JPS6026143B2 - Method for improving film with ion exchange ability - Google Patents

Method for improving film with ion exchange ability

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Publication number
JPS6026143B2
JPS6026143B2 JP52089241A JP8924177A JPS6026143B2 JP S6026143 B2 JPS6026143 B2 JP S6026143B2 JP 52089241 A JP52089241 A JP 52089241A JP 8924177 A JP8924177 A JP 8924177A JP S6026143 B2 JPS6026143 B2 JP S6026143B2
Authority
JP
Japan
Prior art keywords
film
ion exchange
vapor
processing agent
ion
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
JP52089241A
Other languages
Japanese (ja)
Other versions
JPS5424284A (en
Inventor
研介 藻谷
登志生 奥
俊勝 佐田
昭彦 中原
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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Filing date
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Application filed by Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP52089241A priority Critical patent/JPS6026143B2/en
Publication of JPS5424284A publication Critical patent/JPS5424284A/en
Publication of JPS6026143B2 publication Critical patent/JPS6026143B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は陽イオン交換館を有するフィルムの改良に係る
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvements in films having cation exchange chambers.

詳しくは、側鎖にイオン交換基を有し且つ該イオン交換
基が結合している炭素に少なくとも1ケのフッ素原子を
結合しているイオン交換館を有するフィルムの少なくと
も一方の表面に存在するイオン交換基のイオン交換館を
失わせる方法であって、腸イオン交換基例えばスルホン
酸基、カルボキシル基、りん酸基等を対応する酸ハラィ
ド基に変換させる方法である。本発明における酸ハラィ
ド基は必ずしも安定ではなく加熱、酸或いはアルカリー
こよって更に別の官能基に変えることができる。従って
、本発明により得られたイオン交換能を有するフィルム
のうち、表面のみのイオン交換能を低減又は消失させた
ものは、それ自体、電気透析用陽イオン交換膜として低
電荷イオンを選択的に透過させる性質や逆に陰イオン輪
率特に水酸イオンの輸率を減ずる等の用途上の改良が見
られるが、更に第二の改良手段を施すための中間処理物
として有効に利用できる。例えば、本発明により得られ
たフィルムを更にアンモニア、アミン、ポリアミン、ア
ミノアルコール等で処理して表面のみにアミノ基、酸ア
ミド結合、水酸基等の親水基又はアルキル基等の疎水基
を結合させ一層の改良を図ることもできるし、また彼処
理フィルムが本釆持っていた賜イオン交換基とは別種の
腸イオン交換基又は陰イオン交換基を導入することもで
きる。かかる例としては、例えば本来スルホン酸基を有
するフィルムに本発明の処理を施して、その少なくとも
一方の表層部分にスルホニルハラィド基を形成させ、こ
れを酸化又は還元することによってカルボキシ基に変え
ることができる。この場合、本発明の処理によりフィル
ム中の存在する全スルホン酸基をスルホニルハラィド基
にすれば実質的に全イオン交換基をカルボン酸基に変え
得るし、またフィルムの表層を極く浅く(例えば20〃
程度)スルホニルハライド基にすれば薄層上にカルボン
酸基を持つスルホン酸、力ルボン酸の両交換基を有する
イオン交換膜とすることができる。このようなイオン交
換膜は食塩の電解用陣膜として有効である。本発明にあ
っては側鎖に腸イオン交換基を有し且つ該イオン交換基
が結合している炭素に少なくとも1ケのフッ素原子を結
合している腸イオン交換能を有するフィルムを用いるこ
とが必須であり、かかる構造である場合に本発明の処理
がスムーズに行われるのである。
Specifically, ions present on at least one surface of a film having an ion exchange group in its side chain and an ion exchange group having at least one fluorine atom bonded to the carbon to which the ion exchange group is bonded. This is a method of eliminating the ion exchange facility of the exchange group, and is a method of converting intestinal ion exchange groups such as sulfonic acid groups, carboxyl groups, phosphate groups, etc. into corresponding acid halide groups. The acid halide group in the present invention is not necessarily stable and can be further converted into another functional group by heating, acid or alkali. Therefore, among the films having ion-exchange ability obtained by the present invention, those whose ion-exchange ability is reduced or eliminated only on the surface can be used as a cation-exchange membrane for electrodialysis to selectively remove low-charge ions. Improvements in the permeability property and conversely the anion ring rate, especially the transport number of hydroxyl ions, can be seen in terms of usage, and it can be effectively used as an intermediate treatment product for the second improvement means. For example, the film obtained according to the present invention is further treated with ammonia, amine, polyamine, amino alcohol, etc. to bond hydrophilic groups such as amino groups, acid amide bonds, hydroxyl groups, or hydrophobic groups such as alkyl groups only to the surface. In addition, it is also possible to introduce a different type of ion exchange group or anion exchange group from the ion exchange group that the treated film had. As an example of such a film, for example, a film that originally has sulfonic acid groups is subjected to the treatment of the present invention to form a sulfonyl halide group on at least one surface layer portion, and this is converted into a carboxy group by oxidation or reduction. be able to. In this case, by converting all the sulfonic acid groups present in the film into sulfonyl halide groups by the treatment of the present invention, substantially all the ion exchange groups can be changed to carboxylic acid groups, and the surface layer of the film can be made very shallow. (For example, 20
If a sulfonyl halide group is used, an ion exchange membrane having both sulfonic acid and carboxylic acid exchange groups with carboxylic acid groups on the thin layer can be obtained. Such an ion exchange membrane is effective as a membrane for electrolysis of common salt. In the present invention, it is possible to use a film having intestinal ion exchange ability, which has an intestinal ion exchange group in its side chain and has at least one fluorine atom bonded to the carbon to which the ion exchange group is bonded. This is essential, and the process of the present invention can be performed smoothly with such a structure.

