の如き種々の性能を改善する
という観点から、通常は他の単量体に対して仕込み組成
で0.1モル%以上が採用される。
In the present invention, there is no particular reason to limit the copolymerization ratio of the above-mentioned specific perfluoroether, but from the viewpoint of introducing a ring structure into the main chain to improve various performances as described below, it is usually It is used in an amount of 0.1 mol% or more in the charging composition with respect to other monomers.

本発明により得られる共重合体の特徴としては、例えば
、CF2−0F2 と共重合させた場合、ポリテトラフ
ルオロエチレン(以下、PTFEと略記する)と比較し
て結晶性を下げることができる。したがって、この共重
合体は溶融成形が可能になり、透明性も向上する。また
環状部分の組成を高くすると、溶融可溶になりキャスト
成膜も可能となる。つまり得られるテトラフルオロエチ
レンとの共重合体はPTFEより成形が容易となるため
、PTFEと同等のフッ素樹脂としての性能をもつ各種
成形体に用いることができる。さらに透明性やキャスト
成膜法・を利用した各種コーテイング材、電子部材、光
学部材等に用いることができる。
A feature of the copolymer obtained by the present invention is that, for example, when copolymerized with CF2-0F2, the crystallinity can be lowered compared to polytetrafluoroethylene (hereinafter abbreviated as PTFE). Therefore, this copolymer can be melt-molded and has improved transparency. Furthermore, when the composition of the annular portion is increased, it becomes meltable and can be cast into a film. In other words, since the obtained copolymer with tetrafluoroethylene is easier to mold than PTFE, it can be used for various molded products having the same performance as PTFE as a fluororesin. Furthermore, it can be used for various coating materials, electronic components, optical components, etc. that utilize transparency and cast film formation methods.

CF2−GH2と共重合させた場合、弗化ビニリデン単
独重合体(以下、PVdFと略記する)と比較して結晶
性を下げたり、結晶粒径を小さくし、透明性が向上する
。また屈折率も下げることができ、PVdFの特徴の1
つでもある高い強度物性も下げることなく、フッ素含量
を増やすごとができる、したがって、この共重合体は現
在PVdFが用いられている分野すべてに応用可能で、
特に屈折率を下げ透明性が向上するためつり糸などには
好適である。さらに、透明な誘電体として電子部材、光
学部材に用いることもできる。また溶融成形、キャスト
成膜も可能でフッ素含量も高いため、PVdFよりも耐
候性、耐溶剤性、耐熱性、化学的安定性に優れた各種成
形体、各種コーテイング材を提供することができる。
When copolymerized with CF2-GH2, compared to vinylidene fluoride homopolymer (hereinafter abbreviated as PVdF), crystallinity is lowered, crystal grain size is reduced, and transparency is improved. It is also possible to lower the refractive index, which is one of the characteristics of PVdF.
The fluorine content can be increased without compromising the already high strength properties of the copolymer. Therefore, this copolymer can be applied in all fields where PVdF is currently used.
In particular, it is suitable for hanging threads because it lowers the refractive index and improves transparency. Furthermore, it can also be used as a transparent dielectric material in electronic components and optical components. Furthermore, since it can be melt-molded and cast and has a high fluorine content, it is possible to provide various molded bodies and various coating materials that have better weather resistance, solvent resistance, heat resistance, and chemical stability than PVdF.

以上のように、従来知られている含フツ素系モノマーと
特定のパーフルオロエーテル単量体を共重合させると、
結晶性を下げたり結晶粒径を小さくすることができ、透
明性が向上し、溶融成形が可能になる。また弾性率等の
機械的強度も高くなる。さらには、パーフルオロエーテ
ル組成を高くすると溶媒可溶になるなど含フツ素ポリマ
ーの欠点である不透明性、成形性、機械的強度などを改
善することができる。
As mentioned above, when a conventionally known fluorine-containing monomer and a specific perfluoroether monomer are copolymerized,
It is possible to lower the crystallinity and reduce the crystal grain size, improving transparency and making melt molding possible. In addition, mechanical strength such as elastic modulus is also increased. Furthermore, when the perfluoroether composition is increased, it becomes soluble in solvents, and the disadvantages of fluorine-containing polymers such as opacity, moldability, and mechanical strength can be improved.

