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JPS59187006A - Highly dielectric fluororesin film - Google Patents

Highly dielectric fluororesin film

Info

Publication number
JPS59187006A
JPS59187006A JP6195583A JP6195583A JPS59187006A JP S59187006 A JPS59187006 A JP S59187006A JP 6195583 A JP6195583 A JP 6195583A JP 6195583 A JP6195583 A JP 6195583A JP S59187006 A JPS59187006 A JP S59187006A
Authority
JP
Japan
Prior art keywords
film
fluorine gas
vinylidene fluoride
resin
vdf
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
JP6195583A
Other languages
Japanese (ja)
Inventor
Kazuhiko Yamamoto
和彦 山本
「ねじ」垣 和美
Kazumi Nejigaki
Takashi Yasumura
安村 崇
Shuichi Inoue
周一 井上
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.)
Central Glass Co Ltd
JSR Corp
Nippon Synthetic Chemical Industry Co Ltd
Original Assignee
Central Glass Co Ltd
Nippon Synthetic Chemical Industry Co Ltd
Japan Synthetic Rubber 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 Central Glass Co Ltd, Nippon Synthetic Chemical Industry Co Ltd, Japan Synthetic Rubber Co Ltd filed Critical Central Glass Co Ltd
Priority to JP6195583A priority Critical patent/JPS59187006A/en
Publication of JPS59187006A publication Critical patent/JPS59187006A/en
Pending legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Organic Insulating Materials (AREA)

Abstract

PURPOSE:To obtain titled film with improved solvent resistance, useful as a material for various devices, by the fluorine gas treatment and film-forming operation of a vinylidene fluoride resin having a specific amount of vinylidene fluoride. CONSTITUTION:The objective film can be obtained by carrying out a fluorine gas treatment (e.g., using a fluorine gas diluted with inert gas such as He, Ne, at -80 deg.C- the resin melting point, while gradually raising fluorine gas concentration) and film-forming operation of a vinylidene fluoride resin having >=50mol%, as monomer unit, of vinylidene fluoride. The above treatments (or operations) may be performed in any order.

Description

【発明の詳細な説明】 本発明は高誘電率を有するふっ素樹脂フィルムに関する
。さらに詳【−<は、ぶつ化ビニリデン(以下、VDF
と略す)系樹脂を直接ふつ素化することによシ得られる
高誘電性ふっ素樹脂フィルムに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluororesin film having a high dielectric constant. Further details [-< means vinylidene buttoxide (hereinafter referred to as VDF)
This invention relates to a highly dielectric fluororesin film obtained by directly fluorinating a (abbreviated as ) type resin.

VDF系樹脂は高い双極子能率を持つ炭素−ふっ素結合
を有t/ 、その構造の特異性によシ、高い誘電率を示
すポリマーである。たとえば、ポリぶつ化ビニリデン樹
脂(以下、PvDFと略す)より得られるフィルムは比
誘電率で8〜9(IKHz )という高い値を示す。こ
のような特性を生かして、PvDFフィルムはコンデン
サーあるいはエレクトロルミネセンスなどの各種デバイ
ス用材料としての利用が検討されている。しかしながら
最近では、電子技術の発達に伴い、さらに高い誘電率を
有するポリマー材料の出現が期待されている。
VDF resin is a polymer that has carbon-fluorine bonds with high dipole efficiency and exhibits a high dielectric constant due to its unique structure. For example, a film obtained from polyvinylidene dibutride resin (hereinafter abbreviated as PvDF) exhibits a high value of dielectric constant of 8 to 9 (IKHz). Taking advantage of these characteristics, PvDF film is being considered for use as a material for various devices such as capacitors and electroluminescence. However, recently, with the development of electronic technology, it is expected that polymer materials with even higher dielectric constants will appear.

そこで本発明者らは、鋭意研究の結果、VDF系樹脂を
ふっ素ガスで処理したものが高い誘電率を有することを
見出し、高誘電性フィルムを得ることに成功した。
As a result of intensive research, the present inventors discovered that a VDF resin treated with fluorine gas has a high dielectric constant, and succeeded in obtaining a highly dielectric film.

