JPS6325602B2 - - Google Patents
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- JPS6325602B2 JPS6325602B2 JP2634983A JP2634983A JPS6325602B2 JP S6325602 B2 JPS6325602 B2 JP S6325602B2 JP 2634983 A JP2634983 A JP 2634983A JP 2634983 A JP2634983 A JP 2634983A JP S6325602 B2 JPS6325602 B2 JP S6325602B2
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- Japan
- Prior art keywords
- fluorine
- film
- containing polymer
- nitrogen oxides
- nitrogen
- Prior art date
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Description
本発明はスルホニル基を有する含弗素高分子体
からなるカルボキシル基を有する含弗素高分子体
の新規な製造方法に関し、詳しくは含弗素高分子
体が有するスルホニル基を効率よくカルボキシル
基に変換する簡便な方法を提供するものである。
従来、含弗素高分子体のスルホニル基をカルボ
キシル基に変換する方法については多くの提案が
ある。例えば、本発明者等が提案したスルホニル
基(スルホン酸基)をスルホニルハライド基とし
た後、有機溶媒の存在下に酸化処理する方法(特
開昭53−132069、54−83982)、フエノール類と反
応させる方法(特開昭54−20981)、アミン類と反
応させる方法(特開昭54−21478)があり、また
その他では沃化水素酸等の還元剤で処理する方法
(特開昭52−24177)等がある。しかしながら、こ
れら提案された殆んどの方法は、工程が多段階よ
りなるため、設備的な面を含めて経済的な不利が
免れなかつた。本発明者等は上記の不利を解消す
る方法を既に提案している(特願昭56−131646)。
即ち、スルホニル基を有する含弗素高分子体に窒
素酸化物存在下に紫外線を照射する方法である。
この方法では短時間に効率よくカルボキシル基を
生成させることができ、工程の大巾な短縮が従来
の方法に較べて可能になつた。しかしながら、腐
食性が強く、また有害である窒素酸化物を使用し
ているために照射室の材料の選定、窒素酸化物の
漏洩を防ぐための照射室の構造など設備的な面で
若干の改良が必要であつた。
したがつて、本発明者はさらに上記の不利を改
良すべく研究を重ねたところ、スルホニル基を有
する含弗素高分子体が窒素酸化物を安定によく吸
着することを見出し、本発明を完成させるに至つ
た。本発明によればスルホニル基を有する含弗素
高分子体に窒素酸化物を吸着させた後、窒素酸化
物の不存在下に紫外線を照射することを特徴とす
るカルボキシル基を有する含弗素高分子体の製造
方法が提供される。
即ち、本発明においてはスルホニル基を有する
含弗素高分子体を適当な吸着装置内に入れ、適当
な条件下で窒素酸化物を含弗素高分子体に吸着さ
せる。吸着装置内を無毒性のガスで置換して窒素
酸化物を除去した後、窒素酸化物を吸着した含弗
素高分子体が取出される。その後、紫外線の照射
装置において窒素酸化物を吸着した含弗素高分子
体に紫外線を照射することにより、カルボキシル
基を有する含弗素高分子体を簡便に得ることが出
来る。
本発明では、窒素酸化物を吸着させた後に紫外
線照射を行うために、窒素酸化物を有効利用する
ことができ公害物質の使用量の低減ができるこ
と、紫外スペクトル及び赤外スペクトルによれ
ば、窒素酸化物が少なくともNO+として固定さ
れ(吸着され)ていることも確認され、この状態
で紫外線を照射することが可能になつたため、照
射装置の材料の問題が解消され、また装置の構造
が大巾に簡略化されたこと、さらに簡単な装置で
連続的にカルボキシル基を有する含弗素高分子体
の製造が可能になつたことなど工業的メリツトは
大きい。
本発明で用いるスルホニル基を有する含弗素高
分子体としては、特にパーフルオロカーボン系高
分子が好ましく、例えばパーフルオロサルトン
The present invention relates to a new method for producing a fluorine-containing polymer having a carboxyl group, which is made of a fluorine-containing polymer having a sulfonyl group, and more specifically, a simple method for efficiently converting the sulfonyl group of the fluorine-containing polymer into a carboxyl group. This method provides a method. Conventionally, there have been many proposals regarding methods for converting sulfonyl groups in fluorine-containing polymers into carboxyl groups. For example, a method proposed by the present inventors in which a sulfonyl group (sulfonic acid group) is converted into a sulfonyl halide group and then oxidized in the presence of an organic solvent (JP-A-53-132069, 54-83982), There is a method of reaction (Japanese Patent Laid-Open No. 54-20981), a method of reaction with amines (Japanese Patent Laid-Open No. 54-21478), and another method is a method of treatment with a reducing agent such as hydriodic acid (Japanese Patent Laid-Open No. 52-1999). 24177) etc. However, since most of these proposed methods involve multiple steps, they are inevitably disadvantageous economically, including in terms of equipment. The present inventors have already proposed a method to eliminate the above-mentioned disadvantages (Japanese Patent Application No. 131,646/1982).
That is, this is a method in which a fluorine-containing polymer having a sulfonyl group is irradiated with ultraviolet rays in the presence of nitrogen oxides.
This method allows carboxyl groups to be produced efficiently in a short period of time, making it possible to significantly shorten the number of steps compared to conventional methods. However, since highly corrosive and harmful nitrogen oxides are used, some improvements have to be made in terms of equipment, such as the selection of materials for the irradiation chamber and the structure of the irradiation chamber to prevent leakage of nitrogen oxides. was necessary. Therefore, the present inventor conducted further research to improve the above-mentioned disadvantages, and found that a fluorine-containing polymer having a sulfonyl group can stably and well adsorb nitrogen oxides, thereby completing the present invention. It came to this. According to the present invention, a fluorine-containing polymer having a carboxyl group is characterized by adsorbing nitrogen oxides onto the fluorine-containing polymer having a sulfonyl group, and then irradiating the same with ultraviolet rays in the absence of nitrogen oxides. A manufacturing method is provided. That is, in the present invention, a fluorine-containing polymer having a sulfonyl group is placed in a suitable adsorption device, and nitrogen oxides are adsorbed onto the fluorine-containing polymer under appropriate conditions. After purging the inside of the adsorption device with a non-toxic gas to remove nitrogen oxides, the fluorine-containing polymer adsorbing nitrogen oxides is taken out. Thereafter, the fluorine-containing polymer having adsorbed nitrogen oxides is irradiated with ultraviolet rays using an ultraviolet irradiation device, thereby easily obtaining a fluorine-containing polymer having carboxyl groups. In the present invention, since ultraviolet irradiation is performed after nitrogen oxides are adsorbed, nitrogen oxides can be effectively used and the amount of pollutants used can be reduced.According to ultraviolet and infrared spectra, nitrogen It was also confirmed that oxides were fixed (adsorbed) as at least NO It has great industrial merits, such as being greatly simplified and making it possible to continuously produce a fluorine-containing polymer having carboxyl groups using a simple device. The fluorine-containing polymer having a sulfonyl group used in the present invention is particularly preferably a perfluorocarbon polymer, such as perfluorosultone.