炭化水素系の単量体と共重合させた場合、・この共重合
体は、炭化水素系やPTFE、PVdFの如き含フッ素
系の共重合体と比較して、炭化水素系ポリマーとしての
性梯を下げることなくフッ素系ポリマーの特徴を付与す
ることができる。この理由は明らかではないが。
When copolymerized with a hydrocarbon-based monomer, this copolymer has a higher property ladder as a hydrocarbon-based polymer than a hydrocarbon-based or fluorine-containing copolymer such as PTFE or PVdF. It is possible to impart the characteristics of a fluoropolymer without lowering the properties. The reason for this is not clear.

フッ素部分が環状構造を示し結晶を作らないためである
と考えられる。
This is thought to be because the fluorine moiety exhibits a cyclic structure and does not form crystals.

その他、本発明により得られる含フツ素共重合体は、含
フッ素の環状構造を有しているため気体の分離性能も高
くガス分離膜用素材などとしても用いることができる。
In addition, since the fluorine-containing copolymer obtained by the present invention has a fluorine-containing cyclic structure, it has high gas separation performance and can be used as a material for gas separation membranes.

[作用] 本発明において、特定のパーフルオロエーテルを使用す
ることにより環化重合に超高圧条件や高希釈条件の採用
を必要としなくなった機構は必ずしも明確でないが、C
−0−C結合はフレキシブルであるので二つの二重結合
が分子内で近付くのが容易になって、低い圧力下でも環
化重合が進行すると考えられ、また−個のエーテル結合
の介在により二つの二重結合の反応性に何らかの差異を
生じさせやすくなって、高い希釈条件を採用しなくても
共重合反応中のゲル化の副生を抑制できるものと考えら
れる。なお、かかる説明は本発明の理解の助けとするも
のであり、本発明を何ら限定するものでないことは勿論
である。
[Function] In the present invention, the mechanism by which use of a specific perfluoroether eliminates the need for ultra-high pressure conditions or high dilution conditions for cyclization polymerization is not necessarily clear, but C
Since the -0-C bond is flexible, it is thought that the two double bonds can easily approach each other within the molecule, allowing cyclopolymerization to proceed even under low pressure. It is thought that this makes it easier to cause some kind of difference in the reactivity of the two double bonds, thereby suppressing gelation as a by-product during the copolymerization reaction without adopting high dilution conditions. It should be noted that this explanation is provided to assist in understanding the present invention, and is not intended to limit the present invention in any way.

[実施例] 次に、本発明の実施例について更に具体的に説明するが
、かかる説明によって本発明が何ら限定されるものでな
いことは勿論である。
[Examples] Next, Examples of the present invention will be described in more detail, but it goes without saying that the present invention is not limited by such explanations.

実施例1 パーフルオロアリルビニルエーテルの5g、トリクロロ
トリフルオロ5タン(以下、R−113赫 と略記する)の15gと重合開始剤((3F7 Co)
25wt%R−113溶液の80mgを10h(2の耐
圧ガラス製アンプルに入れた。凍結脱気を3回繰り返し
た後にCF2−CF2を0.5g仕込んだ、インキュベ
ーターで振とうさせながら30℃で6時間重合を行なっ
た結果、1.5gの固体が得られた。
Example 1 5 g of perfluoroallyl vinyl ether, 15 g of trichlorotrifluoropentathane (hereinafter abbreviated as R-113), and a polymerization initiator ((3F7 Co)
80 mg of 25 wt% R-113 solution was placed in a pressure-resistant glass ampoule for 10 h (2). After repeating freezing and degassing three times, 0.5 g of CF2-CF2 was charged and incubated at 30°C with shaking in an incubator for 6 hours. As a result of time polymerization, 1.5 g of solid was obtained.

得られた固体をパーフルオロベンゼンに溶解し19Fの
NMRスペクトルにより構造を確認した。その結果、得
られた重合体は、 のような環状構造単位とテトラブルオロエチレン単位と
の共重合体であり、a/bのモル比が110.52であ
ることがわかった。また、この共重合体の固有粘度は0
.425であった。
The obtained solid was dissolved in perfluorobenzene, and the structure was confirmed by 19F NMR spectrum. As a result, it was found that the obtained polymer was a copolymer of a cyclic structural unit such as the following and a tetrafluoroethylene unit, and the a/b molar ratio was 110.52. Moreover, the intrinsic viscosity of this copolymer is 0
.. It was 425.