ところで、ポリマーをふっ素ガスによ多処理する試みは
、古くはA、 J、 Rudgeによるポリエチレン表
面のふつ素化に関する英国特許710,523(195
4)を始めとして、ポリスチレン、ポリメタクリル酸メ
チル、ポリカーボネートなど炭化水素系ポリマーを中心
に種々行なわれて来ている。
By the way, attempts to treat polymers with fluorine gas have been made in British Patent No. 710,523 (195
In addition to 4), various methods have been used mainly for hydrocarbon polymers such as polystyrene, polymethyl methacrylate, and polycarbonate.

またポリエーテル系ポリマーをふっ素ガスで処理するこ
とKより、ふつ素糸オリゴマーを得る特開昭52−24
298の試みなども行なわれているが、ふつ素糸ポリマ
ーのふっ素ガス処理による方法、とくに高誘電特性に着
目17た改質は知られていない。上述のようにふっ素ガ
スを使用【2てポリマーをふつ素化する目的は、炭化水
素系ポリマーの場合、ポリマー表面の水素原子をふっ素
原子に交換することによって、ふつ素糸ポリマーの持つ
特異な性能、すなわち表面エネルギーの低下に伴なう撥
水撥油性、摩擦係数の低下に伴なう高摺動性、さらには
耐熱性、耐溶剤性の向上などの発現を期待することにあ
った。
Furthermore, by treating a polyether polymer with fluorine gas, a double thread oligomer can be obtained from JP-A-52-24.
298 have been attempted, but there are no known methods for treating double-stranded polymers with fluorine gas, especially for modifying them with a focus on high dielectric properties. As mentioned above, using fluorine gas [2] The purpose of fluorinating a polymer is to replace the hydrogen atoms on the polymer surface with fluorine atoms in the case of hydrocarbon polymers, thereby improving the unique performance of the fluorine polymer. That is, it was expected to exhibit water and oil repellency due to a decrease in surface energy, high sliding properties due to a decrease in the coefficient of friction, and further improvements in heat resistance and solvent resistance.

本発明は、ふっ素ガス処理されたVDF系樹脂及びVD
F系樹脂フィルムが、前記の特性に加えて、新たな特性
として、電気的性質である誘電特性に優れた点を見出1
.、新(7い誘′酸材料の製造法と[2て完成(7たも
のである。
The present invention relates to VDF-based resins treated with fluorine gas and VD
In addition to the above-mentioned properties, we discovered that the F-based resin film has a new property: excellent dielectric properties, which are electrical properties.
.. A new method for producing dielectric acid materials and a new method were completed.

すなわち、本発明の要旨は、ぶつ化ビニリデンをモノマ
一単位として関モル係以上有するぶつ化ビニリデン樹脂
を、ふっ素ガスで処理17たのち、フィルム化してなる
高誘電性ふっ素樹脂フィルム、またはぶつ化ビニリデン
をモノマ一単位と〔2て関モル循以上有するぶつ化ビニ
リデン樹脂をフィルム化〔7たのち、ふっ素ガスで処理
1.てなる高誘電性ふっ素樹脂フィルムにある。
That is, the gist of the present invention is to provide a highly dielectric fluororesin film obtained by treating vinylidene butyride resin having a relative molar ratio or higher with vinylidene butthoride as a monomer unit with fluorine gas, or forming a film of vinylidene butyride resin as a monomer unit. A vinylidene butylene resin having one unit of monomer and more than two units of monomer is formed into a film, and then treated with fluorine gas.1. Highly dielectric fluororesin film.

本発明におけるVDF系樹脂のふっ素ガス処理すなわち
直接ふつ素化反応の主たる反応は、次のように示すこと
ができる。
The main reaction of the fluorine gas treatment of the VDF resin in the present invention, that is, the direct fluorination reaction, can be shown as follows.