【式】を開環後、ヘキサフルオロプロ
ピレンオキサイドとのオリゴメリゼーシヨンから
得られるスルホニルフルオライド基を有するビニ
ルモノマー
又は[Formula] Vinyl monomer with sulfonyl fluoride group obtained from oligomerization with hexafluoropropylene oxide after ring opening or
【式】(上式でY
はフツ素トリフルオロメチル基またはパーフルオ
ロアルキル基;m及びnは0乃至5の整数)の重
合体または他の含弗素ビニルモノマー例えばフツ
化ビニリデン、テトラフルオロエチレン、トリフ
ルオロエチレン、クロルトリフルオロエチレン、
ヘキサフルオロプロピレン等との共重合体などで
ある。その他、含弗素高分子体に後処理により、
スルホニル基を導入したものも用いることができ
る。
本発明で言うスルホニル基とは、一般に−
CF2SO2Xで示されるもので、例えばスルホン酸
基(X=OH)及びスルホン酸基のアンモニウム
塩(X=ONH4)、スルフイン酸基(X=H)及
びスルフイン酸基のアンモニウム塩(X=
ONH4)である。特にこれ等のスルホニル基のう
ち好適に用いられるものは、入手が簡単なことか
らスルホン酸基及びそのアンモニウム塩である。
これらのスルホニル基を有する含弗素高分子体
の代表的な製造例は、含弗素ビニルモノマーとス
ルホニルフルオライド基を有するビニルモノマー
との混合物(組成は含弗素高分子体中のスルホニ
ル基の含量により調節する)を公知の重合法、即
ち、開始剤の存在下に重合温度室温〜200℃、圧
力は1〜250Kg/cm2で溶液、乳化あるいは懸濁重
合法で重合し、かくして得られた粉状の高分子体
を適当に例えば粒状、または膜状に成型後に用い
られる。さらに、場合によつては成型膜状物に補
強物質(網など)を裏打ちして機械的強度を増大
したものも好適に用いられる。
本発明の方法で得られるカルボキシル基を有す
る含弗素高分子体を電解用イオン交換膜として用
いる場合、本発明の処理を行う前の含弗素高分子
体中のスルホニル基の含量は0.2〜2.5ミリ当量/
グラム樹脂であることがその電気化学的な面から
好適である。
なお、上記で得られる含弗素高分子体が有する
−SO2Fは、下記の反応に従つて前記した如き所
望のスルホニル基に変換することが出来る。
(1) スルホン酸基またはその塩
(2) スルフイン酸基またはその塩
スルホニル基を有する含弗素高分子体に吸着さ
せる窒素酸化物としては例えばNO2(又はN2O4)、
N2O3、N2O5、NOとNO2の混合物、またはこれ
等のガスを適当に混合したものが好適に用いられ
る。その他、吸着時の条件によつては上記した窒
素酸化物を発生させることのできるような化合物
も用いられる。例えば硝酸、亜硝酸類及びその塩
類等である。これらのうち入手が容易なこと、取
扱いが簡単なことなどからNO2(またはN2O4)、
N2O3またはNOとNO2の混合物のガス状の窒素
酸化物が好ましい。
これ等の窒素酸化物をスルホニル基を有する含
弗素高分子体に吸着させる方法は特に限定的でな
く、通常用いられている多くの公知の方法を適用
することができる。例えば、粒状の含弗素高分子
体の場合は円筒状容器内に充填し、その容器内に
窒素酸化物をそのまま、または適当な不活性ガス
(例えば窒素、ヘリウム、アルゴン等)で希釈下
にバツチ式または連続的に導入してやれば吸着が
行われる。また場合によつては、特に多量に吸着
させたい時は加圧下で行つてもよい。膜状物の場
合は謂ゆるフイルタープレス型の吸着装置に型枠
と膜状物を交互にはさみ、型枠に取付けられたノ
ズルから窒素酸化物または他の不活性ガスで希釈
したものを導入することで吸着させることができ
る。また別の方法では何枚もの膜状物を一度に平
行にカーテン状に取付けた支持体を吸着容器内に
入れ、一度に何枚もの膜状物に吸着させることが
可能である。
含弗素高分子体に対する窒素酸化物の吸着量
は、本発明で得られる含弗素高分子体の使用目的
により一概に言えないが、窒素酸化物の分圧、温
度により調節することができ、一般に用いる含弗
素高分子体のスルホニル基の量(ミリ当量/グラ
ム)の0.01以上、好ましくは0.1以上あれば本発
明は達成される。このような含弗素高分子体に吸
着した窒素酸化物の量は、吸着前後の窒素酸化物
の分圧変化から求めることができるし、また吸着
後の含弗素高分子体を苛性ソーダ等のアルカリを
含む水で吸着した窒素酸化物を逆抽出し、抽出さ
れた窒素酸化物の量を常法に従い定量することに
よつても吸着量を求めることができる。
次に窒素酸化物を吸着した含弗素高分子体は紫
外線を照射される。照射方法は通常光化学反応系
で通常用いられる方法が好適に使用される。一般
に光源は1800〜4000Å程度(勿論この範囲より高
エネルギー側の紫外線も有効であるが)の紫外線
を放射する例えば水銀ランプ等公知の紫外線源を
用いることができる。このランプからの紫外線が
窒素酸化物を吸着した含弗素高分子体に均等に照
射できるように工夫して、かつ温度調節できる反
応器であれば本発明は十分に達成される。紫外線
の照射雰囲気は減圧下であつても窒素、ヘリウ
ム、アルゴン等の不活性ガス存在下、又は加圧下
であつてもよい。
スルホニル基を有する含弗素高分子体が粒状で
あれば振動、撹拌等の手段を用いて流動下で紫外
線の照射を行うことが望ましい。また、膜状の含
弗素高分子体の場合には、紫外線源との位置を固
定し、ある一定強度の紫外線をバツチ式に照射し
てもよい。さらに紫外線源に対して含弗素高分子
体が大きい場合、とくに膜状物にあつては紫外線
源に対して該膜状物を連続的に又は断続的に移動
させつつ照射してもよい。
かくして、本発明の方法によれば、スルホニル
基からカルボキシル基への変化が早く連続的に処
理を行うことが工業的に有利である。なお照射す
る紫外線量および照射時間は、本発明の処理で得
られる含弗素高分子体の使用目的により、用いる
含弗素高分子体の種類、窒素酸化物の吸着量、反
応温度、反応装置の形状等により一概には決定で
きない。一般的に紫外線量および照射時間が大き
過ぎたり、長過ぎたりするとスルホニル基部分の
脱離反応が優先的に起つたりして、好ましくない
結果を与える時がある。このため、紫外線量およ
び照射時間は、本発明の処理で得られる含弗素高
分子体の使用目的に応じて、予め実験を行い決定
することが望ましい。一般に数mW/cm2の線量で
照射時間は数分〜数時間程度で充分に本発明は達
成される。
本発明の方法において紫外線を照射してスルホ
ニル基を有する含弗素高分子体を処理する温度
は、一般に室温から250℃の温度範囲が好ましい。
勿論この範囲外であつても、例えば10℃付近でも
反応は徐々にではあるが進行し、また250℃の温
度以上であつてもカルボキシル基の生成は場合に
よつては充分に認められるが、他の副反応、例え
ばカルボキシル基の一部脱離、特に含弗素高分子
体の場合には変形、強度の劣化などの物理的な面
での欠点が認められるようになるため好ましくな
い。
本発明の方法により処理して得られる含弗素高
分子体は赤外スペクトル(該高分子体が粒状であ
ればKBr法、膜状であればATR法または透過法)
で測定することによつて、処理前には認められな
かつた1780cm-1に新しい吸収帯が生じ、アルカリ
処理を行なうと1680cm-1にシフトすることからパ
ーフルオロアルキル基に連結したカルボキシル基
に起因することが認められ、また処理条件によつ
ては1610cm-1にパーフルオロニトロ基に起因する
と推測される吸収帯が認められる。一方、処理前
に1060cm-1に強く認められるスルホン酸基の吸収
帯(スルホニル基がスルホン酸基である時)は一
般に処理条件を強くすると殆んど消失し、スルホ
ン酸基が殆んど反応してしまう。また処理条件を
弱めるとスルホン酸基は、大部分が残存し少量の
カルボキシル基の生成が認められる。したがつて
本発明は処理条件によりスルホン酸基の中に少量
のカルボキシル基を含む状態から、スルホン酸基
は殆んどなくカルボキシル基のみ存在する状態の
ものまで任意につくることができる。
本発明はスルホニル基をカルボキシル基に一工
程で効率良く変化する有利な方法であるが、さら
に粒状または膜状の含弗素高分子体の表層部に均
一な厚みでカルボキシル基が存在する薄層を形成
できる特徴と有する。このような薄層の判別方法
は、染色により容易にできる。例えば、本発明の
処理を行つた含弗素高分子体をアルコール等の膨
潤性溶媒を含むクリスタルバイオレツトの酸性水
溶液中で染色し、その断面の薄片を切出し、顕微
鏡で観察することによつてカルボキシル基が存在
する層を確認することができる。
さらにまた、本発明の方法は気相下で紫外線の
光を用いた反応であるために、既に述べた粒状、
糸状、膜状以外に袋状のものにも好適に処理でき
る。例えば予め窒素酸化物を吸着した筒状物の中
心部または筒の内表面に紫外線が均等に照射でき
るように紫外線源を配置し、本発明の処理を行え
ば袋状のものにも本発明を適応することができ
る。
本発明の処理で得られるカルボキシル基を有す
る含弗素高分子体は従来公知である用途に制限な
く用いることができる。例えば、カルボキシル基
を有する高分子体が粒状であれば触媒、PHコント
ローラー、特殊イオン交換樹脂等に有用である。
特に膜状物にあつては、近年盛んに研究されてい
る食塩電解用のイオン交換膜として極めて高性能
なものが本発明で得られる。即ち、食塩電解用の
イオン交換膜の好ましい態様として、片面にスル
ホン酸および他面にカルボキシル基を有するもの
が提案されているが、本発明はスルホン酸基を有
する含弗素高分子体の表面に数μ〜数十μのカル
ボキシル基を有する薄層をコントロールよく生成
することが容易であるため、比較的高抵抗の層で
あるカルボキシル基が存在する層を極めて薄くす
ることができ、従来法にくらべ飛躍的に電解用膜
を、一工程で効率良く、しかも簡単な装置でつく
