JPS6115897B2 - - Google Patents

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Publication number
JPS6115897B2
JPS6115897B2 JP54056912A JP5691279A JPS6115897B2 JP S6115897 B2 JPS6115897 B2 JP S6115897B2 JP 54056912 A JP54056912 A JP 54056912A JP 5691279 A JP5691279 A JP 5691279A JP S6115897 B2 JPS6115897 B2 JP S6115897B2
Authority
JP
Japan
Prior art keywords
fluorine
containing polymer
solution
group
polymer
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
JP54056912A
Other languages
Japanese (ja)
Other versions
JPS55149336A (en
Inventor
Tomonori Koorishima
Haruhisa Myake
Tatsuro Asawa
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 JP5691279A priority Critical patent/JPS55149336A/en
Publication of JPS55149336A publication Critical patent/JPS55149336A/en
Publication of JPS6115897B2 publication Critical patent/JPS6115897B2/ja
Granted legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Cell Separators (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

本発明は、含フツ玠ポリマヌの溶液に関し、曎
に詳しく蚀えば、カルボン酞゚ステル基含有のペ
ンダント偎鎖を有する特定の含フツ玠ポリマヌが
含フツ玠溶剀に溶解されおなる新芏な溶液に関す
るものである。 埓来より、含フツ玠ポリマヌは䞀般的に溶剀に
察する耐性を有するこずから、かゝる含フツ玠ポ
リマヌの溶液は殆んど知られおいない。特に、䞻
鎖骚栌炭玠原子にフツ玠原子が倚数結合した含フ
ツ玠ポリマヌを溶解し埗る溶剀は知られおいな
い。 䞀方、前蚘の劂き含フツ玠ポリマヌの溶液が埗
られるならば、皮々の商業的利甚の道が拡倧す
る。䟋えば、テトラフルオロ゚チレンの劂きフツ
玠化オレフむンずカルボン酞型偎鎖を有するフツ
玠化モノマヌずの共重合䜓は、耐酞化性、耐塩玠
性、耐アルカリ性、耐熱性の優れた陜むオン亀換
暹脂䜓ずしお、氎酞化アルカリず塩玠ずを補造す
る際の電解甚隔膜、燃料電池甚隔膜、䞀般透析甚
隔膜その他の倚くの甚途に䜿甚されるこずが、最
近泚目されおいる。そしお、かゝる含フツ玠ポリ
マヌを溶剀に溶解した溶液が埗られるならば、フ
むルム化の手段、操䜜が極めお容易になり、任意
の耇雑な圢状や極めお薄い隔膜も補造可胜ずなる
ず共に、含浞による隔膜の補造も円滑ずなり、曎
に隔膜におけるピンホヌルの補修や適宜物䜓衚面
の含フツ玠ポリマヌによる被芆も可胜になるな
ど、溶液化による皮々の利点がもたらされる。 䞻鎖骚栌炭玠原子に結合したフツ玠含量が倚い
含フツ玠ポリマヌ、䟋えばテトラフルオロ゚チレ
ン重合䜓、テトラフルオロ゚チレンヘキサフル
オロプロピレン共重合䜓、テトラフルオロ゚チレ
ンパヌフルオロアルキルビニル゚ヌテル共
重合䜓の劂きは、炭化氎玠系重合䜓に比しお難溶
性であり、ほずんどの溶剀に䞍溶である。かゝる
含フツ玠ポリマヌでも、スルホン酞のような極性
の高い匷酞性基を有する重合䜓の堎合には、特公
昭48−13333号公報に芋られるように、スルホン
酞基が酞、スルホンアミド又はスルホネヌトの劂
き特定の圢態にあるずきにのみ、䟋倖的に高極性
の有機溶剀に溶解するこずが知られおいる。 しかしながら、カルボン酞偎鎖を有する含フツ
玠ポリマヌの堎合には、偎鎖がカルボン酞基であ
るずいう違いのみで、スルホン酞偎鎖を有する含
フツ玠ポリマヌを良奜に溶解する有機溶剀にも溶
解性を瀺さない。䟋えば、前蚘特公昭48−13333
号公報の実斜䟋には、テトラフルオロ゚チレン
パヌフルオロ・−ゞオキサ−−メチル−
−オクテンスルホン酞の共重合䜓スルホン
酞単量䜓含有量17モル及び19モルが、スル
ホン酞基が酞の圢態のずき、−ブタノヌルやゞ
メチルアセトアミド䞭に溶解するこずが蚘茉され
おいるが、これに盞圓するカルボン酞偎鎖の含フ
ツ玠ポリマヌの堎合には、これらの溶剀には党く
溶解しない。そしお、かゝるカルボン酞偎鎖を有
する含フツ玠ポリマヌの溶解性に぀いおは党く知
られおいないず共に、末だ溶解するずいう報告は
芋圓らない。 本発明者は、前蚘の劂き䞻鎖骚栌炭玠原子に結
合したフツ玠含量が倚い含フツ玠ポリマヌを円滑
有利に溶解せしめる手段に぀いお皮々の研究、怜
蚎を重ねた結果、次の劂き新芏知芋を芋出し、前
蚘目的を達成するこずに初めお成功し、これを本
発明ずしお提䟛するものである。即ち、含フツ玠
ポリマヌに−COOCH3、−COOC4H9、−
COOC10H21、−COOC16H33、
The present invention relates to a solution of a fluorine-containing polymer, and more specifically, to a novel solution obtained by dissolving a specific fluorine-containing polymer having a pendant side chain containing a carboxylic acid ester group in a fluorine-containing solvent. be. Conventionally, since fluorine-containing polymers generally have resistance to solvents, solutions of such fluorine-containing polymers are hardly known. In particular, no solvent is known that can dissolve a fluorine-containing polymer in which a large number of fluorine atoms are bonded to the main chain carbon atoms. On the other hand, if a solution of a fluorine-containing polymer as described above can be obtained, various avenues for commercial use will be expanded. For example, a copolymer of a fluorinated olefin such as tetrafluoroethylene and a fluorinated monomer having a carboxylic acid type side chain is a cation exchange resin with excellent oxidation resistance, chlorine resistance, alkali resistance, and heat resistance. Recently, attention has been paid to its use as a membrane for electrolysis in the production of alkali hydroxide and chlorine, a membrane for fuel cells, a membrane for general dialysis, and many other uses. If a solution obtained by dissolving such a fluorine-containing polymer in a solvent could be obtained, the means and operations for forming a film would be extremely easy, and it would be possible to manufacture membranes with arbitrary complex shapes and extremely thin membranes. Various advantages are brought about by making the solution into a solution, such as facilitating the production of diaphragms, and also making it possible to repair pinholes in the diaphragms and appropriately coat the surfaces of objects with fluorine-containing polymers. Fluorine-containing polymers with a high fluorine content bonded to the main chain carbon atoms, such as tetrafluoroethylene polymers, tetrafluoroethylene/hexafluoropropylene copolymers, and tetrafluoroethylene/perfluoro(alkyl vinyl ether) copolymers. It is less soluble than hydrocarbon polymers and is insoluble in most solvents. Even in such fluorine-containing polymers, in the case of polymers having highly polar and strongly acidic groups such as sulfonic acid, as seen in Japanese Patent Publication No. 13333/1983, the sulfonic acid group is acid, sulfonamide, etc. It is known that only certain forms such as sulfonate or sulfonate are soluble in highly polar organic solvents. However, in the case of fluorine-containing polymers with carboxylic acid side chains, the only difference is that the side chains are carboxylic acid groups, and they are soluble in organic solvents that well dissolve fluorine-containing polymers with sulfonic acid side chains. Does not show gender. For example, the above-mentioned Special Publication Publication No. 48-13333
Examples of the publication include tetrafluoroethylene/
Perfluoro(3,6-dioxa-4-methyl-
7-octensulfonic acid) (sulfonic acid monomer content of 17 mol% and 19 mol%) can be dissolved in n-butanol and dimethylacetamide when the sulfonic acid group is in the acid form. However, corresponding fluorine-containing polymers with carboxylic acid side chains do not dissolve in these solvents at all. Furthermore, nothing is known about the solubility of such fluorine-containing polymers having carboxylic acid side chains, and there have been no reports that they are even soluble. The present inventor has conducted various studies and studies on means for smoothly and advantageously dissolving a fluorine-containing polymer with a high fluorine content bonded to the main chain carbon atoms as described above, and has discovered the following new knowledge. , has succeeded for the first time in achieving the above object, and this is provided as the present invention. That is, −COOCH 3 , −COOC 4 H 9 , −
COOC 10 H 21 , −COOC 16 H 33 ,