4− CH2CF t−+−n十F 2−一−十+CX
 2  CF 2+n但し:X=H又はF 上記反応はPVDFについて示したが、他のVDF系m
脂例えば、′vDF−へキサフルオロプロピレン共重合
体、vDF−ぶつ化ビニル供重合体、VDF −) I
Jフルオロエチレン共重合体、VDF−テトラフルオロ
エチレン共重合体、あるいはVDF−炭化水素系モノマ
−′(例えばアクリル酸誘導体モノマー、メタクリル酸
誘導体モノマーなど)などのVDF系共重合体、さらに
VDF系樹脂と他のポリマーとのブレンド物も同様に使
用でき、いずれの場合も本発明の効果を得ることができ
る。
4- CH2CF t-+-n10F 2-1-10+CX
2 CF 2+n However: X=H or F The above reaction was shown for PVDF, but other VDF systems m
For example, 'vDF-hexafluoropropylene copolymer, vDF-butylated vinyl donor polymer, VDF-) I
VDF-based copolymers such as J-fluoroethylene copolymers, VDF-tetrafluoroethylene copolymers, or VDF-hydrocarbon monomers (e.g., acrylic acid derivative monomers, methacrylic acid derivative monomers, etc.), as well as VDF-based resins. Blends of these and other polymers can also be used, and in either case, the effects of the present invention can be obtained.

ふっ素ガス処理を行うVDF系樹脂の物理的形状につい
ては特に制限はないが、好ま(7〈は、粉末、ベレット
、シート、フィルム状の形態が適当でおる。使用するふ
っ素ガスの純度については、とくに制限はない。
There are no particular restrictions on the physical form of the VDF resin to be treated with fluorine gas, but powder, pellet, sheet, and film forms are suitable (7). Regarding the purity of the fluorine gas used, There are no particular restrictions.

VDF系樹脂は、一般に水素−ふっ素の交換反応が炭化
水素系樹脂(例えばポリエチレン、ポリプロピレンなど
)に比[7遅いため、反応の制御には厳密さは要求され
ないが、La−4dar技術(R,J、 Lagow 
et、 al、 ;proc−Natl、、Acad。
The hydrogen-fluorine exchange reaction of VDF resins is generally slower than that of hydrocarbon resins (e.g. polyethylene, polypropylene, etc.), so strict control of the reaction is not required, but La-4dar technology (R, J, Lagow
et, al,;proc-Natl,,Acad.

Sc i、 674 (1970) ;Polym、 
Let t、 Ig−177(1974))を基本とす
る手法、すなわち希釈ふっ素ガスの使用、あるいは反応
温度を制御することによって、よシ再現性に冨んだふつ
素化■P゛系樹脂かえられる。この場合、ふっ素ガスは
ヘリウムあるいはネオンのような不活性ガスで希釈し、
始めは低いふっ素ガス濃度で反応を行ない、時間を経る
につれ濃度を増加させる。反応温度は=80℃からVD
F系樹脂の融点まで任意である。ふっ素化反応方法は、
ふっ素ガス流通方式あるいはぶつ累ガスを反応器中に滞
留させる回分式のどちらでもよい。
Sci, 674 (1970); Polym,
By using a method based on Lett, Ig-177 (1974), that is, by using diluted fluorine gas or by controlling the reaction temperature, fluorinated P resin can be produced with good reproducibility. . In this case, the fluorine gas is diluted with an inert gas such as helium or neon.
Initially, the reaction is carried out at a low fluorine gas concentration, and the concentration is increased over time. Reaction temperature = 80℃ to VD
It is optional up to the melting point of the F-based resin. The fluorination reaction method is
Either a fluorine gas flow system or a batch system in which the accumulated gas is retained in the reactor may be used.