また処理剤として五塩化りん、三臭化りん及び三沃化り
んは、いずれも本発明の目的を達成することが実験的に
確認されたものである。これらの処理剤はいずれも固体
であり、しかも高濃度で溶解する適当な溶媒がない。従
って、フィルムの如き大表面積の固形物と均一に反応さ
せることが極めて困難である。そこで、まずこれらの処
理剤の蒸気(蒸発及び昇華によるものを含む)を用いる
固一気体系の反応が考えられる。勿論十分な温度と均一
な気流を保てば、かかる反応系においても十分に目的を
達することが可能であるが、通常キヤリャーガスに同伴
する処理剤の濃度が薄いとか、フィルム全面に亘って均
一な濃度及び温度が得難い。このため、反応に長時間を
要するとか或いは均一な処理が難かしい等の工業化が容
易でない面があった。本発明は極めて均一な処理を比較
的短時間で行う方法を提案するものであって、側鎖に腸
イオン交換基を有し且つ該イオン交換基が結合している
炭素に少なくとも1ケのフッ素原子を結合している腸イ
オン交換能を有するフィルムの少なくとも一方の表面に
、五塩化りぼ、三臭化りん及び三沃化りんのうち少なく
とも一種のハロゲン化合物を蒸着せしわた後、これを1
4ぴ○〜180qoに加熱反応させて、該フィルムの少
なくとも表面に存在する腸イオン交換基のイオン交換能
を失わせることを特徴とするイオン交換性フィルムの改
良方法である。
Further, as processing agents, phosphorus pentachloride, phosphorus tribromide, and phosphorus triiodide have all been experimentally confirmed to achieve the object of the present invention. All of these processing agents are solids, and there are no suitable solvents that can dissolve them in high concentrations. Therefore, it is extremely difficult to react uniformly with a solid material having a large surface area such as a film. Therefore, a solid-gas system reaction using vapors (including those caused by evaporation and sublimation) of these processing agents may be considered. Of course, if sufficient temperature and uniform air flow are maintained, it is possible to achieve the desired purpose in such a reaction system, but normally the concentration of the processing agent accompanying the carrier gas is low, or the processing agent is not uniform over the entire surface of the film. Concentration and temperature are difficult to obtain. For this reason, industrialization has been difficult, such as requiring a long time for the reaction or making uniform treatment difficult. The present invention proposes a method for performing extremely uniform treatment in a relatively short time, and the present invention proposes a method for performing extremely uniform treatment in a relatively short time. After vapor-depositing at least one type of halogen compound from phosphorus pentachloride, phosphorus tribromide, and phosphorus triiodide on at least one surface of the film having intestinal ion exchange ability that binds atoms, and wrinkling this, 1
This is a method for improving an ion-exchangeable film, characterized in that the ion-exchange ability of intestinal ion-exchange groups present at least on the surface of the film is lost by heating the film to a temperature of 4 to 180 qo.