【匏】の 劂きカルボン酞゚ステル基含有のペンダント偎鎖
を導入するず、これをトリクロロトリフルオロ゚
タン、ベンゟトリフルオラむドの劂き含フツ玠溶
剀に溶解せしめるこずが可胜ずなるずいう事実を
芋出したものである。 かくしお、本発明は、前蚘知芋に基いお完成さ
れたものであり、カルボン酞゚ステル基含有のペ
ンダント偎鎖を有し䞔぀䞻鎖骚栌を構成する炭玠
原子に結合したフツ玠原子の含有量が該䞻鎖骚栌
炭玠原子の100重量郚圓り玄150〜313重量郚であ
る含フツ玠ポリマヌが、含フツ玠溶剀に溶解され
おなるこずを特城ずする含フツ玠ポリマヌの溶液
を新芏に提䟛するものである。 本発明で溶液ずされるカルボン酞゚ステル基含
有のペンダント偎鎖を有する特定の含フツ玠ポリ
マヌ以䞋、゚ステル型含フツ玠ポリマヌず略蚘
するこずがあるずしおは、ポリマヌに含たれる
カルボン酞゚ステル基の濃床が溶解性に関連する
ので、充分な溶解性をもたらしめるためには、奜
たしくは該濃床以䞋、むオン亀換容量ず呌ぶ
がメチル゚ステル換算で゚ステル型含フツ玠ポリ
マヌ圓り0.5〜3.0ミリ圓量、特に1.0〜2.5ミ
リ圓量であるこずが奜適である。又、カルボ
ン酞゚ステル基の皮類も溶解性に関連し、䞀般的
にぱステル基の炭玠数が倧きくなれば䜎いむオ
ン亀換容量でも溶解性は良奜ずなる。 而しお、゚ステル型含フツ玠ポリマヌは、カル
ボン酞゚ステル基又は該基に転換できる官胜基を
有する含フツ玠ビニル単量䜓の単独重合䜓あるい
は、かゝる単量䜓ずフツ玠化オレフむン、フツ玠
化ビニル゚ヌテルなどずの共重合䜓であるこずが
できる。カルボン酞゚ステル基に転換できる官胜
基の堎合には、重合埌に、官胜基に応じた適宜の
凊理によ぀おカルボン酞゚ステル基に転換され
る。たた、カルボン酞゚ステル基以倖の官胜基、
䟋えばスルホン酞型の官胜基を有する含フツ玠ポ
リマヌの還元凊理特開昭52−24175、52−
24176、52−24177号公報などを参照、酞化凊理
特開昭53−132094、53−132069号公報などを参
照などによ぀お、スルホン酞型官胜基をカルボ
ン酞型官胜基に倉え、曎にこれをカルボン酞゚ス
テル基に転換するこずによ぀おも、本発明におけ
る゚ステル型含フツ玠ポリマヌを入手可胜であ
る。 本発明における゚ステル型含フツ玠ポリマヌ
は、䞻鎖骚栌を構成する炭玠原子に結合したフツ
玠原子の含有量が該䞻鎖骚栌炭玠原子の100重量
郚圓り玄150〜313重量郚である。即ち、本発明で
は、かゝる䞻鎖骚栌炭玠䞊のフツ玠含有量が高い
含フツ玠ポリマヌに、前蚘カルボン酞゚ステル基
含有偎鎖を導入するこずにより、含フツ玠溶剀に
溶解せしめるものである。䞻鎖骚栌炭玠原子䞊の
フツ玠原子含量は、奜たしくは炭玠原子100重量
郚圓り玄200〜305重量郚皋床である。そしお、゚
ステル型含フツ玠ポリマヌのフツ玠含量は20〜60
重量皋床が遞定される。 前蚘゚ステル型含フツ玠ポリマヌの奜たしい䟋
ずしおは、次の繰り返し単䜍(ã‚€)及び(ロ)を含有する
ものが挙げられる。 (ã‚€) −CF2−CXX′− こゝで、は−、−Cl、−又は−CF3であ
り、X′は又は−CF2n−CF3であり、は
〜の敎数であり、は又はであり、は炭
玠数〜20個の有機基であり、は−・・
−又は−−・・−である。そし
お、は−CF2a−CXX′b−CF2c−であ
り、は−CF2−−CXX′d−であり、は−
CXX′−−CF2e−であり、・・は
、およびの少なくずも䞀぀を任意の順序で
配列するこずを衚わし、、、、および
は又は〜の敎数である。−・・−
又は−−・・−の具䜓䟋ずしおは、−
CF2−x、−−CF2x−、−−CF2−CFZ−
、−−CF2−CFZy−−CF2−CFRf−z、
−CF2x−CH2f−、−−CF2−CFZ−−
CF2y−CF2x−CF2−−CFRfz−などが挙
げられる。、、、は〜の敎数であ
り、、fは−又は炭玠数〜個のパヌフ
ルオロアルキル基である。 而しお、前蚘のは炭玠数〜20個の有機基で
あれば良く、通垞は次の劂きが䟋瀺され埗る。䟋
えば、メテル基、゚チル基、プロピル基、−ブ
チル基、−ヘキシル基、−゚チルヘキシル
基、デシル基、セチル基の劂き炭玠数〜20個の
脂肪族炭化氎玠基1H・1H・7H−ドデカフルオ
ロ−−ヘプチル基、1H・1H−ペンタデカフル
オロオクチル基、1H・1H・3H−テトラフルオロ
−−プロピル基、1H・1H・11H−゚むコサフ
ルオロ−−りンデシル基、・・−トリク
ロロ゚チル基、・・−トリクロロブチル基
の劂き炭玠数〜20個の含ハロゲン脂肪族炭化氎
玠基シクロヘキシル基、・−ゞメチルシク
ロヘキシル基、−クロロシクロヘキシル基の劂
き脂環匏炭化氎玠基及び含ハロゲン脂環匏炭化氎
玠基プニル基、トリル基、・−ゞクロロ
プニル基、−フルオロプニル基、−フル
オロプニル基、−フルオロプニル基、−
クロロプニル基、−クロロプニル基、−
クロロプニル基、−トリフルオロメチルプ
ニル基、−ニトロプニル基の劂きプニル基
及び眮換プニル基ベンゞル基、−クロロベ
ンゞル基、−フルオロベンゞル基、−ニトロ
ベンゞル基の劂きベンゞル基及び眮換ベンゞル基
などである。 本発明の奜適な実斜態様では、前蚘及び
X′が−である゚ステル型含フツ玠ポリマヌが
採甚される。たた、がであり、が−−
・・−であるこずが実際的である。曎
に、−−・・−が−−CF2CFZOy
−CF2x−CF2OCFRfz−であり、が〜
の敎数、、が又はであり、、fが−
CF3である゚ステル型含フツ玠ポリマヌは、特に
奜適なものずしお䟋瀺される。は繰り返し単䜍
(ロ)の含有割合に応じお遞定するのが望たしいが、
通垞は特に制限される理由がなく、前蚘の具䜓䟋
の䞭で入手の容易性などを考慮しお遞定される。
䟋えば、がアルキル基など脂肪族炭化氎玠基で
あるものは奜適であり、たた、ベンゞル基、プ
ニル基、シクロヘキシル基なども奜適である。 繰り返し単䜍(ã‚€)及び(ロ)からなる含フツ玠ポリマ
ヌの堎合、(ã‚€)ず(ロ)の組成割合は、前蚘所望のむオ
ン亀換容量を有するように遞定される。そしお、
゚ステル型含フツ玠ポリマヌの分子量は、所定の
容量流速を瀺す枩床で衚珟した堎合、メチル゚ス
テル型においお容量流速100mm秒を瀺す枩床
Tqが、奜たしくは130〜350℃、特には150〜
230℃のものである。かゝる゚ステル型含フツ玠
ポリマヌには、必芁に応じお、CF2CFOB
は炭玠数〜10個の含フツ玠アルキル基を瀺
す、CF2CF−CFCF2、CF2CFO−
CF21〜4−OCFCF2などの䞀皮又は二皮以䞊
の単量䜓から圢成される繰り返し単䜍が含たれお
いおも良い。 本明现曞䞭においお、容量流速ぱステル型含
フツ玠ポリマヌを30Kg/cm2加圧䞋、䞀定枩床の埄
mm、長さmmのオリフむスから熔融流出せし
め、流出する含フツ玠ポリマヌをmm秒の単䜍
で瀺したものである。たた、むオン亀換容量は、
次のようにしお求めた。即ち、゚ステル型含フツ
玠ポリマヌの゚ステル基を、苛性゜ヌダ氎溶液䞭
加氎分解しお−COONa基に倉え、該Na型ポリマ
ヌを1NのHCl䞭で60℃、時間攟眮しお完党に
型に転換し、HClが残存しないように氎で充分掗
浄した。その埌、この型ポリマヌ0.5を、
0.1NのNaOH25mlに氎を25ml加えおなる溶液䞭
に、宀枩で日間静眮した。次いで、ポリマヌを
ずり出しお、溶液䞭のNaOHの量を0.1NのHClで
逆滎定するこずにより求めるものである。 本発明における前蚘の劂き繰り返し単䜍(ã‚€)及び
(ロ)を含有する゚ステル型含フツ玠ポリマヌは、
CF2CXX′で衚わされるフツ玠化オレフむンず
It was discovered that by introducing a pendant side chain containing a carboxylic acid ester group such as [Formula], it becomes possible to dissolve it in a fluorine-containing solvent such as trichlorotrifluoroethane or benzotrifluoride. . Thus, the present invention has been completed based on the above findings, and the present invention has been completed based on the above-mentioned findings. To provide a novel solution of a fluorine-containing polymer, characterized in that the fluorine-containing polymer is dissolved in a fluorine-containing solvent in an amount of about 150 to 313 parts by weight per 100 parts by weight of main chain skeleton carbon atoms. It is. The specific fluorine-containing polymer having pendant side chains containing carboxylic acid ester groups (hereinafter sometimes abbreviated as ester-type fluorine-containing polymer) that is made into a solution in the present invention includes carboxylic acid esters contained in the polymer. Since the concentration of the group is related to solubility, in order to provide sufficient solubility, the concentration (hereinafter referred to as ion exchange capacity) is preferably
is preferably 0.5 to 3.0 milliequivalents, particularly 1.0 to 2.5 milliequivalents/g, in terms of methyl ester, per gram of the ester-type fluorine-containing polymer. Furthermore, the type of carboxylic acid ester group is also related to solubility; generally, the larger the number of carbon atoms in the ester group, the better the solubility even with a low ion exchange capacity. Therefore, the ester type fluorine-containing polymer is a homopolymer of a fluorine-containing vinyl monomer having a carboxylic acid ester group or a functional group convertible to the carboxylic acid ester group, or a combination of such a monomer and a fluorinated olefin. , a copolymer with fluorinated vinyl ether, etc. In the case of a functional group that can be converted into a carboxylic ester group, it is converted to a carboxylic ester group by an appropriate treatment depending on the functional group after polymerization. In addition, functional groups other than carboxylic acid ester groups,
For example, reduction treatment of fluorine-containing polymers having sulfonic acid type functional groups (JP-A-52-24175, 52-