実施例2 パーフルオロアリルビニルエーテルの5g、■ R−113の15gと重合開始剤(C3F7GO)25
wt%R−113溶液の50+sgを100s12 (
7)耐圧ガラス製アンプルに入れた。凍結脱気を3回繰
り返した後にCF2−CF2 を0.5g仕込んだ、3
0℃で45分間重合を行なった結果、1.8gの白色粉
体が得られた。得られた固体は19F NMRスペクト
ルより実施例1と同様な共重合体であることがわかった
Example 2 5g of perfluoroallyl vinyl ether, 15g of R-113 and 25g of polymerization initiator (C3F7GO)
50+sg of wt% R-113 solution was added to 100s12 (
7) Placed in a pressure-resistant glass ampoule. After repeating freezing and degassing three times, 0.5g of CF2-CF2 was charged, 3
As a result of polymerization at 0° C. for 45 minutes, 1.8 g of white powder was obtained. The obtained solid was found to be the same copolymer as in Example 1 from the 19F NMR spectrum.

実施例3 パーフルオロアリルビニルエーテルの5g、純水の25
3. CBF+7G02M)Inの0.09g、Ha)
12 PClaの0.073g、加硫酸アンモニウムの
0.0132gを100+m(2の耐圧ガラス製アンプ
ルに入れた。系内を充分窒素ガスで置換した後に、CF
2−CF2を0.5g仕込んだ、60℃で18時間、イ
ンキュベーターで振とうさせながら重合を行なった結果
、2.5gの固体が得られた。
Example 3 5 g of perfluoroallyl vinyl ether, 25 g of pure water
3. 0.09g of CBF+7G02M)In, Ha)
12 0.073 g of PCla and 0.0132 g of ammonium sulfate were placed in a pressure-resistant glass ampoule of 100+ m (2). After replacing the system with nitrogen gas sufficiently, CF
0.5 g of 2-CF2 was charged and polymerization was carried out at 60° C. for 18 hours with shaking in an incubator, resulting in 2.5 g of solid.

得られた固体をパーフルオロベンゼンに溶解し+91i
のNMRスペクトルにより構造を確認した。また、この
共重合体の固有粘度は0.30であった。
The obtained solid was dissolved in perfluorobenzene and +91i
The structure was confirmed by NMR spectrum. Moreover, the intrinsic viscosity of this copolymer was 0.30.

実施例4 パーフルオロアリルビニルエーテルの20g、R−11
3の80gと重合開始剤ジイソプロピルパーオキシジカ
ーボネートの20+wgを20m(2の耐圧ガラス製ア
ンプルに入れた。実施例1と同様にしてCF2−CF2
を仕込み、同様の条件で4時間30分重合を行なった結
果、アセトンに可溶な固体が12.3g得られた。
Example 4 20 g of perfluoroallyl vinyl ether, R-11
80 g of No. 3 and 20+ wg of polymerization initiator diisopropyl peroxydicarbonate were placed in a 20 m (20 m) pressure-resistant glass ampoule.
was charged and polymerization was carried out for 4 hours and 30 minutes under the same conditions. As a result, 12.3 g of acetone-soluble solid was obtained.

実施例5 パーフルオロアリルビニルエーテルの5gとパーフルオ
ロプロピルパーフルオロビニルエーテルの8.74gと
 2.2’−アゾビスイソブチロニトリルの5gを10
0+Q酎圧ガラス製アンプルに入れた。凍結脱気を3回
繰り返した後、60℃で18時間、インキュベーターで
振とうさせながら重合を行なった結果、0.9gの固体
が得られた。
Example 5 5 g of perfluoroallyl vinyl ether, 8.74 g of perfluoropropyl perfluorovinyl ether, and 5 g of 2.2'-azobisisobutyronitrile were mixed into 10
The 0+Q liquor was placed in a glass ampule. After repeating freezing and degassing three times, polymerization was carried out at 60° C. for 18 hours while shaking in an incubator, resulting in 0.9 g of solid.

[発明の効果] 本発明は、特定のパーフルオロエーテルを共重合成分と
して採用することにより、共重合体主鎖に環構造を有す
る含フツ素共重合体を円滑有利に製造し得るという優れ
た効果を有する。
[Effects of the Invention] The present invention provides an excellent advantage in that a fluorine-containing copolymer having a ring structure in the main chain of the copolymer can be produced smoothly and advantageously by employing a specific perfluoroether as a copolymerization component. have an effect.

