JPS62121733A - Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride - Google Patents

Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride

Info

Publication number
JPS62121733A
JPS62121733A JP26144185A JP26144185A JPS62121733A JP S62121733 A JPS62121733 A JP S62121733A JP 26144185 A JP26144185 A JP 26144185A JP 26144185 A JP26144185 A JP 26144185A JP S62121733 A JPS62121733 A JP S62121733A
Authority
JP
Japan
Prior art keywords
membrane
exchange membrane
cation exchange
pinholes
electrolysis
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
JP26144185A
Other languages
Japanese (ja)
Inventor
Kiyotaka Arai
清隆 新井
Junjiro Iwamoto
岩元 純治郎
Koji Suzuki
公二 鈴木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
AGC Inc
Original Assignee
Asahi Glass Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP26144185A priority Critical patent/JPS62121733A/en
Publication of JPS62121733A publication Critical patent/JPS62121733A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

PURPOSE:To detect simply a pinhole or the like in a fluororesin cation exchange membrane for use in electrolysis of an alkali chloride, by applying an anionic surfactant solution to the ion exchange membrane, adjusting the pressure on one side of the membrane to be larger than that on the other side of the membrane and detecting the formation of bubbles. CONSTITUTION:An anionic surfactant solution is applied by, for example, coating or spraying, to a fluororesin cation exchange membrane for use in electrolysis of an alkali chloride (e.g., a cationic membrane comprising a perfluorocarbon polymer). Suitable examples of the anionic surfactants include sodium oleate, ammonium perfluorooctanoate and ammonium perfluorooctanesulfonate. Its concentration is suitably 0.001-5wt%. The pressure on one side of the cation exchange membrane is adjusted to be larger than that on the other side, and pinholes or the like are detected by bubbles resulting from a gas passing through the pinholes or the like present in the membrane.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、塩化アルカリを電解して水酸化アルカリを製
造するのに用いられる含フッ素樹脂陽イオン交換膜のピ
ンホール等の検出方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for detecting pinholes, etc. in a fluorine-containing resin cation exchange membrane used to produce alkali hydroxide by electrolyzing alkali chloride. It is.

[従来の技術] 塩化アルカリ水溶液の電解に使用される含フッ素樹脂陽
イオン交換膜にピンホール、クラック等(以下ピンホー
ル等という)が発生すると電流効率の低下及び苛性アル
カリ土類金属低下のような性能低下が生ずる。ピンホー
ル等の傷の補修方法としては種々の方法が提案されてい
るが(例えば特開昭58−70863号、58−370
29号公開公報参照)ピンホール等(特にピンホール等
が袋状や円筒状の形状を有するイオン交換膜に発生した
場合)を洩れなく検出する効果的方法が知られていなか
った。
[Prior art] When pinholes, cracks, etc. (hereinafter referred to as pinholes, etc.) occur in the fluorine-containing resin cation exchange membrane used for electrolysis of aqueous alkali chloride solutions, current efficiency decreases and caustic alkaline earth metal decreases. This results in severe performance deterioration. Various methods have been proposed for repairing scratches such as pinholes (for example, Japanese Patent Laid-Open Nos. 58-70863 and 58-370).
(See Publication No. 29) No effective method has been known to detect pinholes (especially when pinholes occur in an ion exchange membrane having a bag-like or cylindrical shape) without leaking.

本発明者は、界面活性剤溶液をイオン交換膜表面に付与
し、該膜の一方の面の気圧を他方の面の気圧より大なら
しめ、該膜に存在するピンホール等を通過する気体によ
り発生する気泡を利用することによりピンホール等を完
全に且つ容易に検出しうろことを見出したが、この方法
の場合、次の難点を有する。
The present inventor applied a surfactant solution to the surface of an ion-exchange membrane, made the pressure on one side of the membrane higher than the pressure on the other side, and caused the gas to pass through pinholes etc. present in the membrane. It has been found that pinholes and the like can be completely and easily detected by utilizing the generated air bubbles, but this method has the following drawbacks.