ることができる。さらに本発明で得られる膜状物
は最近盛んに研究が続けられている省エネルギー
化への工夫、例えばS、P、E(Solid Polymer
Electrolyte)化する方法、またカルボキシル基
が存在する面を白金等でコーテイングする方法、
気泡の付着を防止するために膜状物の表面を粗面
化する方法、無機粉体を膜状物の表面に付着させ
る方法などにも適用できる。
以下、本発明を具体的に説明するため実施例を
示すが、本発明はこれ等に限定されるものではな
い。
実施例 1
テトラフルオロエチレンとパーフルオロ(3,
6−ジオキサ−4−メチル−7−オクテンスルホ
ニルフルオライド)の共重合体で、該スルホニル
フルオライド基を加水分解してスルホン酸基とし
た時の交換容量が0.91(ミリグラム当量/グラム
乾燥樹脂)である厚さ0.18mmの透明フイルムを
1N−HCl中に浸漬して、スルホン酸基をH+型と
した。
他方、円筒の上部・下部に2つのノズルを有し
内径8cmのガラス円筒の中心部に殺菌ランプGL
−15(東芝製)を装着した反応器の内周に紫外線
が表面に均一にあたるように上記したH+型のフ
イルムを15cm×20cm取付けた。この反応器をオイ
ルバス中に浸漬し、ノズルより窒素を50c.c./mの
流速で導入しながら160℃まで昇温した。昇温後、
窒素の導入を止め、ノズルに真空ポンプをつない
でさらに一時間減圧乾燥を行つた。乾燥後、反応
容器を−76cmHgまで減圧とした。ノズルより酸
化窒素(NO)及び二酸化窒素(NO2)をそれぞ
れ5cmHgずつ、さらに窒素を大気圧になるよう
に導入した。この状態で45分放置し、上記フイル
ムに窒素酸化物を吸着させた。反応器内の圧力の
低下は3cmHgであつた。その後、反応器内に窒
素を導入して反応器内を洗浄した。洗浄を完全に
するため反応器内で真空ポンプで脱気した。再
度、反応器内に窒素を大気圧まで導入した。殺菌
ランプを点灯し、照射を開始した。1時間の照射
後ランプを消し、反応器内に窒素を導入して洗浄
した。
フイルムを取り出し、その一部を切り取り赤外
スペクトル測定(ATR法)に供した。残りの部
分は20%にNaOHを含むメタノール−水(容量
比1/1)中で30分間加温し、イオン交換基を
Na+型とした後、染色テスト及び電解テスト等に
供した。その結果、照射面の赤色スペクトルで
は、1780cm-1にカルボキシル基を起因する吸収帯
が中位の強度が認められ、また、1610cm-1にも弱
いながら新しい吸収帯が認められた。一方、未照
射面に認められる1060cm-1のスルホン酸基の吸収
帯は殆んど認められなかつた。Na+型としたフイ
ルムの一部(5mm×10mm位)を、クリスタルバイ
オレツト100mgを、0.5N−HCl−メタノール(容
量比3:7)の混合溶媒100c.c.中に溶かした染色
液中に室温下で15hrs浸漬した。水洗後、ミクロ
トームで断面を薄片状に切取り顕微鏡で観察した
ところ、一方の表面より15μが層状に全く染色さ
れず、他の部分が濃緑色に染つていたことより、
表面より15μの厚みでカルボキシル基が存在して
いることが判つた。
表−1に紫外線処理後のフイルム及び未処理の
フイルムについて、電解テストの測定結果を示
す。電解テストはチタン製の陽極室とニツケル製
の陰極室よりなる2室式で0.5dm2の有効通電面積
をもつセルを用いて行つた。陽極としてチタンの
ラス材に酸化チタンと酸化ルテニウムを被覆した
もの、陰極として軟鉄のラス材を用いた。陽極室
と陰極室の間にフイルムを陽極とは密着し、陰極
と2mmの間隙で組込み(紫外線を照射したものは
照射面を陰極に向けて)、陽極室にCa濃度が
0.5ppm以下の飽和食塩水を供給し、3.5Nの食塩
濃度で排出した。一方、陰極室にNaOHの濃度
が11Nとなるように純水を供給した。電流密度
30A/dm2、極室温度90℃に調節した。[Formula] (in the above formula, Y is a fluorine trifluoromethyl group or a perfluoroalkyl group; m and n are integers of 0 to 5) or other fluorine-containing vinyl monomers such as vinylidene fluoride, tetrafluoroethylene, trifluoroethylene, chlorotrifluoroethylene,
These include copolymers with hexafluoropropylene and the like. In addition, through post-treatment of fluorine-containing polymers,
Those into which a sulfonyl group has been introduced can also be used. The sulfonyl group referred to in the present invention generally refers to -
CF 2 SO 2 X=
ONH 4 ). Particularly preferred among these sulfonyl groups are sulfonic acid groups and their ammonium salts because they are easily available. A typical production example of a fluorine-containing polymer having these sulfonyl groups is a mixture of a fluorine-containing vinyl monomer and a vinyl monomer having a sulfonyl fluoride group (the composition depends on the content of sulfonyl groups in the fluorine-containing polymer). The powder thus obtained is polymerized by a known polymerization method, that is, in the presence of an initiator, at a polymerization temperature of room temperature to 200°C and a pressure of 1 to 250 Kg/cm 2 by solution, emulsion or suspension polymerization. The polymer is used after being appropriately formed into, for example, granules or a film. Furthermore, in some cases, a molded membrane material may be preferably lined with a reinforcing material (such as a net) to increase its mechanical strength. When the fluorine-containing polymer having carboxyl groups obtained by the method of the present invention is used as an ion exchange membrane for electrolysis, the content of sulfonyl groups in the fluorine-containing polymer before the treatment of the present invention is 0.2 to 2.5 mm. Equivalent weight/
Gram resin is preferred from its electrochemical standpoint. Incidentally, -SO 2 F contained in the fluorine-containing polymer obtained above can be converted into a desired sulfonyl group as described above according to the following reaction. (1) Sulfonic acid group or its salt (2) Sulfinic acid group or its salt Examples of nitrogen oxides to be adsorbed onto a fluorine-containing polymer having a sulfonyl group include NO 2 (or N 2 O 4 ),
N 2 O 3 , N 2 O 5 , a mixture of NO and NO 2 , or a suitable mixture of these gases are preferably used. In addition, depending on the conditions during adsorption, compounds that can generate the above-mentioned nitrogen oxides may also be used. For example, nitric acid, nitrites and their salts. Among these, NO 2 (or N 2 O 4 ) is used because it is easily available and easy to handle.