24176, 52-24177, etc.), oxidation treatment (see JP-A-53-132094, 53-132069, etc.) to change the sulfonic acid type functional group to a carboxylic acid type functional group, Furthermore, the ester type fluorine-containing polymer of the present invention can also be obtained by converting it into a carboxylic acid ester group. In the ester type fluorine-containing polymer of the present invention, the content of fluorine atoms bonded to carbon atoms constituting the main chain skeleton is about 150 to 313 parts by weight per 100 parts by weight of the carbon atoms of the main chain skeleton. That is, in the present invention, the carboxylic acid ester group-containing side chain is introduced into a fluorine-containing polymer having a high fluorine content on the main chain carbon, thereby dissolving it in a fluorine-containing solvent. be. The content of fluorine atoms on the main chain skeleton carbon atoms is preferably about 200 to 305 parts by weight per 100 parts by weight of carbon atoms. The fluorine content of the ester type fluorine-containing polymer is 20 to 60.
Approximately % by weight is selected. Preferred examples of the ester type fluorine-containing polymer include those containing the following repeating units (a) and (b). (a) (−CF 2 −CXX′−) Here, X is -F, -Cl, -H or -CF3 , X' is X or -( CF2 ) n - CF3 , and m is 1
is an integer of ~5, n is 0 or 1, A is an organic group having 1 to 20 carbon atoms, and Y is -(P・Q・
R)- or -O-(P.Q.R)-. Then, P is −(CF 2 ) a −(CXX′) b −(CF 2 ) c −, Q is −(CF 2 −O−CXX′) d −, and R is −
(CXX'-O-CF 2 ) e -, (P・Q・R) represents arranging at least one of P, Q and R in any order, and a, b, c, d and e
is 0 or an integer from 1 to 6. -(P・Q・R)−
Or as a specific example of -O-(P・Q・R)-, (-
CF 2 −) x , −O−(CF 2 ) x −, (−O−CF 2 −CFZ−)
y , -(O- CF2 -CFZ) y- (O- CF2 -CFR f- ) z ,
−(CF 2 ) x −(CH 2 ) f −, −O−CF 2 −(CFZ−O−
Examples include CF2 ) y- ( CF2 ) x- ( CF2 -O- CFRf ) z- . x, y, z, and f are integers of 1 to 6, and Z and R f are -F or a perfluoroalkyl group having 1 to 6 carbon atoms. The above A may be any organic group having 1 to 20 carbon atoms, and the following examples are usually exemplified. For example, aliphatic hydrocarbon groups having 1 to 20 carbon atoms such as mether group, ethyl group, propyl group, n-butyl group, n-hexyl group, 2-ethylhexyl group, decyl group, and cetyl group; 1H, 1H, 7H-dodecafluoro-1-heptyl group, 1H・1H-pentadecafluorooctyl group, 1H・1H・3H-tetrafluoro-1-propyl group, 1H・1H・11H-eicosafluoro-1-undecyl group, 1・Halogen-containing aliphatic hydrocarbon groups having 1 to 20 carbon atoms such as 1,1-trichloroethyl group, 1,1,2-trichlorobutyl group; cyclohexyl group, 3,4-dimethylcyclohexyl group, 4-chlorocyclohexyl group Alicyclic hydrocarbon groups and halogen-containing alicyclic hydrocarbon groups such as phenyl group, tolyl group, 2,3-dichlorophenyl group, O-fluorophenyl group, m-fluorophenyl group, P- Fluorophenyl group, O-
Chlorophenyl group, m-chlorophenyl group, P-
Phenyl groups and substituted phenyl groups such as chlorophenyl group, 3-trifluoromethylphenyl group, 3-nitrophenyl group; benzyl group such as benzyl group, O-chlorobenzyl group, O-fluorobenzyl group, m-nitrobenzyl group; Substituted benzyl group, etc. In a preferred embodiment of the present invention, the X and
An ester type fluorine-containing polymer in which X' is -F is used. Also, n is 1 and Y is -O-
(P・Q・R)− is practical. Furthermore, -O-(P・Q・R)- is -O-(CF 2 CFZO) y
−(CF 2 ) x −(CF 2 OCFR f ) z −, and x is 1 to 6
The integers, y and z are 0 or 1, and Z and R f are -
An ester type fluorine-containing polymer such as CF 3 is particularly preferred. A is a repeating unit
It is desirable to select according to the content ratio of (b), but
Usually, there is no particular reason to limit it, and it is selected from among the above-mentioned specific examples in consideration of ease of acquisition.
For example, it is preferable that A is an aliphatic hydrocarbon group such as an alkyl group, and also a benzyl group, a phenyl group, a cyclohexyl group, etc. In the case of a fluorine-containing polymer consisting of repeating units (a) and (b), the composition ratio of (a) and (b) is selected so as to have the desired ion exchange capacity. and,
The molecular weight of the ester-type fluorine-containing polymer is expressed as a temperature at which a predetermined volumetric flow rate is exhibited, and the temperature (Tq) at which a volumetric flow rate of 100 mm 3 /sec is expressed in the methyl ester type is preferably 130 to 350°C, particularly 150°C. ~
It is at 230℃. Such ester-type fluorine-containing polymers may contain CF 2 = CFOB (B
represents a fluorine-containing alkyl group having 1 to 10 carbon atoms), CF 2 =CF−CF=CF 2 , CF 2 =CFO−
(CF 2 ) 1-4 -OCF=CF 2 A repeating unit formed from one or more types of monomers may be included. In this specification, the volumetric flow rate refers to an ester-type fluorinated polymer melted and flowed out from an orifice with a diameter of 1 mm and a length of 2 mm at a constant temperature under a pressure of 30 Kg/cm 2 , and the flow rate of the fluorinated polymer flowing out is mm 3 /sec. It is expressed in units of . In addition, the ion exchange capacity is
It was obtained as follows. That is, the ester groups of the ester-type fluorine-containing polymer are hydrolyzed in an aqueous solution of caustic soda to convert them into -COONa groups, and the Na-type polymer is left in 1N HCl at 60°C for 5 hours to completely hydrogenate.
The mixture was converted into a mold and thoroughly washed with water to ensure that no HCl remained. Then, add 0.5g of this H-type polymer to
It was left standing at room temperature for 2 days in a solution prepared by adding 25 ml of water to 25 ml of 0.1N NaOH. Next, the polymer is taken out and the amount of NaOH in the solution is determined by back titration with 0.1N HCl. The repeating unit (a) as described above in the present invention and
The ester type fluorine-containing polymer containing (b) is
CF 2 = fluorinated olefin represented by CXX′ and