特に、超高圧条件や高希釈条件などを採用しなくても主
鎖への環構造の導入が達成され、また1個のエーテル結
合の介在により重合反応中でのゲル化の副生を抑制する
という効果も認められる。さらに、本発明においては、
各種ポリマー主鎖に含フッ素の環構造を導入できること
から、得られる含フツ素共重合体に種々の優秀且つ有用
な特性を付与し得るという効果もある0例えば、PTF
Eその他の含フツ素ポリマーに適用することにより、本
来の含フツ素ポリマーの耐熱性、化学安定性、電気特性
などを損なうことなく、非結品性、透明性、溶剤可溶性
などの有用な性質を付与し得るし、超薄膜化をも可能と
するものである。
In particular, the introduction of a ring structure into the main chain is achieved without employing ultra-high pressure conditions or high dilution conditions, and the presence of one ether bond suppresses gelation as a by-product during the polymerization reaction. This effect is also recognized. Furthermore, in the present invention,
Since a fluorine-containing ring structure can be introduced into the main chain of various polymers, it is possible to impart various excellent and useful properties to the resulting fluorine-containing copolymers.For example, PTF
By applying it to other fluorine-containing polymers, it can provide useful properties such as non-caking property, transparency, and solvent solubility without impairing the heat resistance, chemical stability, electrical properties, etc. of the original fluorine-containing polymer. It is possible to provide an ultra-thin film.

Claims (1)

【特許請求の範囲】 1、一般式CF_2=CF−(CF_2)−_nO−(
CF_2)−_mCF=CF_2(ただし、nは0〜5
、mは0〜5であり、n+mは1〜6である)で表わさ
れる末端二重結合を二つ有するパーフルオロエーテルと
ラジカル共重合可能な他の単量体とをラジカル共重合せ
しめ、共重合体主鎖に環構造を有する共重合体を生成せ
しめることを特徴とする環状構造を有する含フッ素共重
合体の製造法。 2、パーフルオロエーテルがCF_2=CF−O−CF
_2−CF=CF_2なるパーフルオロアリルビニルエ
ーテルである特許請求の範囲第1項記載の製造 法。 3、パーフルオロエーテルの共重合反応系への仕込み組
成が他の単量体に対して0.1モル%以上である特許請
求の範囲第1項又は第2項記載の製造法。
[Claims] 1. General formula CF_2=CF-(CF_2)-_nO-(
CF_2) -_mCF=CF_2 (where n is 0 to 5
, m is 0 to 5, and n+m is 1 to 6), and another radically copolymerizable monomer is radically copolymerized to form a copolymer. 1. A method for producing a fluorine-containing copolymer having a cyclic structure, which comprises producing a copolymer having a cyclic structure in the polymer main chain. 2. Perfluoroether is CF_2=CF-O-CF
_2-CF=CF_2 perfluoroallyl vinyl ether, the manufacturing method according to claim 1. 3. The production method according to claim 1 or 2, wherein the perfluoroether is charged to the copolymerization reaction system in an amount of 0.1 mol % or more based on other monomers.
JP7177887A 1987-03-27 1987-03-27 Production of fluorine-containing copolymer having cyclic structure Pending JPS63238115A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7177887A JPS63238115A (en) 1987-03-27 1987-03-27 Production of fluorine-containing copolymer having cyclic structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7177887A JPS63238115A (en) 1987-03-27 1987-03-27 Production of fluorine-containing copolymer having cyclic structure

Publications (1)

Publication Number Publication Date
JPS63238115A true JPS63238115A (en) 1988-10-04

Family

ID=13470366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7177887A Pending JPS63238115A (en) 1987-03-27 1987-03-27 Production of fluorine-containing copolymer having cyclic structure

Country Status (1)

Country Link
JP (1) JPS63238115A (en)