本発明の特徴の一つは、まずフィルム上に均一に処理剤
を蒸着させる点にある。
One of the features of the present invention is that the processing agent is first uniformly deposited on the film.

このように蒸着させることによって、次の反応工程で、
極めて均一に且つ濃厚な処理剤の存在下に反応を行わせ
ることができるので、処理の均一性及び処理時間の短縮
が可能となる。フィルム上に処理剤を蒸着させる手段は
特に限定されないが、例えば後述の第1図に示す如く、
処理剤の気化温度以下に保ったフィルムを処理剤蒸着と
接触させることによって容易に達成できる。
By vapor depositing in this way, in the next reaction step,
Since the reaction can be carried out extremely uniformly and in the presence of a concentrated processing agent, it is possible to achieve uniform processing and shorten processing time. The means for depositing the processing agent on the film is not particularly limited, but for example, as shown in FIG. 1 described below,
This can be easily achieved by bringing a film maintained at a temperature below the vaporization temperature of the processing agent into contact with the processing agent vapor deposition.

また処理剤を均一に蒸着したフィルムは蒸着処理剤が再
気化しないよう保存又は反応状態を配慮する必要がある
Furthermore, for a film on which a processing agent has been uniformly deposited, consideration must be given to storage or reaction conditions so that the vapor deposition processing agent does not re-vaporize.

次いで処理剤を反応させるには通常加熱が用いられ「1
4ぴ○〜18ぴ0の範囲内で低温程長時間例えば数時間
また高温程短時間例えば数分間処理される。
Next, heating is usually used to react the processing agent.
Within the range of 4 to 18 pi, the lower the temperature, the longer the treatment time, for example several hours, and the higher the temperature, the shorter time treatment, for example several minutes.

またフィルム内部まで深く処理する場合はフィルムの厚
さにもよるが、例えば0.1肋程度のフィルムにあって
は容易に中心部まで処理し得るし、また0.8側程度で
あればフィルムの両面から処理を行っても全イオン交換
基を変換するには相当に高い温度と長時間とを要する。
しかしながらt フィルムの表層部分例えば20ム以下
の浅い部分のみを処理する場合には、例えば160℃で
20分もあれば十分である。本発明を実施するについて
好適な手段の例を示す。
In addition, when processing deep inside the film, it depends on the thickness of the film, but for example, if the film is about 0.1 rib, it can be easily processed to the center, and if the film is about 0.8 Even if treatment is performed from both sides, considerably high temperatures and long periods of time are required to convert all ion exchange groups.
However, when treating only the surface layer of the t film, for example, a shallow portion of 20 μm or less, 20 minutes at 160° C., for example, is sufficient. Examples of suitable means for carrying out the invention are shown below.

第1図に蒸発の二般的手段を示す。側鎖に陽イオン交換
基を有し且つ該イオン交換基が結合している炭素に少な
くとも1ケのフッ素原子を結合しているイオン交換能を
有するフィルム、例えばデュポン社製のイオン交換膿で
あるパーフルオロ(アルキルビニルヱーテルスルホニル
フルオライド)とテトラフルオロェチレンの共重合体の
加水分解物能、1‘ま矢印の方向に移動させニツプロー
ル11及び12に支えられて黍着函2上を通過する。蒸
着函2は中に処理剤即ち五塩化りん、三臭化りん及び三
沃化りんのうち少なくとも一種のハロゲン化りん化合物
が入れられており、該函は加熱装置3によって加熱され
ることによって、処理剤の蒸気が充満している。場合に
よっては、蒸着函は減圧にしておくのも有効である。か
くすることによって「処理剤蒸気は低温のフィルム上で
凝縮又は析出固化する。処理剤の蒸着を行うフィルムは
適当な長さに裁断された膜であってもよいし、また最尺
に巻き込まれたフィルムであってもよい。
FIG. 1 shows two general means of evaporation. A film with ion exchange ability that has a cation exchange group in its side chain and has at least one fluorine atom bonded to the carbon to which the ion exchange group is bonded, such as ion exchange phlegm manufactured by DuPont. The hydrolyzate of a copolymer of perfluoro(alkyl vinyl ethersulfonyl fluoride) and tetrafluoroethylene is moved 1' in the direction of the arrow and supported by Nipprol 11 and 12 on the dust box 2. pass. The vapor deposition box 2 contains a processing agent, that is, at least one type of halogenated phosphorus compound among phosphorus pentachloride, phosphorus tribromide, and phosphorus triiodide, and is heated by a heating device 3 to The room is filled with processing agent vapor. In some cases, it may be effective to keep the vapor deposition box under reduced pressure. In this way, the processing agent vapor condenses or precipitates and solidifies on the low-temperature film.The film on which the processing agent is vapor-deposited may be a film cut to an appropriate length, or it may be rolled up to the maximum length. It may also be a film.