【匏】で衚わされる重合胜のある含 フツ玠カルボン酞゚ステル単量䜓以䞋、単に゚
ステル単量䜓ず略蚘ずの共重合により容易に入
手され埗る。又、共重合の際に、゚ステル単量䜓
ずしおがメチル基や゚チル基であるメチル゚ス
テル単量䜓や゚チル゚ステル単量䜓を䜿甚し、埗
られるポリマヌを凊理するこずによ぀お、゚ステ
ル基をデシル゚ステル基、ブチル゚ステル基、セ
チル゚ステル基、プニル゚ステル基などに転化
するこずもできる。かゝる凊理ずしおは、゚ステ
ル基を、䞀旊酞型に倉えお該酞型を他の゚ステル
基に転化したり、あるいぱステル亀換反応など
により盎接他の゚ステル基に転化したりする手段
が適宜採甚され埗る。曎に、本発明においおは、
前蚘の通り、カルボン酞゚ステル基に転化できる
官胜基を有する含フツ玠ポリマヌから、加氎分
解、䞭和、還元、酞化などの各皮反応凊理によ
り、カルボン酞゚ステル基に倉えるこずなどによ
぀おも、前蚘の劂き特定゚ステル型含フツ玠ポリ
マヌを入手し埗るものである。 而しお、前蚘゚ステル型含フツ玠ポリマヌ䞭の
繰り返し単䜍(ロ)の含有モル比は、前蚘奜適なむオ
ン亀換容量ずなる様に遞定されるが、通垞は〜
30モル、奜たしくは10〜25モル皋床である。
繰り返し単䜍(ロ)の含有モル比が少なすぎるなどむ
オン亀換容量が䜙りに小さすぎるず、溶解性が䞍
充分ずなり、含フツ玠溶剀溶液ずしお実甚的なも
のが埗られ難くなる。たた、逆にむオン亀換容量
が䜙りに倧きすぎる堎合には、その分子量が小さ
くなる傟向にあり、その溶液から溶剀を飛散させ
た埌に埗られるフむルムの匷床が小さすぎるなど
の難点が認められる。 本発明で゚ステル型含フツ玠ポリマヌの溶解に
䜿甚される含フツ玠溶剀ずしおは、フツ玠含有量
が15重量以䞊あるものが奜適であり、皮々の含
フツ玠有機化合物が䟋瀺され埗る。䟋えば、・
・−トリクロロトリフルオロ゚タン、−ブ
ロモ−−フルオロ゚タン、−ブロモ−・
・−トリフルオロブテン−・−クロロ−
・−ゞブロモトリフルオロ゚タン、ヘプタフ
ルオロブチロニトリル、パヌフルオロ−−ヘプ
チルブロマむド、パヌフルオロオクタノニトリ
ル、ヘキサフルオロ−・・・−テトラク
ロロブタン、・−ゞクロロ−・−ゞフル
オロ゚タン、−ブロモ−−クロロ−・・
−トリフルオロ゚タンの劂き脂肪族フルオロ炭
化氎玠又は脂肪族フルオロニトリル化合物ビス
−フルオロプニル゚ヌテル、−ブロモ
プニルトリフルオロメチル゚ヌテル、−ブチ
ル−・・・−テトラフルオロ゚チル゚ヌ
テル、−クロロ−・・−トリフルオロ゚
チル゚チル゚ヌテル、−クロロ−・・−
トリフルオロメチル゚ヌテル、パヌフルオロ−
−ブチルテトラヒドロフランの劂きフツ玠化゚ヌ
テル化合物ビスパヌフルオロむ゜プロピル
ケトン、ヘキサフルオロアセチルアセトン、メチ
ルヘプタフルオロプロピルケトン、・・−
トリクロロトリフルオロアセトン、トリフルオロ
アセトプノンの劂きフツ玠化ケトン化合物
・−ゞクロロヘキサフルオロシクロブタン、
・−ゞクロロオクタフルオロシクロヘキセン
−の劂きフツ玠化脂環匏化合物ベンゟトリフ
ルオラむド、−ブロモベンゟトリフルオラむ
ド、−ブロモ−−クロロベンゟトリフルオラ
むド、−ブロモフルオロベンれン、−ブロモ
−−フルオロトル゚ン、−クロロベンゟトリ
フルオラむド、−クロロベンゟトリフルオラむ
ド、−クロロベンゟトリフルオラむド、−ク
ロロフルオロベンれン、−クロロ−−フルオ
ロニトロベンれン、・−ゞクロロベンゟトリ
フルオラむド、−ゞフルオロベンれン、・
−ゞフルオロトル゚ン、・−ゞトリフルオ
ロメチルベンれン、・−ゞトリフルオロ
メチルベンれンの劂きフツ玠化芳銙族化合物な
どが挙げられる。 本発明における含フツ玠溶剀ずしおは、実甚的
には容易に入手可胜であるずいうほかに、溶液か
ら溶剀を容易に陀去できるために、沞点が奜たし
くは250℃以䞋のものを採甚するのが良い。た
た、実際に特定含フツ玠ポリマヌ溶液の調補や取
り扱いの容易性などを考慮すれば、䜙りに䜎沞点
の含フツ玠溶剀は望たしくない。埓぀お、通垞は
沞点10〜250℃皋床、特に20〜220℃皋床の含フツ
玠溶剀を遞定するのが望たしい。かゝる芳点か
ら、本発明においおは、・・−トリクロロ
トリフルオロ゚タン、・−ゞクロロ−・
−ゞフルオロ゚タン、ベンゟトリフルオラむド、
及びベンゟトリフルオラむドのメチル、クロロ、
フルオロ、ニトロ、又はトリフルオロメチル基眮
換䜓などが特に奜適な含フツ玠溶剀ずしお䟋瀺さ
れ埗るものである。 ゚ステル型含フツ玠ポリマヌを含フツ玠溶剀に
溶解するにあた぀おは、前蚘特定の含フツ玠ポリ
マヌの所定量を溶剀䞭に添加し、必芁に応じお、
加熱、撹拌など既知の溶解促進手段を斜すなどに
より行なわれる。䜿甚する゚ステル型含フツ玠ポ
リマヌの圢状は、塊状物、フむルム、シヌト状、
繊維状、ロツド状、ペレツト状など劂䜕なるもの
でも良いが、溶解促進の芋地から奜たしくは20メ
ツシナ以䞊の现分䜓、䟋えば粒状物、粉末などで
あるのが望たしい。溶解に際しおの枩床は、高枩
であればあるほど溶解促進䞊奜たしく、通垞は20
〜250℃、奜たしくは30〜150℃にお行なわれる
が、溶解を促進させるため〜10気圧の加圧䞋で
実斜するこずもできる。 かくしお埗られる゚ステル型含フツ玠ポリマヌ
の溶液は、皮々の甚途に䜿甚できるが、特に該溶
液を泚型するか、又はアスベストもしくはポリテ
トラフルオロ゚チレンなどの倚孔質䜓に該溶液を
含浞させるこずにより、電解甚、透析甚、燃料電
池甚などの任意の圢状のフむルム、シヌト状物な
どを぀くるのに奜適であり、曎にはこのようにし
お぀く぀たフむルム又は他のフむルムにおけるピ
ンホヌルなどの損傷箇所を修埩するのに極めお有
効である。たた、該溶液を䜿甚するこずにより、
スペヌサヌネツト、電極などの物䜓の衚面被芆を
するのにも極めお䟿利になる。 次に本発明の実斜䟋に぀いお曎に具䜓的に説明
するが、かゝる説明によ぀お本発明が䜕ら限定さ
れるものでないこずは勿論である。尚、実斜䟋䞭
の郚は、特に明瀺しない限り重量郚である。 実斜䟋  テトラフルオロ゚チレンずCF2CFO
CF23COOCH3の共重合䜓からなり、むオン亀
換容量1.40ミリ圓量、容量流速100mm秒
を瀺す枩床以䞋Tq230℃を有するポリマヌ粉
末を、酢酞容量2N塩酞容量からなる溶液
に60℃で16時間浞挬しお、ポリマヌが有するむオ
ン亀換基を酞型ずしお也燥した。該酞型ポリマヌ
100郚、デシルアルコヌル600郚、濃硫酞郚の混
合物を、110℃で12時間加熱しお、むオン亀換基
をデシル゚ステル型に転化せしめ、デシル゚ステ
ル型ポリマヌ120郚を埗た。該デシル゚ステル型
ポリマヌ郚を、−クロロベンゟトリフルオラ
むド95郚に加え、100℃に加熱しお溶解埌、60℃
に冷华しお、デシル゚ステル型ポリマヌの重量
溶液を埗た。 実斜䟋  テトラフルオロ゚チレンずCF2CFO
CF23COOCH3の共重合䜓からなり、むオン亀
換容量1.7ミリ圓量、Tq215℃を有するポリ
マヌ粉末100郚を、ブタノヌル600郚ず濃硫酞郚
の混合物に加えお、110℃で12時間加熱しおむオ
ン亀換基がブチル゚ステルずな぀たポリマヌ107
郚を埗た。該ブチル゚ステル型ポリマヌ郚を
・・−トリフルオロトリクロロ゚タン97郚
䞭に溶解した60℃のポリマヌ溶液を埗た。 実斜䟋  テトラフルオロ゚チレンずCF2CFOCF2
COOCH3の共重合䜓からなり、むオン亀換容量
1.90ミリ圓量、Tq220℃を有するポリマヌ粉
末郚を、−クロロベンゟトリフルオラむド95
郚に加えお110℃に加熱しお溶解埌、60℃に冷华
しお濃床重量のポリマヌ溶液を埗た。 実斜䟋  テトラフルオロ゚チレンずCF2CFO
CF23COOCH3の共重合䜓からなり、むオン亀
換容量1.20ミリ圓量、Tq230℃を有するポリ
マヌ粉末を実斜䟋ず同様に凊理しお、そのむオ
ン亀換基を酞型ずし、該酞型ポリマヌ100郚ずセ
チルアルコヌル600郚ず濃硫酞郚の混合物を110
℃で12時間加熱した。むオン亀換基がセチル゚ス
テルずな぀たポリマヌ125郚を埗た。該セチル゚
ステル型ポリマヌ郚を−クロロベンゟトリフ
ルオラむド95郚に加え、100℃に加熱しお溶解
埌、60℃に冷华しおセチル゚ステル型ポリマヌの
重量溶液を埗た。 実斜䟋  テトラフルオロ゚チレンず
It can be easily obtained by copolymerization with a polymerizable fluorine-containing carboxylic acid ester monomer represented by the formula (hereinafter simply referred to as ester monomer). In addition, during copolymerization, a methyl ester monomer or an ethyl ester monomer in which A is a methyl group or an ethyl group is used as the ester monomer, and the resulting polymer is treated to form an ester group. can also be converted into a decyl ester group, a butyl ester group, a cetyl ester group, a phenyl ester group, etc. As such a treatment, a method of first converting the ester group into an acid form and then converting the acid form into another ester group, or directly converting it into another ester group by transesterification etc. is adopted as appropriate. can be done. Furthermore, in the present invention,
As mentioned above, a fluorine-containing polymer having a functional group that can be converted into a carboxylic acid ester group can be converted into a carboxylic acid ester group through various reaction treatments such as hydrolysis, neutralization, reduction, and oxidation. The specific ester-type fluorine-containing polymer described above can be obtained. The molar ratio of the repeating units (b) in the ester-type fluorine-containing polymer is selected so as to provide the suitable ion exchange capacity, but is usually 5 to 5.
It is about 30 mol%, preferably about 10 to 25 mol%.
If the ion exchange capacity is too low, such as when the molar ratio of the repeating unit (b) is too low, the solubility will be insufficient and it will be difficult to obtain a practical fluorine-containing solvent solution. On the other hand, if the ion exchange capacity is too large, the molecular weight tends to decrease, resulting in problems such as the strength of the film obtained after scattering the solvent from the solution. The fluorine-containing solvent used for dissolving the ester-type fluorine-containing polymer in the present invention preferably has a fluorine content of 15% by weight or more, and various fluorine-containing organic compounds may be exemplified. For example, 1.
1,2-trichlorotrifluoroethane, 1-bromo-2-fluoroethane, 4-bromo-1.
1,2-trifluorobutene-1,1-chloro-
1,1-dibromotrifluoroethane, heptafluorobutyronitrile, perfluoro-n-heptyl bromide, perfluorooctanonitrile, hexafluoro-2,2,3,3-tetrachlorobutane, 1,2-dichloro- 1,2-difluoroethane, 1-bromo-2-chloro-1,1.
Aliphatic fluorohydrocarbons or aliphatic fluoronitrile compounds such as 2-trifluoroethane; bis(P-fluorophenyl) ether, P-bromophenyl trifluoromethyl ether, n-butyl-1, 1, 2, 2 -tetrafluoroethyl ether, 2-chloro-1,1,2-trifluoroethyl ethyl ether, 2-chloro-1,1,2-