本発明においてVDF系樹脂を完全にふつ素化すること
は好ましくない。完全なふつ素化はむ【7ろ所期の誘電
特性にすぐれた樹脂を現出できず、粉体又はペレットを
完全にふつ素化すると成形性が欠如し、フィルムを完全
にふっ素化すると極端な収縮などの現象が現われて好ま
(−<ない。VDF系樹脂の水−素一ふっ素変換率で示
されるふつ素化率は50係以下、好ま]−くは25%〜
o、iqbが適当である。50係を越えると誘電率の向
上が小さい。
In the present invention, it is not preferable to completely fluorine the VDF resin. Complete fluorination fails to produce a resin with the desired dielectric properties, complete fluorination of powder or pellets results in lack of moldability, and complete fluorination of film results in extreme It is preferable that phenomena such as shrinkage occur (-<no. The fluorination rate indicated by the hydrogen-hydrogen-monofluorine conversion rate of the VDF resin is preferably 50 or less, preferably) - or 25% to
o, iqb are suitable. When the ratio exceeds 50, the improvement in dielectric constant is small.

以上のようなふっ素ガス処理によって得られた粉末、ペ
レット、シートよシ成形されたふつ素化VDF系樹脂フ
ィルムあるいはVDF系樹脂フィルムのふっ素化体は、
ふっ素ガス処理前のものに比較して誘電率が向上(7、
シかもVDF’系樹脂の良溶媒であるジメチルホルムア
ミド、ジメチルアセトアミド、メチルエチルケトンに対
して溶解LK<くなるなど、耐溶剤性の向上が認められ
る。
The fluorinated VDF resin film or the fluorinated VDF resin film formed into powder, pellets, or sheets obtained by the above fluorine gas treatment is as follows:
The dielectric constant is improved compared to that before fluorine gas treatment (7,
Furthermore, improvement in solvent resistance was observed, such as the solubility LK being less than LK for dimethylformamide, dimethylacetamide, and methyl ethyl ketone, which are good solvents for VDF'-based resins.

以下、本発明を実施例に基づいて詳細に説明する。Hereinafter, the present invention will be explained in detail based on examples.

実施例において使用【7たふっ素樹脂のふつ素化ライン
のフローチャートは添付図面のとおシである。図中、1
は捧希釈ふっ素ガスボンベ、2はヘリウムガスボンベ、
3はふっ素ガスボンベ、4,5はガス流量計、6はガス
混合器、7はステンレス製反応器、8,8′は吸収系、
9はストップバルブ、lOは調圧パルプ、11は流量調
節実施例I PVDF粉末試料(ツルペイ社、ンーレフXP −sN
粉末: 150メツシユバスの粒径のもの)を4個のニ
ッケル製ボートにそれぞれ約3yおき、図示のふっ素化
ライン中のステンレス製反応器内7に挿入(7、反応器
内をヘリウムで置換した。次いで30℃において、ヘリ
ウムで杯に希釈17たふっ素ガスを3.4 /g (D
 流量T8時間流し、ふっ素化を開始【また。続いて、
ふっ素ガスを3.0 ’/gの流量で、40時時間流−
1さらにふつ素化を進めた。次いで、反応器内のふっ素
ガスをヘリウムガスで置換したのち、2個のニッケル製
ボート中のふっ素化PVDF各3yを取シ出【7た。重
量増加にょシ求めた上記PVDFのふっ素化率は15.
3%、また元素分析によシ求めたふっ素化率は14.5
%であった。
The flowchart of the fluorination line for the fluororesin used in the Examples is shown in the attached drawings. In the figure, 1
1 is a diluted fluorine gas cylinder, 2 is a helium gas cylinder,
3 is a fluorine gas cylinder, 4 and 5 are gas flow meters, 6 is a gas mixer, 7 is a stainless steel reactor, 8 and 8' are absorption systems,
9 is a stop valve, IO is a pressure regulating pulp, 11 is a flow rate regulation example I PVDF powder sample (Tsurupei Co., Ltd., N-REF XP-sN)
Powder: Particle size of 150 mesh baths) was placed in four nickel boats at intervals of about 3 y each, and inserted into a stainless steel reactor 7 in the fluorination line shown in the figure (7, the inside of the reactor was replaced with helium. Then, at 30°C, 3.4/g (D
Flow rate T8 hours and start fluorination [again. continue,
Fluorine gas was flowed for 40 hours at a flow rate of 3.0'/g.
1. Further basicization was carried out. Next, after replacing the fluorine gas in the reactor with helium gas, each 3y of fluorinated PVDF in the two nickel boats was taken out [7]. The fluorination rate of the above PVDF determined by weight increase is 15.
3%, and the fluorination rate determined by elemental analysis was 14.5.
%Met.