即ち、含フッ素樹脂陽イオン交換膜の種類或は界面活性
剤の種類によっては、界面活性剤が・cオン交換膜に吸
着されて、イオン交換膜を塩化アルカリの電解に使用し
た電解槽の摺電圧がL昇したり電流効率が低下する等、
性能低下が生ずることがあり、性能回復のため、イオン
交換膜を長時間水洗いしたり特殊処理を必要とすること
があった。
In other words, depending on the type of fluorine-containing resin cation exchange membrane or the type of surfactant, the surfactant may be adsorbed on the C ion exchange membrane, and the ion exchange membrane may be used to electrolyze alkali chloride. Voltage increases by L, current efficiency decreases, etc.
Performance may deteriorate, and in order to restore performance, the ion exchange membrane may need to be washed with water for a long time or special treatment may be required.

[発明が解決しようとする問題点] 本発明は、従来技術が有していた前述の欠点を解消する
ことを目的とするものである。
[Problems to be Solved by the Invention] The present invention aims to eliminate the above-mentioned drawbacks of the prior art.

し問題点を解決するための手段] 本発明は、前述の問題点を解決すべくなされたものであ
り、塩化アルカリ電解用含フッ素樹脂陽イオン交換膜に
アニオン系界面活性剤溶液を付与し、該膜の一方の面の
気圧を他方の面の気圧より大ならしめ、該膜に存在する
ピンホール等を通過する気体に起因して発生する気泡に
よりピンホール等を検出することを特徴とするピンホー
ル等の検出方法を提供するものである。
Means for Solving the Problems] The present invention has been made to solve the above-mentioned problems, and includes applying an anionic surfactant solution to a fluorine-containing resin cation exchange membrane for alkali chloride electrolysis, The method is characterized in that the air pressure on one side of the membrane is made higher than the air pressure on the other side, and pinholes, etc., are detected by bubbles generated due to gas passing through the pinholes, etc., present in the membrane. This provides a method for detecting pinholes, etc.

次に本発明を更に具体的に説明する。Next, the present invention will be explained in more detail.

本発明においてアニオン系界面活性剤としては一般式R
−X、(こ−に R:好ましくは05以上、更に好まし
くはC1以上のアルキル基又if −y o O7/l
/ * /l/基、X : −(00M、 −303M
In the present invention, the anionic surfactant has the general formula R
-X, (here R: preferably an alkyl group of 05 or more, more preferably C1 or more, or if -y o O7/l
/ * /l/ group, X: -(00M, -303M
.

−0S03 M 、 −0P03 M2 、又は−PO
3M2基、M:アルカリ金属又はNH4)で表わされる
化合物が好適に使用できる。
-0S03 M, -0P03 M2, or -PO
A compound represented by 3M2 group, M: alkali metal or NH4) can be preferably used.

Rとしては炭素数5以トのアルキル基及びフロロアルキ
ル基が適当であり、好ましくはオレイン酸塩、パーフル
十ロオクタン酸塩、パーフルオロオクタスルフォン酸塩
、ナトリウム・ラウリルサフェート、ドデシルベンゼン
スルホン酸1′!!等が特に好適に使用できる。
As R, an alkyl group having 5 or more carbon atoms and a fluoroalkyl group are suitable, and preferably oleate, perfluorooctanoate, perfluorooctasulfonate, sodium lauryl sulfate, dodecylbenzenesulfonic acid 1 ′! ! etc. can be used particularly preferably.

界面活性剤溶液の濃度としては好ましくは0.001〜
5fff量%、特には0.O1〜1重量%程度が適当で
ある。7M度があまり小さいと起泡性が充分でなく、濃
度をあまり大きくしても実益がなく、却って溶液粘度が
高く取扱い性が悪くなる。
The concentration of the surfactant solution is preferably 0.001~
5fff amount%, especially 0. Approximately 1 to 1% by weight of O is suitable. If the 7M degree is too low, the foaming properties will not be sufficient, and there is no practical benefit even if the concentration is increased too much.On the contrary, the solution viscosity will be high and the handling properties will be poor.