Trifluoromethyl ether, perfluoro-2
-Fluorinated ether compounds such as butyltetrahydrofuran; bis(perfluoroisopropyl)
Ketone, hexafluoroacetylacetone, methylheptafluoropropyl ketone, 1, 1, 3-
Fluorinated ketone compounds such as trichlorotrifluoroacetone and trifluoroacetophenone;
1,2-dichlorohexafluorocyclobutane,
Fluorinated alicyclic compounds such as 1,2-dichlorooctafluorocyclohexene-1; benzotrifluoride, O-bromobenzotrifluoride, 3-bromo-4-chlorobenzotrifluoride, O-bromofluorobenzene, 2- Bromo-4-fluorotoluene, O-chlorobenzotrifluoride, m-chlorobenzotrifluoride, P-chlorobenzotrifluoride, O-chlorofluorobenzene, 3-chloro-4-fluoronitrobenzene, 2,4-dichlorobenzotrifluoride Ride, O-difluorobenzene, 2.4
Examples include fluorinated aromatic compounds such as -difluorotoluene, 1,3-di(trifluoromethyl)benzene, and 1,4-di(trifluoromethyl)benzene. As the fluorine-containing solvent used in the present invention, it is preferable to use one having a boiling point of preferably 250°C or less, since it is practically easily available and the solvent can be easily removed from the solution. . In addition, when considering the ease of preparing and handling the specific fluorine-containing polymer solution, a fluorine-containing solvent having an excessively low boiling point is not desirable. Therefore, it is usually desirable to select a fluorine-containing solvent with a boiling point of about 10 to 250°C, particularly about 20 to 220°C. From this point of view, in the present invention, 1,1,2-trichlorotrifluoroethane, 1,2-dichloro-1,2
-difluoroethane, benzotrifluoride,
and benzotrifluoride methyl, chloro,
Particularly suitable fluorine-containing solvents include those substituted with fluoro, nitro, or trifluoromethyl groups. When dissolving the ester-type fluorine-containing polymer in a fluorine-containing solvent, a predetermined amount of the specific fluorine-containing polymer is added to the solvent, and if necessary,
This is carried out by applying known dissolution promoting means such as heating and stirring. The shape of the ester type fluorine-containing polymer used is lump, film, sheet,
It may be in any form such as fibrous, rod, or pellet, but from the viewpoint of promoting dissolution, it is preferably in the form of fine particles of 20 or more meshes, such as granules or powder. The higher the temperature at the time of dissolution, the more favorable it is for promoting dissolution, and is usually 20°C.
The reaction is carried out at a temperature of -250°C, preferably 30 - 150°C, but can also be carried out under an increased pressure of 1 - 10 atm to promote dissolution. The solution of the ester-type fluorine-containing polymer thus obtained can be used for various purposes, but in particular, it can be used by casting the solution or impregnating a porous material such as asbestos or polytetrafluoroethylene with the solution. It is suitable for making films of arbitrary shapes, sheets, etc. for use in electrolysis, dialysis, fuel cells, etc., and is also suitable for removing damaged parts such as pinholes in films made in this way or other films. Extremely effective for repair. Moreover, by using the solution,
It is also extremely useful for coating the surface of objects such as spacer nets and electrodes. Next, embodiments 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. Incidentally, parts in the examples are parts by weight unless otherwise specified. Example 1 Tetrafluoroethylene and CF 2 =CFO
A polymer powder consisting of a copolymer of (CF 2 ) 3 COOCH 3 and having an ion exchange capacity of 1.40 meq/g and a temperature (Tq) of 230°C exhibiting a volumetric flow rate of 100 mm 3 /sec was mixed with 1 volume of acetic acid/2N hydrochloric acid. The polymer was immersed in a solution of 1 volume at 60° C. for 16 hours to convert the ion exchange groups of the polymer into an acid form and then dried. The acid type polymer
A mixture of 100 parts of decyl alcohol, 600 parts of decyl alcohol, and 2 parts of concentrated sulfuric acid was heated at 110° C. for 12 hours to convert the ion exchange group to a decyl ester type polymer, thereby obtaining 120 parts of a decyl ester type polymer. Add 5 parts of the decyl ester type polymer to 95 parts of P-chlorobenzotrifluoride, heat to 100°C to dissolve, and then heat to 60°C.
A 5% by weight solution of the decyl ester type polymer was obtained. Example 2 Tetrafluoroethylene and CF 2 =CFO
100 parts of a polymer powder consisting of a copolymer of (CF 2 ) 3 COOCH 3 and having an ion exchange capacity of 1.7 meq/g and a Tq of 215°C was added to a mixture of 600 parts of butanol and 2 parts of concentrated sulfuric acid, and the mixture was heated at 110°C. Polymer 107 whose ion exchange group became butyl ester after heating for 12 hours
I got the department. A polymer solution at 60° C. was obtained by dissolving 3 parts of the butyl ester type polymer in 97 parts of 1,1,2-trifluorotrichloroethane. Example 3 Tetrafluoroethylene and CF 2 =CFO (CF 2 )
Composed of a copolymer of COOCH 3 , with ion exchange capacity
5 parts of polymer powder having 1.90 meq/g and Tq 220°C were added to O-chlorobenzotrifluoride 95
After heating to 110°C to dissolve, the mixture was cooled to 60°C to obtain a polymer solution having a concentration of 5% by weight. Example 4 Tetrafluoroethylene and CF 2 =CFO
A polymer powder consisting of a copolymer of (CF 2 ) 3 COOCH 3 and having an ion exchange capacity of 1.20 meq/g and a Tq of 230°C was treated in the same manner as in Example 1 to convert the ion exchange group into an acid form, and to 110 parts of a mixture of 100 parts of acid type polymer, 600 parts of cetyl alcohol, and 2 parts of concentrated sulfuric acid.
Heated at ℃ for 12 hours. 125 parts of a polymer in which the ion exchange group was cetyl ester was obtained. 5 parts of the cetyl ester type polymer were added to 95 parts of O-chlorobenzotrifluoride, heated to 100°C to dissolve, and then cooled to 60°C to obtain a 5% by weight solution of the cetyl ester type polymer. Example 5 Tetrafluoroethylene and