Gaseous nitrogen oxides of N 2 O 3 or a mixture of NO and NO 2 are preferred. The method for adsorbing these nitrogen oxides onto a fluorine-containing polymer having a sulfonyl group is not particularly limited, and many commonly used known methods can be applied. For example, in the case of a granular fluorine-containing polymer, it is packed in a cylindrical container, and the nitrogen oxide is placed in the container either as is or in batches diluted with an appropriate inert gas (e.g. nitrogen, helium, argon, etc.). Adsorption takes place if introduced in a continuous manner or continuously. In some cases, when a particularly large amount of adsorption is desired, the adsorption may be carried out under pressure. In the case of a film-like material, the formwork and the film-like material are alternately sandwiched between a so-called filter press type adsorption device, and nitrogen oxide or another inert gas diluted with nitrogen oxide or other inert gas is introduced through a nozzle attached to the formwork. This allows it to be absorbed. In another method, it is possible to place a support on which a number of membrane-like materials are attached in parallel in a curtain-like manner into an adsorption container, and to cause the support to be adsorbed onto a number of membrane-like materials at once. Although the adsorption amount of nitrogen oxides on the fluorine-containing polymer cannot be definitively determined depending on the purpose of use of the fluorine-containing polymer obtained by the present invention, it can be adjusted by adjusting the partial pressure of nitrogen oxides and the temperature. The present invention can be achieved if the amount of sulfonyl groups (milliequivalents/gram) in the fluorine-containing polymer used is 0.01 or more, preferably 0.1 or more. The amount of nitrogen oxides adsorbed on such a fluorine-containing polymer can be determined from the change in partial pressure of nitrogen oxides before and after adsorption. The amount of adsorption can also be determined by back-extracting the nitrogen oxides adsorbed by the water contained and quantifying the amount of extracted nitrogen oxides according to a conventional method. Next, the fluorine-containing polymer that has adsorbed nitrogen oxides is irradiated with ultraviolet light. As the irradiation method, a method commonly used in photochemical reaction systems is preferably used. In general, a known ultraviolet source such as a mercury lamp that emits ultraviolet rays of about 1800 to 4000 angstroms (although of course ultraviolet rays on the higher energy side than this range is also effective) can be used. The present invention can be fully achieved if the reactor is designed to uniformly irradiate the fluorine-containing polymer adsorbed with nitrogen oxides with the ultraviolet rays from the lamp and whose temperature can be controlled. The ultraviolet irradiation atmosphere may be under reduced pressure, in the presence of an inert gas such as nitrogen, helium, or argon, or under increased pressure. If the fluorine-containing polymer having a sulfonyl group is in the form of particles, it is preferable to irradiate it with ultraviolet rays under flowing conditions using means such as vibration or stirring. Further, in the case of a film-like fluorine-containing polymer, the position with the ultraviolet source may be fixed and ultraviolet rays of a certain intensity may be irradiated in batches. Further, when the fluorine-containing polymer is large relative to the ultraviolet light source, especially in the case of a film-like material, the film-like material may be irradiated with the ultraviolet light source while being moved continuously or intermittently. Thus, according to the method of the present invention, it is industrially advantageous that the conversion from sulfonyl groups to carboxyl groups is rapid and that the process is carried out continuously. The amount of ultraviolet rays to be irradiated and the irradiation time depend on the purpose of use of the fluorine-containing polymer obtained by the treatment of the present invention, the type of fluorine-containing polymer used, the amount of nitrogen oxide adsorption, the reaction temperature, and the shape of the reaction apparatus. etc., it cannot be determined unambiguously. Generally, if the amount of ultraviolet rays and the irradiation time are too large or too long, the elimination reaction of the sulfonyl group may occur preferentially, giving undesirable results. Therefore, it is desirable to determine the amount of ultraviolet rays and the irradiation time in advance through experiments, depending on the intended use of the fluorine-containing polymer obtained by the treatment of the present invention. Generally, the present invention can be sufficiently achieved with a dose of several mW/cm 2 and an irradiation time of several minutes to several hours. In the method of the present invention, the temperature at which the fluorine-containing polymer having a sulfonyl group is treated by irradiating ultraviolet light is generally preferably in the range of room temperature to 250°C.
Of course, even outside this range, for example around 10°C, the reaction proceeds, albeit slowly, and even at temperatures above 250°C, the formation of carboxyl groups can be observed in some cases. Other side reactions, such as partial elimination of carboxyl groups, especially in the case of fluorine-containing polymers, are not preferred because physical defects such as deformation and deterioration of strength are observed. The fluorine-containing polymer obtained by processing according to the method of the present invention has an infrared spectrum (KBr method if the polymer is granular, ATR method or transmission method if the polymer is film-like)
As a result of measurement, a new absorption band appears at 1780 cm -1 that was not observed before treatment, and it shifts to 1680 cm -1 after alkali treatment, indicating that it is caused by the carboxyl group linked to the perfluoroalkyl group. In addition, depending on the processing conditions, an absorption band at 1610 cm -1 that is assumed to be caused by perfluoronitro groups is observed. On the other hand, the absorption band of sulfonic acid groups that is strongly observed at 1060 cm -1 before treatment (when the sulfonyl group is a sulfonic acid group) generally disappears when the treatment conditions are strengthened, and most of the sulfonic acid groups are not reacted. Resulting in. Furthermore, when the treatment conditions are weakened, most of the sulfonic acid groups remain and a small amount of carboxyl groups are observed to be produced. Accordingly, in the present invention, depending on the processing conditions, it is possible to arbitrarily produce a product ranging from a state containing a small amount of carboxyl group in the sulfonic acid group to a state in which there are almost no sulfonic acid groups and only carboxyl groups are present. The present invention is an advantageous method for efficiently converting a sulfonyl group into a carboxyl group in one step, but it also forms a thin layer in which carboxyl groups exist with a uniform thickness on the surface layer of a granular or film-like fluorine-containing polymer. Has features that can be configured. Such thin layers can be easily distinguished by staining. For example, a fluorine-containing polymer treated according to the present invention is dyed in an acidic aqueous solution of crystal violet containing a swelling solvent such as alcohol, a thin section of the cross section is cut, and the carboxyl polymer is observed under a microscope. The layer in which the group is present can be confirmed. Furthermore, since the method of the present invention is a reaction using ultraviolet light in a gas phase, the above-mentioned granular,
In addition to thread-like and film-like forms, bag-like forms can also be suitably processed. For example, by arranging an ultraviolet ray source so that ultraviolet rays can be uniformly irradiated onto the center of a cylindrical object or the inner surface of the cylindrical object that has previously adsorbed nitrogen oxides, and applying the treatment according to the present invention, the present invention can be applied to bag-like objects as well. Able to adapt. The fluorine-containing polymer having a carboxyl group obtained by the treatment of the present invention can be used in conventionally known applications without any limitations. For example, if a polymer having carboxyl groups is in the form of particles, it is useful for catalysts, PH controllers, special ion exchange resins, and the like.