得られたふっ素化PVDF粉末を、加熱プレスを使用し
て温度210℃で電′嚇し、約100μmのフィルムを
作成t7た。さらに、フィルム両面に金を蒸着したのち
、横河ヒューレットバッカード社(YHP)製の427
4 A、 Mu l t i −FrequencyL
CRメーターで、5℃、IKHzにおける比誘電率を測
定(7た。またジメチルホルムアミド(25℃)中に成
形フィルムを浸漬1.て、溶解性を調べた。その結果を
表−1に示す。
The obtained fluorinated PVDF powder was electrolyzed at a temperature of 210° C. using a hot press to form a film of about 100 μm. Furthermore, after gold was vapor-deposited on both sides of the film, 427
4 A, Multi-FrequencyL
Using a CR meter, the dielectric constant at 5°C and IKHz was measured (7).The formed film was also immersed in dimethylformamide (25°C) to examine its solubility.The results are shown in Table 1.

実施例2 実施例1の残り2個のニッケル製ボート中の各3yの試
料について、さらにふつ素化を進めた。実施例1のふっ
素化に加え、へりウムカスで十に希釈1−だふっ素ガス
ヲ、3.57分の流量で2時間、続いてふっ素ガスを3
.0’4の流量で40時間流【またのち、ふつ素化PV
DFをとシ出(7た。重量増加によシ求めたふつ素化素
は18.8%、また元素分析によシ求めたふつ素化率は
167%であった。次に実施例1と同様にして、このふ
つ素化PVDFの比誘電率及び耐溶剤性を測定1.た。
Example 2 Fluorination was further advanced for each 3y sample in the remaining two nickel boats of Example 1. In addition to the fluorination in Example 1, fluorine gas was thoroughly diluted with helium gas for 2 hours at a flow rate of 3.57 minutes, and then fluorine gas was added at a flow rate of 3.57 minutes.
.. Flow rate of 0'4 for 40 hours [Later, fluorinated PV
DF was distilled out (7.0%).The fluorinated element determined by weight increase was 18.8%, and the fluorinated element determined by elemental analysis was 167%.Next, Example 1 In the same manner as in 1., the dielectric constant and solvent resistance of this fluorinated PVDF were measured.

〜ぞの結果を表−1に示す。The results are shown in Table 1.

実施例3 実施例1と同様に試料を反応器に挿入(7、系内をヘリ
ウムで置換後、30℃で4−に希釈(7たふっ素ガスを
a、3m17.の流量でU時間流(またのち、ふつ素化
PVDFをとシ出(−だ。重量増加によシ求めたフッ素
化率は8.5%であった。
Example 3 Insert the sample into the reactor in the same manner as in Example 1 (7) After replacing the system with helium, dilute to 4-4 at 30°C (7). Later, fluorinated PVDF was extracted (-).The fluorination rate determined from the increase in weight was 8.5%.

次に実施例1と同様に(2てフィルムを成形1〜、誘電
率と耐溶剤性を測定(また。その結果を表−1に示す。
Next, in the same manner as in Example 1 (2), the film was molded (1 to 1), and the dielectric constant and solvent resistance were measured (also, the results are shown in Table 1).

実施例4 実施例1と同様に試料を反応器に挿入l〜、系内をヘリ
ウムで置換後、30℃で−Fに希釈lまたふっ素ガスを
3.0’/分の流量で6時間流したのち、ふつ素化PV
DFをとり出した。M量増加によシ求めたふつ素化率は
1.4係であった。
Example 4 A sample was inserted into the reactor in the same manner as in Example 1. After purging the system with helium, the sample was diluted with -F at 30°C and fluorine gas was flowed at a flow rate of 3.0'/min for 6 hours. After that, Futanized PV
I took out my DF. The hydrogenation rate determined by increasing the amount of M was 1.4.