【匏】の共重合䜓 からなり、むオン亀換容量1.32ミリ圓量、
Tq224℃を有するポリマヌ粉末を、実斜䟋ず同
様に凊理しお、そのむオン亀換基をデシル゚ステ
ル型ずした。該デシル゚ステル型ポリマヌ郚を
−クロロベンゟトリフルオラむド95郚に加え、
110℃に加熱しお溶解埌、60℃に冷华しおデシル
゚ステル型ポリマヌの重量溶液を埗た。 実斜䟋  テトラフルオロ゚チレンず
It consists of a copolymer of [formula], with an ion exchange capacity of 1.32 milliequivalents/g,
A polymer powder having a Tq of 224° C. was treated in the same manner as in Example 1 to convert the ion exchange group into a decyl ester type. Adding 5 parts of the decyl ester type polymer to 95 parts of O-chlorobenzotrifluoride,
After heating to 110°C to dissolve, the mixture was cooled to 60°C to obtain a 5% by weight solution of the decyl ester type polymer. Example 6 Tetrafluoroethylene and

【匏】の共重合䜓から なり、むオン亀換容量1.40ミリ圓量、Tq215
℃を有するポリマヌ粉末100郚を、プノヌル600
郚ず濃硫酞郚ず混合し、110℃で12時間加熱し
おむオン亀換基がプニル゚ステル型ずな぀たポ
リマヌ105郚を埗た。該プニル゚ステル型ポリ
マヌ郚を−クロロベンゟトリフルオラむド97
郚に加えお100℃に加熱しお溶解埌、60℃に冷华
しおプニル゚ステル型ポリマヌの重量溶液
を埗た。 実斜䟋  テトラフルオロ゚チレンずCF2CFO
CF23COOCH3の共重合䜓からなり、むオン亀
換容量1.50ミリ圓量を有する厚さ200Όの含
フツ玠ポリマヌフむルムを、NaOH氎溶液䞭加氎
分解しおNa型ずした。該膜にカミ゜リで長さ
mmの傷を付けたのち、該膜を甚いお、陜極ず陰極
ずを区画し、宀型電解槜を圢成した。陜極には
ロゞりム被芆チタン電極、陰極にはステンレスを
それぞれ䜿甚し、極間距離2.2cm、膜の有効面積
を25cm2ずし、䞋蚘の条件で塩化ナトリりム氎溶液
の電解を行ない氎酞化ナトリりムを補造した。 陜極宀には4Nの塩化ナトリりム氎溶液、陰極
宀には12Nの氎酞化ナトリりム氎溶液を仕蟌み、
陜極宀には4Nの塩化ナトリりム氎溶液を150ml
時、陰極宀には、そこから埗られる氎酞化ナトリ
りムの濃床が、玄14.4Nになるように所定量の氎
をそれぞれ䟛絊しながら、電解槜の電流密床20
A/dm2、液枩85℃にお電解を行な぀たが、電解の
結果埗られた14.4NのNaOHからなる陰極液䞭に
はNaClが1130ppm含たれおいた。 カミ゜リでmmの切傷の぀いた膜面に、酢酞
容、2N HCl1容からなる溶液を振りかけ、膜を
時間攟眮したのち颚也し、さらに60℃に加熱し
た。カミ゜リでmmの切傷の぀いた郚分に実斜䟋
のデシル゚ステル型ポリマヌの重量溶液を
泚ぎ、颚也しお切傷を修理した。切傷を修理した
膜をNaOH氎溶液䞭で凊理しお、修理した郚分の
むオン亀換基をナトリりム塩型ずしお、再び塩化
ナトリりム氎溶液の電気分解に甚いた。極間電圧
3.8ボルトおいお陰極宀から14.4NのNaOH氎溶液
が96の電流効率で埗られ、そのなかに含たれる
NaClは20ppmであ぀た。 実斜䟋  フツ玠暹脂倚孔䜓フむルムであるフロロポア
FP200䜏友電工瀟補を実斜䟋のデシル゚ス
テル型ポリマヌの重量溶液に30分浞挬埌、匕
䞊げ、颚也しおデシル゚ステル型ポリマヌが付着
した倚孔䜓フむルムを埗た。このフむルムを
NaOH氎溶液で凊理しお付着ポリマヌのむオン亀
換基をNa型ずした。Na型ポリマヌを付着したフ
ツ玠暹脂倚孔䜓は也燥埌も、氎に浞挬すれば容易
に氎に濡れた。 䞀方、䞊蚘凊理をしないフロロポアFP200は
党く氎に濡れなか぀た。
Consisting of a copolymer of [formula], ion exchange capacity 1.40 meq/g, Tq215
100 parts of polymer powder, 600 parts of phenol
1 part and 2 parts of concentrated sulfuric acid and heated at 110°C for 12 hours to obtain 105 parts of a polymer in which the ion exchange group was of the phenyl ester type. 3 parts of the phenyl ester type polymer is P-chlorobenzotrifluoride97
After heating to 100°C to dissolve, the mixture was cooled to 60°C to obtain a 3% by weight solution of phenyl ester type polymer. Example 7 Tetrafluoroethylene and CF 2 =CFO
A 200Ό thick fluorine-containing polymer film made of a copolymer of (CF 2 ) 3 COOCH 3 and having an ion exchange capacity of 1.50 meq/g was hydrolyzed in an aqueous NaOH solution to form the Na type. Cut a length of 2 into the membrane with a razor.
After making a scratch of mm, the membrane was used to partition an anode and a cathode to form a two-chamber electrolytic cell. A rhodium-coated titanium electrode was used as the anode, and stainless steel was used as the cathode. The distance between the electrodes was 2.2 cm, and the effective area of the membrane was 25 cm 2 . Sodium hydroxide was produced by electrolyzing a sodium chloride aqueous solution under the following conditions. A 4N aqueous sodium chloride solution was placed in the anode chamber, and a 12N aqueous sodium hydroxide solution was placed in the cathode chamber.
Add 150ml of 4N sodium chloride solution to the anode chamber.
At this time, a predetermined amount of water was supplied to the cathode chamber so that the concentration of sodium hydroxide obtained therefrom was approximately 14.4N, and the current density of the electrolytic cell was 20N.
Electrolysis was carried out at A/dm 2 and a liquid temperature of 85°C, and the catholyte containing 14.4N NaOH obtained as a result of electrolysis contained 1130 ppm of NaCl. Acetic acid 3.
volume, sprinkle with a solution consisting of 1 volume of 2N HCl and incubate the membrane for 3
After being left for a while, it was air-dried and further heated to 60°C. A 5% by weight solution of the decyl ester type polymer of Example 1 was poured into a 2 mm incision made with a razor, and the cut was repaired by air drying. The membrane with the repaired cut was treated in an aqueous NaOH solution, and the ion exchange group in the repaired area was converted into a sodium salt form, which was then used again for electrolysis of an aqueous sodium chloride solution. Voltage between poles
At 3.8 volts, a 14.4N NaOH aqueous solution is obtained from the cathode chamber with a current efficiency of 96%, and it contains
NaCl was 20 ppm. Example 8 Fluoropore, a porous fluororesin film
FP200 (manufactured by Sumitomo Electric Industries, Ltd.) was immersed in a 5% by weight solution of the decyl ester type polymer of Example 1 for 30 minutes, then pulled up and air-dried to obtain a porous film to which the decyl ester type polymer was attached. this film
The ion exchange group of the attached polymer was changed to Na type by treatment with an aqueous NaOH solution. Even after drying, the porous fluororesin material with the Na-type polymer attached easily became wet when immersed in water. On the other hand, Fluoropore FP200 without the above treatment did not get wet with water at all.