In particular, in the case of membrane-like materials, the present invention provides extremely high-performance ion exchange membranes for salt electrolysis, which have been actively researched in recent years. That is, as a preferred embodiment of an ion exchange membrane for salt electrolysis, one having a sulfonic acid group on one side and a carboxyl group on the other side has been proposed. It is easy to control thin layers with carboxyl groups of several microns to several tens of microns, so it is possible to make the layer containing carboxyl groups, which is a relatively high resistance layer, extremely thin, making it possible to Electrolytic membranes can be produced dramatically more efficiently in one process and with simple equipment. Furthermore, the film-like material obtained by the present invention can be applied to energy-saving devices that have been actively researched recently, such as S, P, and E (Solid Polymer).
Electrolyte) method, or coating the surface where carboxyl groups are present with platinum etc.
It can also be applied to a method of roughening the surface of a film-like object to prevent the adhesion of air bubbles, a method of attaching inorganic powder to the surface of a film-like object, and the like. Examples are shown below to specifically explain the present invention, but the present invention is not limited thereto. Example 1 Tetrafluoroethylene and perfluoro(3,
A copolymer of 6-dioxa-4-methyl-7-octensulfonyl fluoride), which has an exchange capacity of 0.91 (milligram equivalent/gram dry resin) when the sulfonyl fluoride group is hydrolyzed to form a sulfonic acid group. A transparent film with a thickness of 0.18mm is
The sulfonic acid groups were converted to H + form by immersion in 1N HCl. On the other hand, a germicidal lamp GL is placed in the center of a glass cylinder with an inner diameter of 8 cm and has two nozzles at the top and bottom of the cylinder.
-15 (manufactured by Toshiba) was attached to the inner periphery of the reactor so that the surface was uniformly exposed to ultraviolet rays, and the above-mentioned H + type film was attached at 15 cm x 20 cm. This reactor was immersed in an oil bath, and the temperature was raised to 160° C. while introducing nitrogen through a nozzle at a flow rate of 50 c.c./m. After raising the temperature,
The introduction of nitrogen was stopped, a vacuum pump was connected to the nozzle, and vacuum drying was continued for another hour. After drying, the reaction vessel was evacuated to −76 cmHg. Nitrogen oxide (NO) and nitrogen dioxide (NO 2 ) were introduced through nozzles at 5 cmHg each, and nitrogen was introduced to bring the pressure to atmospheric pressure. The film was left in this state for 45 minutes to allow nitrogen oxides to be adsorbed onto the film. The pressure drop inside the reactor was 3 cmHg. Thereafter, nitrogen was introduced into the reactor to clean the inside of the reactor. The reactor was degassed using a vacuum pump to ensure thorough cleaning. Nitrogen was again introduced into the reactor up to atmospheric pressure. The germicidal lamp was turned on and irradiation started. After 1 hour of irradiation, the lamp was turned off and nitrogen was introduced into the reactor for cleaning. The film was taken out and a portion thereof was cut out and subjected to infrared spectrum measurement (ATR method). The remaining portion was heated for 30 minutes in methanol-water containing 20% NaOH (volume ratio 1/1) to remove ion exchange groups.
After converting into Na + form, it was subjected to dyeing tests, electrolytic tests, etc. As a result, in the red spectrum of the irradiated surface, an absorption band attributable to carboxyl groups with medium intensity was observed at 1780 cm -1 , and a new, albeit weak absorption band was observed at 1610 cm -1 . On the other hand, the absorption band of sulfonic acid groups at 1060 cm -1 observed on the unirradiated surface was hardly observed. A portion of the Na + film (approximately 5 mm x 10 mm) was placed in a staining solution in which 100 mg of crystal violet was dissolved in 100 c.c. of a mixed solvent of 0.5N-HCl-methanol (volume ratio 3:7). It was soaked for 15 hours at room temperature. After washing with water, the cross section was cut into thin sections using a microtome and observed under a microscope. As a result, 15 μm of one surface was not stained at all in a layered manner, and the other parts were stained dark green.
It was found that carboxyl groups were present at a thickness of 15μ from the surface. Table 1 shows the measurement results of the electrolytic test for the film after ultraviolet treatment and the untreated film. The electrolytic test was carried out using a two-chamber cell consisting of a titanium anode chamber and a nickel cathode chamber and an effective current-carrying area of 0.5 dm 2 . A titanium lath material coated with titanium oxide and ruthenium oxide was used as the anode, and a soft iron lath material was used as the cathode. A film is placed between the anode chamber and the cathode chamber, with the anode in close contact with the cathode, with a gap of 2 mm (for those irradiated with ultraviolet rays, the irradiated surface should face the cathode) to increase the Ca concentration in the anode chamber.
A saturated saline solution of 0.5 ppm or less was supplied and discharged at a salt concentration of 3.5N. On the other hand, pure water was supplied to the cathode chamber so that the concentration of NaOH was 11N. Current density
The power was adjusted to 30 A/dm 2 and the temperature in the polar chamber was 90°C.