処理剤を黍着したフィルムは蒸着面同志が接するように
2枚重ね合せて巻き取るか、又は蒸着面に別のフィルム
を重ねて巻き取る等して保管するか「又はこのように巻
き取った後ただちにそのままの状態で140℃以上に加
熱することによって本発明を達成することができる。ま
た最尺の場合には一旦巻き取った蒸着フィルム又は黍着
工程から出て来るフィルムを巻き取ることなく、第2図
に示す如く加熱ロール4,5,6にかけることもできる
。加熱ロ−ルは第2図にあっては3本示したが、この数
、形状等は加熱時間との関係で適宜決まるものである。
第3図に別の態様の例を示す。本例は最尺フィルム1が
蒸着函2に入り、次いで反応工程に連続的に送られる場
合である。蒸着函2は可及的に外気を遮断された函であ
って、必要によりパイプ8より吸引されており、処理剤
は本図に示されていない別の装置で蒸発させ該蒸気のみ
又は、該蒸気を窒素その他の不活性なキャリャーガスに
よってパイプ9より導入される。あるいは黍着函2の内
部で処理剤を蒸発させることも出釆る。例えば、その一
つの態様として蒸着函内の上部に処理剤を盛った金網棚
を設け、加熱により処理剤蒸気を発生させる。これは第
1図の上下が逆になった場合に相当する。この場合に函
内を予め減圧にしておくことも効果的である。要は、処
理を受けるフィルム上に処理剤の均一な層を形成させる
ことが重要であり、そのためには蒸着函内の処理剤蒸気
の濃度が均一に保たれる必要がある。
Film coated with a processing agent can be stored by stacking two films together so that their vapor-deposited surfaces are in contact with each other, or by rolling up another film on the vapor-deposited surface. The present invention can be achieved by immediately heating the film to 140°C or higher in that state.In addition, in the case of the largest length, the vapor-deposited film that has been rolled up or the film that comes out of the coating process is not rolled up. , heating rolls 4, 5, and 6 as shown in Figure 2.Three heating rolls are shown in Figure 2, but the number, shape, etc. may vary depending on the heating time. It is decided as appropriate.
FIG. 3 shows an example of another embodiment. In this example, the largest film 1 is placed in the vapor deposition box 2 and then continuously sent to the reaction process. The vapor deposition box 2 is a box that is shielded from outside air as much as possible, and suction is carried out through a pipe 8 if necessary, and the processing agent is evaporated in another device not shown in this figure, and only the vapor or the vapor is removed. Steam is introduced through pipe 9 with nitrogen or other inert carrier gas. Alternatively, the processing agent may be evaporated inside the dust collecting box 2. For example, in one embodiment, a wire mesh shelf filled with a processing agent is provided in the upper part of the vapor deposition box, and processing agent vapor is generated by heating. This corresponds to the case where the top and bottom of FIG. 1 are turned upside down. In this case, it is also effective to reduce the pressure inside the box in advance. In short, it is important to form a uniform layer of the processing agent on the film to be processed, and for this purpose it is necessary to maintain a uniform concentration of the processing agent vapor within the deposition box.

通常、フィルムに直接処理剤蒸気を反応させる場合に比
べると蒸着に要する時間は頗る短い。それ故、その短い
時間だけ函内の蒸気濃度を均一に保つことは、反応に要
する長時間にわたって函内蒸気濃度を均一に維持しなけ
ればならない直接反応の場合に比して極めて容易であり
、これは本法を実施する上での非常に大きな利点である
。葵着函は加熱又は保温されているのが好ましい。
Usually, the time required for vapor deposition is much shorter than when the film is directly reacted with processing agent vapor. Therefore, it is extremely easy to maintain a uniform vapor concentration inside the box for that short period of time, compared to the case of direct reaction, where the vapor concentration inside the box must be maintained uniformly over a long period of time required for the reaction. This is a huge advantage in implementing this method. It is preferable that the Aoi box is heated or kept warm.