Claims (1)

【特蚱請求の範囲】  カルボン酞゚ステル基含有のペンダント偎鎖
を有し䞔぀䞻鎖骚栌を構成する炭玠原子に結合し
たフツ玠原子の含有量が該䞻鎖骚栌炭玠原子の
100重量郚圓り玄150〜313重量郚である含フツ玠
ポリマヌが、含フツ玠溶剀に溶解されおなるこず
を特城ずする含フツ玠ポリマヌの溶液。  カルボン酞゚ステル基の濃床がメチル゚ステ
ル換算で含フツ玠ポリマヌ圓り0.5〜3.0ミリ
圓量である特蚱請求の範囲第項蚘茉の含フツ玠
ポリマヌの溶液。  含フツ玠ポリマヌのフツ玠含有量が20〜60重
量である特蚱請求の範囲第項蚘茉の含フツ玠
ポリマヌ溶液。  含フツ玠ポリマヌの本文䞭に定矩する容量流
速100mm秒を瀺す枩床が130〜350℃である特
蚱請求の範囲第項蚘茉の含フツ玠ポリマヌの溶
液。  含フツ玠ポリマヌが次の繰り返し単䜍(ã‚€)及び
(ロ)を含有する特蚱請求の範囲第項蚘茉の含フツ
玠ポリマヌの溶液。 (ã‚€) −CF2−CXX′− ここで、は−、−Cl、−又は−CF3であ
り、X′は又は−CF2n−CF3であり、は
〜の敎数であり、は又はであり、は炭
玠数〜20個の有機基であり、は−・・
−又は−−・・−である。そし
お、は−CF2a−CXX′b−CF2c−であ
り、は−CF2−−CXX′d−であり、は−
CXX′−−CF2e−であり、・・は
、およびの少なくずも䞀぀を任意の順序で
配列するこずを衚わし、、、、および
は又は〜の敎数である。  含フツ玠ポリマヌがCF2CXX′で衚わされ
るフツ玠化オレフむン単量䜓ず
【匏】で衚わされる重合胜のある含 フツ玠カルボン酞゚ステル単量䜓ずの共重合䜓で
ある特蚱請求の範囲第項蚘茉の含フツ玠ポリマ
ヌの溶液。  含フツ玠ポリマヌ䞭の繰り返し単䜍
【匏】の含有モル比が〜30モ ルである特蚱請求の範囲第項又は第項蚘茉
の含フツ玠ポリマヌの溶液。  含フツ玠溶剀のフツ玠含有量が15重量以䞊
である特蚱請求の範囲第項蚘茉の含フツ玠ポリ
マヌの溶液。  含フツ玠溶剀の沞点が10〜250℃である特蚱
請求の範囲第項又は第項蚘茉の含フツ玠ポリ
マヌ溶液。  溶液䞭の含フツ玠ポリマヌ濃床が重量
以䞊である特蚱請求の範囲第項蚘茉の含フツ玠
ポリマヌの溶液。  が炭玠数〜20個の脂肪族、脂環族、又
は芳銙族炭化氎玠基およびそれから誘導される基
から遞択される特蚱請求の範囲第項、第項、
又は第項蚘茉の含フツ玠ポリマヌの溶液。  含フツ玠溶剀が、・・−トリクロロ
トリフルオロ゚タンである特蚱請求の範囲第項
又は第項蚘茉の含フツ玠ポリマヌの溶液。  含フツ玠溶剀がベンゟトリフルオラむドお
よびそれのメチル基、クロロ基、フルオロ基、ニ
トロ基、又はトリフルオロメチル基眮換䜓から遞
択される特蚱請求の範囲第項又は第項蚘茉の
含フツ玠ポリマヌの溶液。
[Scope of Claims] 1. The content of fluorine atoms having a pendant side chain containing a carboxylic acid ester group and bonded to carbon atoms constituting the main chain skeleton is equal to
A solution of a fluorine-containing polymer, characterized in that about 150 to 313 parts by weight of the fluorine-containing polymer per 100 parts by weight is dissolved in a fluorine-containing solvent. 2. The solution of the fluorine-containing polymer according to claim 1, wherein the concentration of carboxylic acid ester groups is 0.5 to 3.0 milliequivalents per gram of the fluorine-containing polymer in terms of methyl ester. 3. The fluorine-containing polymer solution according to claim 1, wherein the fluorine-containing polymer has a fluorine content of 20 to 60% by weight. 4. The solution of the fluorine-containing polymer according to claim 1, wherein the temperature at which the volume flow rate of the fluorine-containing polymer as defined in the text of the fluorine-containing polymer is 100 mm 3 /sec is 130 to 350°C. 5 The fluorine-containing polymer has the following repeating units (a) and
A solution of a fluorine-containing polymer according to claim 1, which contains (b). (a) (−CF 2 −CXX′−) Here, X is -F, -Cl, -H or -CF3 , X' is X or -( CF2 ) n - CF3 , and m is 1
is an integer of ~5, n is 0 or 1, A is an organic group having 1 to 20 carbon atoms, and Y is -(P・Q・
R)- or -O-(P・Q・R)-. Then, P is −(CF 2 ) a −(CXX′) b −(CF 2 ) c −, Q is −(CF 2 −O−CXX′) d −, and R is −
(CXX'-O-CF 2 ) e -, (P・Q・R) represents arranging at least one of P, Q and R in any order, and a, b, c, d and e
is 0 or an integer from 1 to 6. 6 A patent claim in which the fluorine-containing polymer is a copolymer of a fluorinated olefin monomer represented by CF 2 =CXX′ and a fluorine-containing carboxylic acid ester monomer having polymerizability represented by the formula A solution of the fluorine-containing polymer according to item 5. 7. The solution of a fluorine-containing polymer according to claim 5 or 6, wherein the molar ratio of the repeating unit [formula] in the fluorine-containing polymer is 5 to 30 mol%. 8. The solution of a fluorine-containing polymer according to claim 1, wherein the fluorine content of the fluorine-containing solvent is 15% by weight or more. 9. The fluorine-containing polymer solution according to claim 1 or 8, wherein the fluorine-containing solvent has a boiling point of 10 to 250°C. 10 Fluorine-containing polymer concentration in solution is 1% by weight
A solution of a fluorine-containing polymer according to claim 1, which is as follows. 11 Claims 5 and 6, wherein A is selected from aliphatic, alicyclic, or aromatic hydrocarbon groups having 1 to 20 carbon atoms and groups derived therefrom;
Or the solution of the fluorine-containing polymer according to item 7. 12. The solution of a fluorine-containing polymer according to claim 8 or 9, wherein the fluorine-containing solvent is 1,1,2-trichlorotrifluoroethane. 13. The fluorine-containing solvent according to claim 8 or 9, wherein the fluorine-containing solvent is selected from benzotrifluoride and its substituted products with a methyl group, a chloro group, a fluoro group, a nitro group, or a trifluoromethyl group. solution of basic polymers.
JP5691279A 1979-05-11 1979-05-11 Fluorine-containing polymer solution Granted JPS55149336A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5691279A JPS55149336A (en) 1979-05-11 1979-05-11 Fluorine-containing polymer solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5691279A JPS55149336A (en) 1979-05-11 1979-05-11 Fluorine-containing polymer solution