【表】
実施例 2
実施例1で用いた共重合体よりなり、厚さ0.13
mmで交換容量が0.81(ミリグラム当量/グラム乾
燥樹脂)のフイルムを実施例1と同様にH+型と
した。フイルムを100℃で1時間減圧乾燥した後、
二つのノズルを有するセパラブルフラスコ内に移
した。室温下で一方のノズルより酸化窒素、二酸
化窒素及びアルゴンの混合ガス(容量比でそれぞ
れ5:1:50)を100c.c./minの流速で1時間導
入し、他方のノズルより排出した。その後窒素酸
化物を吸着したフイルムを二つに分け、一方を実
施例1で用いた反応器中に150℃に昇温した後組
込んだ実施例1の方法と同様に反応器内に窒素の
代りにヘリウムを大気圧より0.5気圧程度高く封
入した。殺菌ランプを点灯し30分間照射した。こ
の時、紫外線ランプの強度はフイルムの照射面で
1.5mW/cm2であつた。照射後、反応器内を窒素
で洗浄し、フイルムを取出した。
未処理フイルム、窒素酸化物を吸着させただけ
のフイルム及び上記の処理を行つた本発明のフイ
ルムを実施例1と同様にNaOH/MeOH−H2O
中に室温下で10時間浸漬した。さらに水洗して
Na+型とした。
このような三つのフイルムを減圧乾燥して赤外
スペクトルを測定したところ、本発明の処理を行
つたフイルムの紫外線を照射した面にだけ1680cm
-1のカルボキシレート基(Na+塩)に帰属される
吸収帯が認められ、他のものは全く未処理のもの
と同じ赤外スペクトルを与えた。
一方、染色テストにおいても本発明の処理を行
つたフイルムの照射面から内側に8μ程の厚みで
染色されていない層が認められた。他方、他のフ
イルムは全体が均一に緑色に染色されていた。
又、実施例1の装置で電解テストを行つたとこ
ろ、本発明のフイルムは10NのNaOHを製造して
セル電圧3.30V、電流効率(NaOH)94%、50%
NaOH中のNaCl濃度40ppmであつた。一方、未
処理のフイルム及び窒素酸化物を吸着させただけ
のフイルムはセル電圧がそれぞれ3.23Vと3.25V、
電流効率もそれぞれ54%と55%であつた。
実施例 3
テトラフルオロエチレンとパーフルオロ(3,
6−ジオキサ−4−メチル−7−オクテンスルホ
ニルフルオライド)の共重合体で加水分解した時
の交換容量が0.71(ミリグラム当量/グラム乾燥
樹脂)であり、ポリテトラフルオロエチレンの平
織布(400デニールの糸をタテ・ヨコ共にインチ
当り50本打込んだもの)をはさみ加熱融着して得
られる膜状物で、厚さが0.35mmのものを常法に従
いスルホン酸基をH+型とした。この膜状物を、
ステンレス製で片側より紫外線を照射することが
可能な窓(10cm×15cm・石英製)を設けた反応器
に組込んだ。他面のステンレス板に平型のヒータ
ーを取付け照射面の温度をコントロールできるよ
うにした。水銀ランプSHL−100UV−2(東芝
製)の2本を平行に石英窓から4cmの距離に設置
した。反応室に窒素と二酸化窒素の混合物(容量
比で20:1)を100c.c./分の流速で導入しつつ昇
温した。2時間導入を続けた。反応器の温度は
130℃に到達していた。その後、窒素に切換え50
c.c./分の流速で導入した。反応器より流出する窒
素中に二酸化窒素が紫外線吸収スペクトルで検出
されないことを確認した後、水銀ランプを点灯し
た。2時間照射を続けたところ反応器の温度は
140℃に昇温していた。水銀ランプを消し、反応
室を窒素で洗浄して、膜を反応器より取出した。
実施例1と同様に赤外スペクトルおよび電解性能
を測定した。赤外スペクトルによれば1780cm-1の
カルボキシル基の吸収帯は中位に、また1610cm-1
は弱位に認められた。一方、スルホン酸基は殆ん
ど認められなかつた。実施例1と同様に電解テス
トを行つた結果、6NのNaOHを製造したところ
セル電圧が3.35Vで電流効率が95%であつた。
NaOHの濃度をさらに9Nに増やしたところセル
電圧が3.45V、電流効率は95%のままであつた。
実施例 4
テトラフルオロエチレンとCF2=CF−
OCF2CF2OCF2CF2SO2Fの共重合体で、スルホニ
ルフルオライド基を加水分解した時の交換容量が
1.1(ミリグラム当量/グラム乾燥樹脂)である厚
さ0.15mmのフイルムを常法に従いH+型とした後
本発明の処理を行つた。
フイルムを減圧乾燥後、実施例2で用いたセパ
ラブルフラスコ内に入れた。セパラブルフラスコ
を100℃のオイルバスに浸漬した後、ノズルより
酸化窒素と二酸化窒素の等モル混合物と窒素(容
量比でそれぞれ1:1:10)の混合物を550c.c./
分の流速で導入した。30分導入した後窒素だけ導
入し続け、フラスコ内を洗浄した。
窒素酸化物を吸着したフイルムは実施例1で用
いた反応器に組込んだ。反応器の温度を190℃に
昇温し、反応器内を真空ポンプで−76cmHgまで
減圧とした。殺菌ランプを点灯し、1時間紫外線
を照射した。殺菌ランプを消しフイルムを取出し
た。NaOH/MeOH−H2O中に室温下で5時間
浸漬してNa+型とした後、赤外スペクトルを測定
したところ、照射面には1680cm-1の吸収帯が強く
認められ、また1060cm-1の吸収帯はシヨルダー状
に認められた。他方、未照射の面へ未処理のフイ
ルムのそれと全く同じものであつた。
実施例1と同様に、照射面を陰極側に向けて電
解テストを行つたところ、12NのNaOHを製造し
てセル電圧が3.30V、電流効率が96%であつた。
実施例 5
実施例1で用いたH+型のフイルムを2%のア
ンモニヤ水に室温下で1日浸漬してNH4 +型とし
た。水洗後、風乾したフイルムを実施例1と全く
同じ方法で本発明の処理を行つた。得られたフイ
ルムの赤外スペクトルを測定したところ、紫外線
を照射した面に1780cm-1にカルボキシル基に、
又、1060cm-1のスルホン酸基に起因する吸収帯が
同程度の強度で認められた。
実施例 6
実施例5で得たNH4 +型のフイルムを特開昭54
−4289の方法に従い、フイルムの片面を五塩化リ
ン蒸気と150℃の温度下に接触させて、片面のス
ルホン酸基をスルホニルクロライド基に変えた。
さらに、10%の亜硫酸ナトリウム水溶液中に80℃
で10時間浸漬してスルホニルクロライド基をスル
フイン酸基(Na+塩)とした。得られたフイルム
を希HCl水溶液中に浸漬してH+型とした。
得られたフイルムを実施例1に従い本発明の処
理を行つた。反応温度を110℃に及び窒素酸化物
として酸化窒素を10cmHg、二酸化窒素を2cmHg
とした以外は実施例1と全く同じ方法とした。ま
たスルフイン酸が存在する面を照射した。
得られたフイルムをNa+型に変えた後、実施例
1と同様の電解テストを行つたところ、10Nの
NaOHを製造してセル電圧3.41V、電流効率94%
であつた。また赤外スペクトルを測定したとこ
ろ、照射面には1680cm-1にカルボキシレート基に
相当する吸収帯が強く認められたが、1010cm-1及
び930cm-1のスルフイン酸に基づく吸収帯は殆ん
ど認められなかつた。
実施例 7
実施例4で用いた共重合体でスルホニルフルオ
ライド基を加水分解した時の交換容量が0.3(ミリ
グラム当量/グラム乾燥樹脂)である厚さ0.2mm
のフイルムを冷凍破砕後フルイにかけ、150〜60
メツシユの粒状物を得た。常法に従い粒状物を
H+型に変えた後減圧乾燥を行つた。
粒状物をさらに実施例3で用いたステンレス製
の反応器に反応器の底板を丁度覆う程度に入れ
た。反応器を超音波洗浄器内に置き、反応器に振
動を与えられるようにした。
反応器内に二酸化窒素とヘリウムの混合物(容
量比で1:100)を超音波をかけつつ100c.c./分の
流速で30分導入した。導入後、窒素で反応器内を
洗浄しつつ昇温した。反応器の温度が80℃になつ
た時、実施例3で用いた水銀ランプ2本を石英管
から5cmの距離に設置して点灯した。3時間照射
を続けたところ反応器の温度は100℃に到達して
いた。水銀ランプを消し、超音波をかけるのを止
めて粒状物を取り出した。
粒状物をそのままATR法で赤外スペクトルを
測定したところ、1780cm-1にカルボキシル基に起
因する吸収帯が中位の強度で認められ、他方1060
cm-1のスルホン酸の吸収帯は殆んど認められなか
つた。
一方、粒状物を輪切りにしてその薄片をクリス
タルバイオレツトで染色したものを顕微鏡で観察
したところ、表面より30μが全く染色されず、そ
の内側は緑色に染色されていた。
実施例 8
実施例6で得たスルフイン酸基を有するフイル
ム(H+型)を1%のアンモニア水に室温下で10
時間浸漬し、NH4 +型とした。得られたフイルム
を実施例2と全く同じ方法で本発明の処理を行つ
た。処理後のフイルムの赤外スペクトルを測定し
たところ、照射面には1780cm-1にカルボキシル基
の吸収帯が中位の強度で、又、スルフイン酸基に
基づく吸収帯がシヨルダー状に認められた。
20%のNaOH及び3%のNaClOを含む水溶液
中で80℃で5時間酸化後、実施例1と同様の電解
テストを行つたところ、8NのNaOHを製造して
セル電圧が3.40V、電流効率が93%であつた。
実施例 9〜16
実施例1で用いたH+型のフイルム及び反応器
を用いて窒素酸化物の吸着量とカルボキシル基の
生成量との関係を調べた。即ち、反応器内にフイ
ルムを組込んだ後N2O3(NOとNO2の等モル混合
物)と窒素の混合物を導入した。室温下に1時間
吸着させた後、フイルムの一部を切り取り1%の
NaOH水中に浸漬した。室温下で20時間放置し、
抽出された窒素酸化物の定量に供した。
他方、残りのフイルムは反応器内を大気圧の窒
素に置換後、160℃で1時間紫外線を照射した。
照射後Na+型に変えた後、赤外スペクトルを測定
し、カルボキシレート基及びスルホン酸基の相対
存在量を測定した。これ等の操作をN2O3の分圧
を変えて繰返し、吸着量とカルボキシレート基の
生成具合を調べた。結果を表−2に示す。[Table] Example 2 Made of the copolymer used in Example 1, thickness 0.13
A film having an exchange capacity of 0.81 (milligram equivalent/gram dry resin) in mm was made into H + form as in Example 1. After drying the film under reduced pressure at 100℃ for 1 hour,
Transferred into a separable flask with two nozzles. At room temperature, a mixed gas of nitrogen oxide, nitrogen dioxide, and argon (volume ratio: 5:1:50, respectively) was introduced through one nozzle at a flow rate of 100 c.c./min for 1 hour, and then discharged through the other nozzle. Thereafter, the film adsorbing nitrogen oxides was divided into two parts, and one part was placed in the reactor used in Example 1 after the temperature was raised to 150℃. Instead, helium was sealed at a pressure approximately 0.5 atmospheres higher than atmospheric pressure. A sterilization lamp was turned on and irradiated for 30 minutes. At this time, the intensity of the ultraviolet lamp is determined by the irradiated surface of the film.
It was 1.5mW/ cm2 . After irradiation, the inside of the reactor was cleaned with nitrogen and the film was taken out. An untreated film, a film on which nitrogen oxides were simply adsorbed, and a film of the present invention subjected to the above treatment were treated with NaOH/MeOH-H 2 O in the same manner as in Example 1.
It was immersed in water for 10 hours at room temperature. Wash more with water