次に実施例1と同様に【7てフィルム成形(7、誘電率
と耐溶剤性を測定した。その結果を表−1に示す。
Next, in the same manner as in Example 1, the film was molded (7) and the dielectric constant and solvent resistance were measured. The results are shown in Table 1.

実施例−5 実施例1と同様に試料を反応器に挿入し、系内をヘリウ
ムで置換し、30℃で十に希釈したふっ素ガスを3.0
 ”/分の流量で2時間流して反応させたのち、ふつ素
化PVDFを取り出した。得られたふつ素化PVDFの
重量増加により求めたふつ素化率は0,4係であった。
Example-5 A sample was inserted into the reactor in the same manner as in Example 1, the inside of the system was replaced with helium, and fluorine gas diluted at 30°C was heated to 3.0°C.
After reacting for 2 hours at a flow rate of 1/min, the fluorinated PVDF was taken out.The fluorinated PVDF obtained had a fluorinated PVDF ratio of 0.4 as determined from the weight increase.

次に、実施例1と同様にフィルム成形して誘電率と耐溶
剤性を測定した。その結果を表−1に示す。
Next, a film was formed in the same manner as in Example 1, and the dielectric constant and solvent resistance were measured. The results are shown in Table-1.

実施例6 500rn1重合器の中にぶつ化ビニリデン60139
ヘキサフルオロプロピレン4.7y、  トリクロルト
リフルオロエタン400m バーフルオロブチリルパー
オキサイド5,4yを仕込み、20℃で調時間重合を行
い、ぶつ化ビニリデンーヘキサフルオログロビレン共重
合体粉末(ぶつ化ビニリデン組成96.3モルqb)を
得た。該共重合体粉末を反応器に挿入し、30℃で十に
希釈したふっ素ガスを3−2./3)の流量で6時間流
したのち、ふつ素化PVDFをとりだした。重量増加に
よシ求めたふつ素化率は2.1係であった。
Example 6 Vinylidene butt 60139 in a 500rn1 polymerization vessel
4.7y of hexafluoropropylene, 400m of trichlorotrifluoroethane, 5.4y of barfluorobutyryl peroxide were charged, polymerization was carried out at 20°C for a set time, and vinylidene butyride-hexafluoroglobylene copolymer powder (vinylidene butylene composition: 96%) was prepared. .3 mol qb) was obtained. The copolymer powder was inserted into a reactor, and fluorine gas diluted at 30°C was heated in 3-2. After flowing at a flow rate of /3) for 6 hours, the fluorinated PVDF was taken out. The hydrogenation rate determined from the increase in weight was 2.1.

次に実施例1と同様にしてフィルム成形し、誘電率と耐
溶剤性を測定した。その結果を表−1に示す。
Next, a film was formed in the same manner as in Example 1, and the dielectric constant and solvent resistance were measured. The results are shown in Table-1.

比較例I PVDF 粉末試料(ツルペイ社、ソーレフXP−8N
粉末、150メツシユパスの粒径)を加熱プレスを用い
て、温度210℃で厚さ約1o。
Comparative Example I PVDF powder sample (Tsurupei Co., Ltd., Solef XP-8N
Powder (particle size of 150 mesh passes) was prepared using a hot press at a temperature of 210° C. to a thickness of about 1.0 mm.

μmのフィルムに作成し、その誘電率および耐溶剤性を
測定した。その結果を表−1に示す。
A micrometer film was prepared, and its dielectric constant and solvent resistance were measured. The results are shown in Table-1.