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0303298A2 (en) * 1987-08-14 1989-02-15 Asahi Glass Company Ltd. Novel fluorine-containing cyclic polymer
JPH0368140A (en) * 1989-04-19 1991-03-25 Asahi Glass Co Ltd Semiconductor element and integrated circuit device
US5451992A (en) * 1991-10-29 1995-09-19 Canon Kabushiki Kaisha Ink jet head having an improved ink discharge surface and ink jet apparatus equipped with the head
US5462586A (en) * 1993-09-08 1995-10-31 Japan Gore-Tex, Inc. Oil-and water repellent gas-permeable filter
US5502132A (en) * 1992-07-27 1996-03-26 Asahi Glass Company Ltd. Process for producing a perfluoro copolymer
JPH08234001A (en) * 1995-02-24 1996-09-13 Asahi Glass Co Ltd Antireflection optical article
JP2001151970A (en) * 1999-09-13 2001-06-05 Daikin Ind Ltd Fluororesin composition capable of film-forming at low temperature
WO2001098834A1 (en) * 2000-06-21 2001-12-27 Asahi Glass Company, Limited Resist composition
WO2004052953A1 (en) * 2002-12-06 2004-06-24 Asahi Glass Company, Limited Tetrafluoroethylene copolymer, process for producing the same and paste extrudate
US6835782B1 (en) 1999-07-14 2004-12-28 Daikin Industries, Ltd. Method for curing fluoropolymer
US6858692B2 (en) * 2001-02-09 2005-02-22 Asahi Glass Company, Limited Fluorinated compound, fluoropolymer and process for its production
US6960387B2 (en) 2001-06-25 2005-11-01 Asahi Glass Company, Limited Optical film
US7060771B2 (en) 2000-12-28 2006-06-13 Central Glass Company, Limited Transparent fluorine-containing copolymer
JP2006180450A (en) * 2004-11-26 2006-07-06 Univ Of Tokyo Electrostatic induction conversion device
WO2007077722A1 (en) * 2006-01-05 2007-07-12 Asahi Glass Company, Limited Fluorine-containing polymer and fluorine-containing polymer composition containing same
US7449811B2 (en) 2004-11-26 2008-11-11 The University Of Tokyo Electrostatic induction conversion device
US7453620B2 (en) 2003-09-03 2008-11-18 Asahi Glass Company, Limited Spatial optical modulation element and spatial optical modulation method
WO2008143069A1 (en) 2007-05-16 2008-11-27 Asahi Glass Company, Limited Method for production of fluorine-treated perfluoropolymer
WO2009123022A1 (en) 2008-03-31 2009-10-08 旭硝子株式会社 Acceleration sensor device and sensor network system
JP2010526908A (en) * 2007-05-11 2010-08-05 スリーエム イノベイティブ プロパティズ カンパニー Melt processable fluoropolymers with long chain branches, methods for their preparation and use
US7879446B2 (en) * 2007-07-12 2011-02-01 Industrial Technology Research Institute Fluorinated cyclic olefin electret film
US8029871B2 (en) 2005-06-09 2011-10-04 Hoya Corporation Method for producing silica aerogel coating
US8199404B2 (en) 2007-12-27 2012-06-12 Pentax Ricoh Imaging Company, Ltd. Anti-reflection coating, optical member, exchange lens unit and imaging device
US8298622B2 (en) 2005-04-22 2012-10-30 Pentax Ricoh Imaging Company, Ltd. Silica aerogel coating and its production method
WO2014042023A1 (en) 2012-09-11 2014-03-20 旭硝子株式会社 Plastic optical fiber and method for producing same
CN104054016A (en) * 2012-03-30 2014-09-17 富士胶片株式会社 Optical element and image display device
EP3184307A1 (en) 2015-12-25 2017-06-28 Ricoh Company, Ltd. Printing device and printing method
US9982091B2 (en) 2014-03-06 2018-05-29 3M Innovative Properties Company Highly fluorinated elastomers
WO2019176223A1 (en) * 2018-03-14 2019-09-19 株式会社クレハ Polymer gel electrolyte for nonaqueous electrolyte secondary battery, and nonaqueous electrolyte secondary battery
EP3686254A1 (en) 2019-01-25 2020-07-29 Ricoh Company, Ltd. Ink, method of manufacturing ink, printing method, and printing device
US11111326B2 (en) 2013-12-11 2021-09-07 3M Innovative Properties Company Highly fluorinated elastomers
EP3988624A1 (en) 2020-10-21 2022-04-27 Ricoh Company, Ltd. Ink set, inkjet printing apparatus, and inkjet printing method
WO2024009701A1 (en) * 2022-07-07 2024-01-11 Agc株式会社 Fluorine-containing polymer, composition, surface treatment agent, and article