Publications (2)

Publication Number Publication Date
JPS55149336A JPS55149336A (en) 1980-11-20
JPS6115897B2 true JPS6115897B2 (en) 1986-04-26

Family

ID=13040664

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7045044B2 (en) 2000-09-27 2006-05-16 Asahi Kasei Chemicals Corporation Dispersion composition containing perfluorocarbon-based copolymer

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4433082A (en) * 1981-05-01 1984-02-21 E. I. Du Pont De Nemours And Company Process for making liquid composition of perfluorinated ion exchange polymer, and product thereof
US4453991A (en) * 1981-05-01 1984-06-12 E. I. Du Pont De Nemours And Company Process for making articles coated with a liquid composition of perfluorinated ion exchange resin
US4784882A (en) * 1985-05-31 1988-11-15 The Dow Chemical Company Method for forming composite polymer films
HUT44053A (en) * 1985-05-31 1988-01-28 Dow Chemical Co New fluoropolymer solutions
US5290846A (en) * 1992-08-28 1994-03-01 E. I. Du Pont De Nemours And Company Solvents for fluorinated polymers
US5364929A (en) * 1993-01-13 1994-11-15 E. I. Du Pont De Nemours And Company Dissolution of tetrafluoroethylene polymers at superautogenous pressure
WO2002072694A1 (en) * 2001-02-13 2002-09-19 Asahi Kasei Kabushiki Kaisha Ion-exchange fluororesin precursor composition
JP2007153960A (en) * 2005-12-01 2007-06-21 Yunimatekku Kk Fluorine-containing copolymer and article on which thin film thereof is formed

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7045044B2 (en) 2000-09-27 2006-05-16 Asahi Kasei Chemicals Corporation Dispersion composition containing perfluorocarbon-based copolymer

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Publication number Publication date
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