比較例2 実施例6で得たぶつ化ビニリデン−へキサフルオロプロ
ピレン共重合体粉末を加熱プレスを用いて、温度210
 ℃で厚さ約100μmのフィルムに作成し、その誘電
率および耐溶剤性を測定した。その結果を表−1に示す
Comparative Example 2 The vinylidene butyride-hexafluoropropylene copolymer powder obtained in Example 6 was heated at a temperature of 210°C using a hot press.
A film with a thickness of about 100 μm was prepared at ℃, and its dielectric constant and solvent resistance were measured. The results are shown in Table-1.

実施例7〜11 PVDF(7#ヘイ社、7−L/71010)を4゜鱗
押出機を用いて、温度250℃で肉厚加μmのフィルム
に成形した。このフィルムがう面積25mX 100W
iLの試料を切シ出し銅製の金網上に乗せ、添付図中の
ふっ素化ライン中のステンレス製反応器内に挿入した。
Examples 7 to 11 PVDF (7# Hei Co., Ltd., 7-L/71010) was molded into a film with a wall thickness of μm at a temperature of 250° C. using a 4° scale extruder. This film has an area of 25mX 100W
A sample of iL was cut out, placed on a copper wire mesh, and inserted into a stainless steel reactor in the fluorination line shown in the attached figure.

次に反応系内をヘリウムガスで置換したのち、温度30
℃でヘリウムガスで十に希釈されたふっ素ガスを3.0
m17.の流量で、それぞれ5時間(実施例7)、12
時間(実施例8)、16時間(実施例9)、調時間(実
施例10)、48時間(実施例11)流し、ふつ素化反
応を行なって、それぞれ試料を作成した。各試料のふっ
素化率はESCAを用いてCIFIの測定から求めたF
すのモル比率で表わすと、%= 1.os (実施例7
)、1.20 (実施例8)、1.26 (実施例9)
、1.32 (実施例10)、1.40 (実施例11
)であった。次にそれぞれのフィルムについて、誘電率
と耐溶剤性を測定した。その結果を表−1に示す。
Next, after replacing the inside of the reaction system with helium gas, the temperature was 30
Fluorine gas diluted with helium gas at 3.0 °C
m17. at a flow rate of 5 hours (Example 7) and 12 hours, respectively.
Samples were prepared by carrying out the fluorination reaction for 16 hours (Example 8), 16 hours (Example 9), 48 hours (Example 11), and 48 hours (Example 11). The fluorination rate of each sample was determined from the CIFI measurement using ESCA.
Expressed as a molar ratio of %=1. os (Example 7
), 1.20 (Example 8), 1.26 (Example 9)
, 1.32 (Example 10), 1.40 (Example 11
)Met. Next, the dielectric constant and solvent resistance of each film were measured. The results are shown in Table-1.

実施例12 実施例7〜11と同様にしてPVDFフィルムを反応器
内に挿入し、温度30℃で十に希釈されたふつ素化ガス
を3.o ’/分の流量で2時間流した。次にふっ素ガ
スを4.8”7gの流量で70時間流し、ふっ素化PV
DFフィルムを得た。試料のふつ素化率はESCAを用
いてC+8の測定から求めた%のモル比率で表わすと、
1.75であった。このフィルムについて、誘電率と耐
溶剤性を測定した。その結果を表−1に示す。
Example 12 A PVDF film was inserted into a reactor in the same manner as in Examples 7 to 11, and a sufficiently diluted fluorinated gas was added at a temperature of 30° C. for 3 hours. It was run for 2 hours at a flow rate of o'/min. Next, fluorine gas was passed through 4.8" at a flow rate of 7g for 70 hours, and the fluorinated PV
A DF film was obtained. The hydrogenation rate of the sample is expressed as a molar ratio of % determined from the measurement of C+8 using ESCA.
It was 1.75. The dielectric constant and solvent resistance of this film were measured. The results are shown in Table-1.