Cited By (46)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0303292A2 (en) * 1987-08-14 1989-02-15 Asahi Glass Company Ltd. Cyclic polymerization
EP0303298A2 (en) * 1987-08-14 1989-02-15 Asahi Glass Company Ltd. Novel fluorine-containing cyclic polymer
JPH0368140A (en) * 1989-04-19 1991-03-25 Asahi Glass Co Ltd Semiconductor element and integrated circuit device
US5451992A (en) * 1991-10-29 1995-09-19 Canon Kabushiki Kaisha Ink jet head having an improved ink discharge surface and ink jet apparatus equipped with the head
US5502132A (en) * 1992-07-27 1996-03-26 Asahi Glass Company Ltd. Process for producing a perfluoro copolymer
US5462586A (en) * 1993-09-08 1995-10-31 Japan Gore-Tex, Inc. Oil-and water repellent gas-permeable filter
JPH08234001A (en) * 1995-02-24 1996-09-13 Asahi Glass Co Ltd Antireflection optical article
US6835782B1 (en) 1999-07-14 2004-12-28 Daikin Industries, Ltd. Method for curing fluoropolymer
JP2001151970A (en) * 1999-09-13 2001-06-05 Daikin Ind Ltd Fluororesin composition capable of film-forming at low temperature
WO2001098834A1 (en) * 2000-06-21 2001-12-27 Asahi Glass Company, Limited Resist composition
US6916590B2 (en) 2000-06-21 2005-07-12 Asahi Glass Company, Limited Resist composition
US7060771B2 (en) 2000-12-28 2006-06-13 Central Glass Company, Limited Transparent fluorine-containing copolymer
US7417100B2 (en) 2000-12-28 2008-08-26 Central Glass Company, Limited Transparent fluorine-containing copolymer
US6858692B2 (en) * 2001-02-09 2005-02-22 Asahi Glass Company, Limited Fluorinated compound, fluoropolymer and process for its production
US6960387B2 (en) 2001-06-25 2005-11-01 Asahi Glass Company, Limited Optical film
US7153568B2 (en) 2001-06-25 2006-12-26 Asahi Glass Company, Limited Optical film
JP2004231936A (en) * 2002-12-06 2004-08-19 Asahi Glass Co Ltd Tetrafluoroethylene copolymer, method for producing the same and paste extrusion molded product
WO2004052953A1 (en) * 2002-12-06 2004-06-24 Asahi Glass Company, Limited Tetrafluoroethylene copolymer, process for producing the same and paste extrudate
US7071273B2 (en) 2002-12-06 2006-07-04 Asahi Glass Company, Limited Tetrafluoroethylene copolymer, its production method and paste extruded product
US7453620B2 (en) 2003-09-03 2008-11-18 Asahi Glass Company, Limited Spatial optical modulation element and spatial optical modulation method
US7449811B2 (en) 2004-11-26 2008-11-11 The University Of Tokyo Electrostatic induction conversion device
JP2006180450A (en) * 2004-11-26 2006-07-06 Univ Of Tokyo Electrostatic induction conversion device
JP4670050B2 (en) * 2004-11-26 2011-04-13 国立大学法人 東京大学 Electret and electrostatic induction type conversion element
US8053948B2 (en) 2004-11-26 2011-11-08 The University Of Tokyo Electrostatic induction conversion device
US8298622B2 (en) 2005-04-22 2012-10-30 Pentax Ricoh Imaging Company, Ltd. Silica aerogel coating and its production method
US8029871B2 (en) 2005-06-09 2011-10-04 Hoya Corporation Method for producing silica aerogel coating
WO2007077722A1 (en) * 2006-01-05 2007-07-12 Asahi Glass Company, Limited Fluorine-containing polymer and fluorine-containing polymer composition containing same
US8017709B2 (en) 2006-01-05 2011-09-13 Asahi Glass Company, Limited Fluorinated polymer and fluorinated polymer composition containing it
US8969500B2 (en) 2007-05-11 2015-03-03 3M Innovative Properties Company Melt-processible fluoropolymers having long-chain branches, methods of preparing them and uses thereof
JP2010526908A (en) * 2007-05-11 2010-08-05 スリーエム イノベイティブ プロパティズ カンパニー Melt processable fluoropolymers with long chain branches, methods for their preparation and use
JP2014065911A (en) * 2007-05-11 2014-04-17 3M Innovative Properties Co Melt-processible fluoropolymers having long-chain branches, methods of preparing them and uses thereof
WO2008143069A1 (en) 2007-05-16 2008-11-27 Asahi Glass Company, Limited Method for production of fluorine-treated perfluoropolymer
US7879446B2 (en) * 2007-07-12 2011-02-01 Industrial Technology Research Institute Fluorinated cyclic olefin electret film
US8199404B2 (en) 2007-12-27 2012-06-12 Pentax Ricoh Imaging Company, Ltd. Anti-reflection coating, optical member, exchange lens unit and imaging device
WO2009123022A1 (en) 2008-03-31 2009-10-08 旭硝子株式会社 Acceleration sensor device and sensor network system
CN104054016A (en) * 2012-03-30 2014-09-17 富士胶片株式会社 Optical element and image display device
WO2014042023A1 (en) 2012-09-11 2014-03-20 旭硝子株式会社 Plastic optical fiber and method for producing same
US9304251B2 (en) 2012-09-11 2016-04-05 Asahi Glass Company, Limited Plastic optical fiber and method for its production
US11111326B2 (en) 2013-12-11 2021-09-07 3M Innovative Properties Company Highly fluorinated elastomers
US9982091B2 (en) 2014-03-06 2018-05-29 3M Innovative Properties Company Highly fluorinated elastomers
EP3184307A1 (en) 2015-12-25 2017-06-28 Ricoh Company, Ltd. Printing device and printing method
WO2019176223A1 (en) * 2018-03-14 2019-09-19 株式会社クレハ Polymer gel electrolyte for nonaqueous electrolyte secondary battery, and nonaqueous electrolyte secondary battery
EP3686254A1 (en) 2019-01-25 2020-07-29 Ricoh Company, Ltd. Ink, method of manufacturing ink, printing method, and printing device
EP3988624A1 (en) 2020-10-21 2022-04-27 Ricoh Company, Ltd. Ink set, inkjet printing apparatus, and inkjet printing method
US11851571B2 (en) 2020-10-21 2023-12-26 Ricoh Company, Ltd. Ink set, inkjet printing apparatus, and inkjet printing method
WO2024009701A1 (en) * 2022-07-07 2024-01-11 Agc株式会社 Fluorine-containing polymer, composition, surface treatment agent, and article