また蒸着函にはフィルム冷却用の冷却水を通すのも蒸着
効果を上げる点で好ましい。処理剤を蒸着したフィルム
は連続的に次の反応工程に導かれる。反応工程は通常蒸
着函と同様に外気をほぼ遮断した函状物7中に収容され
るのがよい。ここではフィルムがロール10に支えられ
た無限ベルト15の間に挟まれて移動する間に加熱装置
16の熱により反応を生ずる。この場合に蒸着している
処理剤の気散を防止するため、パイプ13より処理剤の
蒸気を導入するのも好適である。また処理剤は一般に劇
薬であるため外部に洩れるのを防ぐためにパイプ14よ
り吸引しておくことも衛生上好ましい場合がある。実施
例 1 パーフルオロ(3,6ージオキサー4ーメチル−7−オ
クテンスルホニルフルオラィド)を主成分とするパーフ
ルオロアルキルピニルェーテルスルホニルフルオライド
とテトラフルオロエチレンの共重合物を加水分解処理し
てスルホン酸型の腸イオン交換膜とした。
It is also preferable to pass cooling water for cooling the film through the deposition box in order to increase the deposition effect. The film on which the processing agent has been deposited is continuously led to the next reaction step. The reaction step is preferably carried out in a box-like object 7 that is substantially shut off from outside air, similar to a normal vapor deposition box. Here, while the film is sandwiched between the endless belts 15 supported by the rolls 10 and moves, a reaction occurs due to the heat of the heating device 16. In this case, in order to prevent the vapor-deposited processing agent from being diffused, it is also preferable to introduce the vapor of the processing agent through the pipe 13. Furthermore, since the processing agent is generally a powerful chemical, it may be preferable from a sanitary standpoint to suck it up through the pipe 14 to prevent it from leaking outside. Example 1 A copolymer of perfluoroalkyl pinylethersulfonyl fluoride containing perfluoro(3,6-dioxa-4-methyl-7-octensulfonyl fluoride) as a main component and tetrafluoroethylene was hydrolyzed. A sulfonic acid type intestinal ion exchange membrane was used.

これの交換容量は0.91ミリ当量/グラム乾燥樹脂(
日型)で厚みが0.15肌であった。これを過剰の60
%HN03中に60qoで16時間浸潰して完全に酸型
にしたのちに、水洗後減圧乾燥した。この膜の15伽×
20弧を、五塩化りんを約10夕入れた第1図に示す如
き蒸着函(開ロ部約10仇×12肌に挿着し、ニッブロ
ールを回転させることなく、下部より約200℃に加熱
して1ぴ分間で均質な五塩化りんの蒸着被膜が得られた
。このものを次いで、フェロ板の間に挟んで150℃で
2■ト間加圧加熱した。
The exchange capacity of this is 0.91 meq/g dry resin (
The thickness was 0.15 skin. This is an excess of 60
After soaking in %HN03 at 60 qo for 16 hours to completely convert it into an acid form, it was washed with water and dried under reduced pressure. 15 x of this film
Insert the 20 arc into a vapor deposition box as shown in Figure 1 (approximately 10 in. x 12 skin in the opening) into which phosphorus pentachloride was poured for about 10 in. Without rotating the nib roll, heat to about 200°C from the bottom. A homogeneous vapor-deposited film of phosphorus pentachloride was obtained in 1 minute.The film was then sandwiched between ferro plates and heated under pressure at 150°C for 2 hours.