実施例13〜14 実施例12と同様にして反応器内温度を一40℃(実施
例13)、80℃(実施例14 )に保って、ふつ素化
を行ない、ふっ素化PVDFフィルムを得た。各試料の
ふつ素化率はES CAを用いてC+8の測定から求め
たす。のモル比率で表わすと、1.24 (実施例13
)、1.62 (実施例14)であった。次にそれぞれ
のフィルムについて誘電率と耐溶剤性を測定した。その
結果を表−1に示す。
Examples 13 to 14 Fluorination was carried out in the same manner as in Example 12 while maintaining the temperature inside the reactor at -40°C (Example 13) and 80°C (Example 14) to obtain a fluorinated PVDF film. . The hydrogenation rate of each sample was determined from the measurement of C+8 using ES CA. When expressed as a molar ratio of 1.24 (Example 13
), 1.62 (Example 14). Next, the dielectric constant and solvent resistance of each film were measured. The results are shown in Table-1.

比較例3 実施例7〜11において、ふっ素ガス処理前のPVDF
フィルムの誘電率と耐溶剤性を測定した。その結果を表
−1に示す。
Comparative Example 3 In Examples 7 to 11, PVDF before fluorine gas treatment
The dielectric constant and solvent resistance of the film were measured. The results are shown in Table-1.

表  −1Table-1

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

図面は、本発明の高誘電性ふっ素樹脂フィルムを得るた
めに、ぶつ化ビニリデン系樹脂を直接ふつ素化するため
の装置の1例を示すフローチャートである。 1・・・・・・十希釈ふっ素ガスボンベ、2・・・・・
・ヘリウムガスボンベ、 3・・・・・・ふっ素ガスボンベ、 6・・・・・・ガス混合器、 7・・・・・・ステンレス製反応器。
The drawing is a flowchart showing an example of an apparatus for directly fluorinating vinylidene butylene resin in order to obtain the highly dielectric fluororesin film of the present invention. 1...10 diluted fluorine gas cylinder, 2...
・Helium gas cylinder, 3... Fluorine gas cylinder, 6... Gas mixer, 7... Stainless steel reactor.

Claims (3)

【特許請求の範囲】[Claims] (1)  ふう化ビニリデンをモノマ一単位として(資
)モルチ以上有するぶつ化ビニリデン系樹脂を原料とし
、これにふっ素ガス処理とフィルム化処理を施(−てな
る高誘電性ふっ素樹脂フィルム。
(1) A highly dielectric fluororesin film made by using a vinylidene fluoride resin containing vinylidene fluoride as a monomer unit or more as a raw material, and subjecting it to fluorine gas treatment and film-forming treatment.
(2)  ぶつ化ビニリデン系樹脂をふっ素ガスで処理
したのち、フィルム化【2てなる特許請求の範囲第(1
)項に記載の高誘電性ふっ素樹脂フィルム。
(2) After treating the vinylidene fluoride resin with fluorine gas, it is formed into a film [Claim No. 1 consisting of (2)
) Highly dielectric fluororesin film described in item 1.
(3)ぶつ化ビニリデン系樹脂をフィルム化【7たのち
、ぶつ化ガスで処理してなる特許請求の範囲第(11項
に記載の高誘電性ふっ素樹脂フィルム。
(3) A highly dielectric fluororesin film according to claim 11, which is obtained by forming a vinylidene fluoride resin into a film and then treating it with a fluorine gas.
JP6195583A 1983-04-08 1983-04-08 Highly dielectric fluororesin film Pending JPS59187006A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6195583A JPS59187006A (en) 1983-04-08 1983-04-08 Highly dielectric fluororesin film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6195583A JPS59187006A (en) 1983-04-08 1983-04-08 Highly dielectric fluororesin film

Publications (1)

Publication Number Publication Date
JPS59187006A true JPS59187006A (en) 1984-10-24

Family

ID=13186117

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6195583A Pending JPS59187006A (en) 1983-04-08 1983-04-08 Highly dielectric fluororesin film

Country Status (1)

Country Link
JP (1) JPS59187006A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4650833A (en) * 1984-03-07 1987-03-17 Kureha Chemical Industry Co. Thin transparent polytetrafluoroethylene film and production process thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4650833A (en) * 1984-03-07 1987-03-17 Kureha Chemical Industry Co. Thin transparent polytetrafluoroethylene film and production process thereof

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