Similar Documents

Publication Publication Date Title
JPS63238115A (en) Production of fluorine-containing copolymer having cyclic structure
US4910276A (en) Cyclic polymerization
JPS63238111A (en) Production of fluorine-containing polymer having cyclic structure
EP0199138B1 (en) Novel fluorovinyl ether and copolymer comprising the same
US3528954A (en) Process for homopolymerization of tetrafluoroethylene and copolymerization of same with fluoro co-monomers in the solvent 1,1,2 - trichloro - 1,2,2 - trifluoroethane
EP2791191B1 (en) Crosslinkable vinylidene fluoride and trifluoroethylene polymers
EP0247379B1 (en) Process for the polymerization of fluorinated monomers in aqueous dispersion
EP0617058B1 (en) (Co)polymerization process in aqueous emulsion of fluorinated olefinic monomers
JP3471456B2 (en) Novel fluorinated thermoplastic elastomer having excellent mechanical and elastic properties and method for producing the same
EP0662096B1 (en) Iodine containing chain transfer agents for fluoromonomer polymerizations
US5494984A (en) Method for producing a fluorinated polymer
US6677414B2 (en) Aqueous emulsion polymerization process for the manufacturing of fluoropolymers
EP0437619B1 (en) Fluorinated copolymer and method of producing the same
KR20080094667A (en) Fluoroelastomers
US4530972A (en) Fluoride-containing polymer and composition containing same
JP2581182B2 (en) Cyclopolymerization method
EP1244715B1 (en) Aqueous emulsion polymerization process for the manufacturing of fluoropolymers
US9194982B2 (en) Optical member, process for producing same, and article provided with optical member
US5385981A (en) Thermoplastic fluoroelastomers produced by graft copolymerization
US5856417A (en) Fluorine-containing copolymer
CN103987738B (en) Fluorine allyl group sulfuryl azide monomer and polymkeric substance thus
EP0525687B1 (en) Ionically vulcanizable fluoroelastomeric copolymers
JP3278979B2 (en) Cold and alcohol resistant fluorinated elastic copolymer
JPH0718002A (en) Production of fluorocopolymer
JPH11171934A (en) Fluorine-containing copolymer