It was made into Na + type. When these three films were dried under reduced pressure and their infrared spectra were measured, it was found that only the ultraviolet irradiated side of the film treated according to the present invention had a wavelength of 1680 cm.
An absorption band assigned to the -1 carboxylate group (Na + salt) was observed, and the others gave an infrared spectrum exactly the same as the untreated one. On the other hand, in the dyeing test, an undyed layer with a thickness of about 8 μm was observed inside the irradiated surface of the film treated according to the present invention. On the other hand, the other films were uniformly dyed green throughout. Further, when an electrolytic test was conducted using the apparatus of Example 1, the film of the present invention produced 10N NaOH, had a cell voltage of 3.30V, and a current efficiency (NaOH) of 94% and 50%.
The NaCl concentration in NaOH was 40 ppm. On the other hand, the cell voltage of the untreated film and the film that only adsorbed nitrogen oxides was 3.23V and 3.25V, respectively.
The current efficiency was also 54% and 55%, respectively. Example 3 Tetrafluoroethylene and perfluoro(3,
The exchange capacity when hydrolyzed with a copolymer of 6-dioxa-4-methyl-7-octensulfonyl fluoride (6-dioxa-4-methyl-7-octensulfonyl fluoride) is 0.71 (milligram equivalent/gram dry resin), A film-like material obtained by sandwiching and heat-sealing denier thread (50 strands per inch both vertically and horizontally), with a thickness of 0.35 mm, and converting the sulfonic acid group into H + type using the usual method. did. This film-like substance
It was installed in a reactor made of stainless steel and equipped with a window (10 cm x 15 cm, made of quartz) that allows ultraviolet rays to be irradiated from one side. A flat heater was attached to the stainless steel plate on the other side to control the temperature of the irradiated surface. Two mercury lamps SHL-100UV-2 (manufactured by Toshiba) were installed in parallel at a distance of 4 cm from the quartz window. A mixture of nitrogen and nitrogen dioxide (20:1 by volume) was introduced into the reaction chamber at a flow rate of 100 c.c./min while the temperature was raised. The introduction continued for 2 hours. The temperature of the reactor is
The temperature had reached 130℃. Then switch to nitrogen 50
A flow rate of cc/min was introduced. After confirming that no nitrogen dioxide was detected in the nitrogen flowing out from the reactor by ultraviolet absorption spectrum, the mercury lamp was turned on. After 2 hours of continuous irradiation, the temperature of the reactor was
The temperature had risen to 140℃. The mercury lamp was turned off, the reaction chamber was flushed with nitrogen, and the membrane was removed from the reactor.
The infrared spectrum and electrolytic performance were measured in the same manner as in Example 1. According to the infrared spectrum, the absorption band of carboxyl group at 1780 cm -1 is in the middle, and the absorption band of carboxyl group at 1610 cm -1
was recognized as weak. On the other hand, almost no sulfonic acid groups were observed. As a result of conducting an electrolysis test in the same manner as in Example 1, when 6N NaOH was produced, the cell voltage was 3.35V and the current efficiency was 95%.
When the concentration of NaOH was further increased to 9N, the cell voltage remained at 3.45V and the current efficiency remained at 95%. Example 4 Tetrafluoroethylene and CF 2 =CF−
A copolymer of OCF 2 CF 2 OCF 2 CF 2 SO 2 F, the exchange capacity when hydrolyzing the sulfonyl fluoride group is
A film having a thickness of 0.15 mm with a ratio of 1.1 (milligram equivalent/gram dry resin) was converted into H + form according to a conventional method and then subjected to the treatment of the present invention. After drying the film under reduced pressure, it was placed in the separable flask used in Example 2. After immersing the separable flask in an oil bath at 100°C, 550 c.c./cm of an equimolar mixture of nitrogen oxide and nitrogen dioxide and a mixture of nitrogen (volume ratio: 1:1:10, respectively) were poured through a nozzle.
It was introduced at a flow rate of minutes. After 30 minutes of introduction, only nitrogen was continued to be introduced to wash the inside of the flask. The film adsorbing nitrogen oxides was incorporated into the reactor used in Example 1. The temperature of the reactor was raised to 190°C, and the pressure inside the reactor was reduced to -76 cmHg using a vacuum pump. A germicidal lamp was turned on and ultraviolet rays were irradiated for 1 hour. I turned off the germicidal lamp and took out the film. After immersing it in NaOH/MeOH-H 2 O for 5 hours at room temperature to convert it into Na + form, the infrared spectrum was measured, and a strong absorption band at 1680 cm -1 was observed on the irradiated surface, and a strong absorption band at 1060 cm - The absorption band 1 was observed in a shoulder shape. On the other hand, the unirradiated side was exactly the same as that of the untreated film. As in Example 1, an electrolytic test was performed with the irradiated surface facing the cathode, and 12N NaOH was produced, the cell voltage was 3.30 V, and the current efficiency was 96%. Example 5 The H + type film used in Example 1 was immersed in 2% ammonia water at room temperature for one day to form the NH 4 + type film. After washing with water and air drying, the film was subjected to the treatment of the present invention in exactly the same manner as in Example 1. When the infrared spectrum of the obtained film was measured, it was found that on the surface irradiated with ultraviolet rays, there were carboxyl groups at 1780 cm -1 .