その後、.膜を水洗し赤外反射スペクトルによって表層
部を見たところ、142比松‐1に強い吸収ピークが認
められ、逆に1060仇‐1のスルホン酸ピークは消失
していた。この膜をクリスタルバイオレットの酸性俗に
浸潰して16時間放置後、断面を顕微鏡で見たところ、
膜の両側が約10ミクロンづつ染色されず、中央部は鮮
明に染色されていた。念のため、この膜を10%のNa
OHーメタノール溶液に浸潰してスルホニルクロラィド
基をスルホン酸基に加水分解したのち、再び染色テスト
をしたところ、膜の断面に関して鮮明に染色され、赤外
反射スペクトルでは1420軌の吸収が消失し、106
0軌の吸収が再び現われた。次いでこの膜を再び硝酸に
よって酸型として硫黄を蛍光X線によって分析したとこ
ろ、硝酸浸潰して酸型にした五塩化りん処理する前の膜
に比較して0.7%しか硫黄含量は減少していなかった
。実施例 2テトラフルオロエチレンとパーフルオロ(
3,6−ジオキサー4ーメチルー7ーオクテンスルホニ
ルフルオラィド)を主成分とするパーフルオロアルキル
ビニルエーテルスルホニルフルオライドの共重合膜状物
の加水分解物で交換容量が0.83ミリ当量/グラム乾
燥膜(日型)のものを用いた。
after that,. When the membrane was washed with water and the surface layer was examined using an infrared reflection spectrum, a strong absorption peak was observed at 142 Himatsu-1, and conversely, the sulfonic acid peak at 1060 Himatsu-1 had disappeared. After soaking this membrane in acidic crystal violet solution and leaving it for 16 hours, the cross section was examined under a microscope.
Approximately 10 microns on both sides of the membrane were not stained, and the center was clearly stained. Just to be sure, this film was coated with 10% Na.
After hydrolyzing the sulfonyl chloride groups into sulfonic acid groups by immersion in an OH-methanol solution, a dyeing test was performed again, and the cross section of the membrane was clearly dyed, and the absorption at 1420 orbital disappeared in the infrared reflection spectrum. , 106
Zero orbital absorption reappeared. Next, this membrane was made into an acid form with nitric acid again and analyzed for sulfur by fluorescent X-rays.The sulfur content was reduced by only 0.7% compared to the membrane before phosphorus pentachloride treatment, which had been soaked in nitric acid and made into an acid form. It wasn't. Example 2 Tetrafluoroethylene and perfluoro(
A hydrolyzate of a copolymer membrane of perfluoroalkyl vinyl ether sulfonyl fluoride containing 3,6-dioxer (4-methyl-7-octensulfonyl fluoride) as the main component, with an exchange capacity of 0.83 meq/g dry membrane. (Japanese type) was used.

これを第1図に示す装置により、被曝時間が1び分にな
るようゆっくりと巻き取った。尚、巻き取りに際しては
テフロンPFA(デュポン社製)フィルムを重ね合せた
。巻き取ったフィルムは、そのまま150午0の空気裕
中で1.虫時間加熱功反応させた。このフィルムについ
て、実施例1と同機のテストを行ったところ、ほぼ同様
の結果が得られた。これによって、連続的に処理するこ
とが可能であることが確認された。実施例 3 実施例1で用いたと同じパ−フルオロ(3,6ージオキ
サー4ーメチル−7ーオクテンスルホニルフルオライド
)の共重合体フィルムの加水分解したものでスルホン酸
ソーダ型の膜を用いた。
This was slowly wound up using the apparatus shown in FIG. 1 so that the exposure time was 1 minute. Incidentally, during winding, a Teflon PFA (manufactured by DuPont) film was overlapped. The wound film was placed in an air bath at 150 pm for 1. The insects reacted well after heating for a while. When this film was tested on the same machine as in Example 1, almost the same results were obtained. This confirmed that continuous processing was possible. Example 3 A sodium sulfonate type membrane was used, which was obtained by hydrolyzing the same perfluoro(3,6-dioxer-4-methyl-7-octensulfonyl fluoride) copolymer film used in Example 1.

即ち実施例1で用いた酸型の膜を0.5規定の食塩水中
に5時間浸潰し、酸性となった溶液を苛性ソーダで中和
して、その中に膜を浸潰したままとして完全にナトリウ
ム型とした。この腰を第1図に示す蒸発箱(開口部約1
0仇×12仇)の中に表1に示す化合物を10夕入れて
装着し、下部より200qoに加熱して20分間で膜面
に蒸着被膜を形成し、次いでこれを鉄板の間にはさんで
表1に示す条件で加熱した。
That is, the acid type membrane used in Example 1 was immersed in 0.5N saline solution for 5 hours, the acidic solution was neutralized with caustic soda, and the membrane was completely immersed in the solution. It was made into a sodium type. This waist is shown in Figure 1 in the evaporation box (opening approx.
The compound shown in Table 1 was placed in a chamber (0x12cm) for 10 nights, heated from the bottom to 200qo to form a vapor deposited film on the film surface for 20 minutes, and then sandwiched between iron plates. It was heated under the conditions shown in Table 1.