Furthermore, an absorption band at 1060 cm -1 due to the sulfonic acid group was observed with similar intensity. Example 6 The NH 4 + type film obtained in Example 5 was
-4289, one side of the film was brought into contact with phosphorus pentachloride vapor at a temperature of 150°C to convert the sulfonic acid groups on one side to sulfonyl chloride groups.
Furthermore, in a 10% sodium sulfite aqueous solution at 80°C.
The sulfonyl chloride group was converted into a sulfinic acid group (Na + salt) by immersion in water for 10 hours. The obtained film was immersed in a dilute aqueous HCl solution to form an H + form. The obtained film was subjected to the treatment of the present invention according to Example 1. The reaction temperature was raised to 110℃, and the nitrogen oxides were 10 cmHg of nitrogen oxide and 2 cmHg of nitrogen dioxide.
The method was exactly the same as in Example 1 except for the following. Also, the surface where sulfinic acid was present was irradiated. After changing the obtained film to Na + type, an electrolytic test similar to that in Example 1 was conducted, and the result was
Manufacture NaOH, cell voltage 3.41V, current efficiency 94%
It was hot. Furthermore, when we measured the infrared spectrum, a strong absorption band corresponding to carboxylate groups was observed at 1680 cm -1 on the irradiated surface, but absorption bands based on sulfinic acid at 1010 cm -1 and 930 cm -1 were almost completely absent. It was not recognized. Example 7 The copolymer used in Example 4 had a thickness of 0.2 mm with an exchange capacity of 0.3 (milligram equivalent/gram dry resin) when the sulfonyl fluoride group was hydrolyzed.
After freezing and crushing the film, put it through a sieve and
Granules of mesh were obtained. Remove granules according to the usual method.
After changing to H + form, it was dried under reduced pressure. The granular material was further placed in the stainless steel reactor used in Example 3 to the extent that it just covered the bottom plate of the reactor. The reactor was placed in an ultrasonic cleaner so that vibrations could be applied to the reactor. A mixture of nitrogen dioxide and helium (1:100 by volume) was introduced into the reactor at a flow rate of 100 c.c./min for 30 minutes while applying ultrasound. After the introduction, the temperature was increased while cleaning the inside of the reactor with nitrogen. When the temperature of the reactor reached 80° C., the two mercury lamps used in Example 3 were placed at a distance of 5 cm from the quartz tube and turned on. When irradiation continued for 3 hours, the temperature of the reactor reached 100°C. The mercury lamp was turned off, the ultrasound application was stopped, and the particulate material was removed. When the infrared spectrum of the particulate matter was directly measured using the ATR method, an absorption band at 1780 cm -1 due to carboxyl groups was observed with medium intensity, and an absorption band at 1060 cm -1 with medium intensity was observed.
Almost no absorption band of sulfonic acid at cm -1 was observed. On the other hand, when the granular material was sliced into rings and the thin sections were stained with crystal violet and observed under a microscope, it was found that 30 μm from the surface was not stained at all, and the inside was stained green. Example 8 The sulfinic acid group-containing film (H + type) obtained in Example 6 was dissolved in 1% ammonia water at room temperature for 10 minutes.
It was soaked for an hour to form NH 4 + form. The obtained film was subjected to the treatment of the present invention in exactly the same manner as in Example 2. When the infrared spectrum of the film after treatment was measured, an absorption band of carboxyl groups with medium intensity was observed at 1780 cm -1 on the irradiated surface, and a shoulder-shaped absorption band due to sulfinic acid groups was observed. After oxidation at 80°C for 5 hours in an aqueous solution containing 20% NaOH and 3% NaClO, the same electrolytic test as in Example 1 was performed, and 8N NaOH was produced, the cell voltage was 3.40V, and the current efficiency was was 93%. Examples 9 to 16 Using the H + type film and reactor used in Example 1, the relationship between the amount of nitrogen oxides adsorbed and the amount of carboxyl groups produced was investigated. That is, after the film was installed in the reactor, a mixture of N 2 O 3 (an equimolar mixture of NO and NO 2 ) and nitrogen was introduced. After adsorption at room temperature for 1 hour, a part of the film was cut out and 1%
Soaked in NaOH water. Leave it at room temperature for 20 hours,
The extracted nitrogen oxides were quantified. On the other hand, the remaining film was irradiated with ultraviolet rays at 160° C. for 1 hour after purging the inside of the reactor with nitrogen at atmospheric pressure.
After changing to the Na + form after irradiation, infrared spectra were measured to determine the relative abundance of carboxylate groups and sulfonic acid groups. These operations were repeated by changing the partial pressure of N 2 O 3 to examine the amount of adsorption and the degree of formation of carboxylate groups. The results are shown in Table-2.
【表】【table】
Claims (1)
酸化物を吸着させた後、紫外線を照射することを
特徴とするカルボキシル基を有する含弗素高分子
体の製造方法。 2 スルホニル基がスルホン酸基またはそのアン
モニウム塩である特許請求の範囲第1項記載の方
法。 3 窒素酸化物の吸着量がスルホニル基に対し当
量比で0.01以上である特許請求の範囲第1項記載
の方法。 4 含弗素高分子体がパーフルオロ系の高分子よ
りなる特許請求の範囲第1項記載の方法。 5 含弗素高分子体がパーフルオロオレフインと
パーフルオロアルキルスルホニルビニルエーテル
の共重合体である特許請求の範囲第1項記載の方
法。 6 窒素酸化物がNO2、N2O3またはNOとNO2
の混合物である特許請求の範囲第1項記載の方
法。 7 含弗素高分子体が膜状物である特許請求の範
囲第1項記載の方法。[Scope of Claims] 1. A method for producing a fluorine-containing polymer having a carboxyl group, which comprises adsorbing nitrogen oxides onto the fluorine-containing polymer having a sulfonyl group, and then irradiating the polymer with ultraviolet rays. 2. The method according to claim 1, wherein the sulfonyl group is a sulfonic acid group or an ammonium salt thereof. 3. The method according to claim 1, wherein the adsorption amount of nitrogen oxides is 0.01 or more in equivalent ratio to sulfonyl groups. 4. The method according to claim 1, wherein the fluorine-containing polymer is a perfluorinated polymer. 5. The method according to claim 1, wherein the fluorine-containing polymer is a copolymer of perfluoroolefin and perfluoroalkylsulfonyl vinyl ether. 6 Nitrogen oxides are NO 2 , N 2 O 3 or NO and NO 2
The method according to claim 1, which is a mixture of. 7. The method according to claim 1, wherein the fluorine-containing polymer is a film-like material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2634983A JPS59152903A (en) | 1983-02-21 | 1983-02-21 | Production of fluorine-containing polymer having carboxyl group |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2634983A JPS59152903A (en) | 1983-02-21 | 1983-02-21 | Production of fluorine-containing polymer having carboxyl group |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59152903A JPS59152903A (en) | 1984-08-31 |
| JPS6325602B2 true JPS6325602B2 (en) | 1988-05-26 |
Family
ID=12190977
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2634983A Granted JPS59152903A (en) | 1983-02-21 | 1983-02-21 | Production of fluorine-containing polymer having carboxyl group |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59152903A (en) |
-
1983
- 1983-02-21 JP JP2634983A patent/JPS59152903A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59152903A (en) | 1984-08-31 |
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