その後充分に水洗した後、1.の規定の塩酸中に浸潰し
て平衡にして、1000サイクル交流によって膜の電気
抵抗を測定した。
After washing thoroughly with water, 1. The electrical resistance of the membrane was measured by immersing it in a specified amount of hydrochloric acid to equilibrate it and performing 1000 cycles of alternating current.

即ちスルホン酸ソーダ基が不活性化これた度合を比較し
た。更に膜表面の反射による赤外吸収スペクトルを測定
したところ各々の膜について106位汝のスルホン酸基
に基因する吸収は消失し、それぞれのスルホニルハラィ
ド基に相当する波数に吸収が認められた。
That is, the degree to which the sodium sulfonate group was inactivated was compared. Furthermore, when we measured the infrared absorption spectrum due to reflection on the film surface, it was found that for each film, the absorption based on the sulfonic acid group at position 106 disappeared, and absorption was observed at the wavenumber corresponding to each sulfonyl halide group. .

表1Table 1

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

第1図は本発明における蒸発の一般的手段を示すもので
あり、1はフィルム、2は蒸着函、3は加熱装置である
。 第2図は長尺フィルムを処理する場合の一態様を示すも
のであり4,5,6はそれぞれ加熱ロールである。第3
図は長尺フィルムを連続的に処理する場合の一態様を示
すものであり、7は反応工程、16は加熱装置である。
次Z図が2図 次ろ図
FIG. 1 shows general means for evaporation in the present invention, where 1 is a film, 2 is a vapor deposition box, and 3 is a heating device. FIG. 2 shows one mode of processing a long film, and 4, 5, and 6 are heating rolls, respectively. Third
The figure shows an embodiment in which a long film is continuously processed, where 7 is a reaction step and 16 is a heating device.
Next Z diagram is 2nd diagram

Claims (1)

【特許請求の範囲】 1 側鎖に陽イオン交換基を有し、且つ該イオン交換基
が結合している炭素に少なくとも1ケのフツ素原子を結
合している陽イオン交換能を有するフイルムの少なくと
も一方の表面に、五塩化りん、三臭化りん及び三沃化り
んのうち少なくとも一種のハロゲン化りん化合物を蒸着
せしめた後、これを140°〜180℃に加熱反応させ
て、該フイルムの少なくとも表面に存在する陽イオン交
換基のイオン交換能を失わせることを特徴とするイオン
交換性フイルムの改良方法。 2 イオン交換能を有する長尺フイルムを用い、まずそ
の少なくとも一方の面にハロゲン化りん化合物を蒸着し
、次いで加熱工程に連続的に供給することを特徴とする
特許請求の範囲第1項記載の方法。
[Scope of Claims] 1. A film having cation exchange ability, which has a cation exchange group in its side chain and has at least one fluorine atom bonded to the carbon to which the ion exchange group is bonded. After vapor-depositing at least one type of halogenated phosphorus compound among phosphorus pentachloride, phosphorus tribromide, and phosphorus triiodide on at least one surface, this is reacted by heating at 140° to 180°C to form the film. 1. A method for improving an ion-exchangeable film, the method comprising eliminating the ion-exchange ability of at least the cation-exchange groups present on the surface. 2. The method according to claim 1, characterized in that a long film having ion exchange ability is used, and a halogenated phosphorus compound is first vapor-deposited on at least one surface of the film, and then continuously supplied to a heating step. Method.
JP52089241A 1977-07-27 1977-07-27 Method for improving film with ion exchange ability Expired JPS6026143B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52089241A JPS6026143B2 (en) 1977-07-27 1977-07-27 Method for improving film with ion exchange ability

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52089241A JPS6026143B2 (en) 1977-07-27 1977-07-27 Method for improving film with ion exchange ability

Publications (2)

Publication Number Publication Date
JPS5424284A JPS5424284A (en) 1979-02-23
JPS6026143B2 true JPS6026143B2 (en) 1985-06-21

Family

ID=13965239

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52089241A Expired JPS6026143B2 (en) 1977-07-27 1977-07-27 Method for improving film with ion exchange ability

Country Status (1)

Country Link
JP (1) JPS6026143B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62198626U (en) * 1986-06-06 1987-12-17

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5994271A (en) * 1983-10-31 1984-05-30 Matsushita Electric Ind Co Ltd Cassette tape recorder

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62198626U (en) * 1986-06-06 1987-12-17

Also Published As

Publication number Publication date
JPS5424284A (en) 1979-02-23

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