本発明に使用される含フッ素樹脂陽イオン交換膜として
は特に限定はないがパーフロロカーボンポリマーよりな
りイオン交換基としては、カルボン酸、スルホン酸、リ
ン酸、等を有するカチン交換膜の場合特に有効である。
The fluorine-containing resin cation exchange membrane used in the present invention is not particularly limited, but it is particularly effective in the case of a cathine exchange membrane made of perfluorocarbon polymer and having ion exchange groups such as carboxylic acid, sulfonic acid, phosphoric acid, etc. It is.

これらの膜はフィルム状及び成形加工して袋状で用いら
れる。特に好ましくは、カルボン酸基を有するパーフロ
ロカーボンポリマーからなるイオン交換膜が用いられ、
特に隔膜法のアスベストをイオン交換膜に交換した、イ
オン交換膜電解システムにおいては膜は袋状に加工して
用いられる。
These membranes are used in the form of films or molded bags. Particularly preferably, an ion exchange membrane made of a perfluorocarbon polymer having carboxylic acid groups is used,
In particular, in an ion exchange membrane electrolysis system in which asbestos in the diaphragm method is replaced with an ion exchange membrane, the membrane is processed into a bag shape.

含フッ素樹脂陽イオン交換膜の表面にアニオン系界面活
性剤溶液(以下単に”溶液”という)を塗布、スプレー
等の方法により付与する。或は”溶液”中にイオン交換
膜を浸漬することにより ”溶液”を付与することもで
きる。
An anionic surfactant solution (hereinafter simply referred to as "solution") is applied to the surface of the fluororesin cation exchange membrane by coating, spraying, or the like. Alternatively, the "solution" can also be applied by immersing the ion exchange membrane in the "solution".

次いで、イオン交換膜の一方の表面の気圧を他方の表面
の気圧より大ならしめる。
Next, the air pressure on one surface of the ion exchange membrane is made greater than the air pressure on the other surface.

具体的には、イオン交換膜が袋状の場合、袋の内部へ空
気を吹込み圧力を大気圧により大ならしめる。或はイオ
ン交換膜を、上面を解放した箱体の該上面に、(”溶液
”を付与した面が上向きとなるように)気密に係合せし
め、箱体の内部の圧力を大ならしめる。圧力差は1〜1
000100O好ましくは10〜1100mm1(程度
が適当である。ピンホール等を通過する気体に起因して
発生する気泡により、目視でピンホールを洩れなく、且
つ容易に検出できる。
Specifically, when the ion exchange membrane is bag-shaped, air is blown into the bag to increase the pressure to atmospheric pressure. Alternatively, the ion exchange membrane is airtightly engaged with the top surface of the box with the top open (with the side to which the "solution" has been applied facing upward) to increase the pressure inside the box. The pressure difference is 1-1
000100O, preferably 10 to 1100 mm1 (approximately 10 to 1100 mm1). Due to the bubbles generated due to the gas passing through the pinhole etc., the pinhole can be visually detected without leakage and easily.

[作用1 アニオン系界面活性剤は、塩化アルカリ電解用含フッ素
樹脂陽イオン交換膜にほとんど或は全く吸着されず、或
は吸着されてもイオン交換膜の性能に影響を与えないも
のと思われる。この傾向はパーフルオロカーボンポリマ
ーよりなる陽イオン交換膜の場合特に著しい。
[Effect 1 It seems that anionic surfactants are hardly or not adsorbed at all on fluorine-containing resin cation exchange membranes for alkali chloride electrolysis, or even if they are adsorbed, they do not affect the performance of the ion exchange membranes. . This tendency is particularly remarkable in the case of cation exchange membranes made of perfluorocarbon polymers.

[実施例] 実施例I CF2 = CF2 と CF2 = CFO(CF2
hGOOclbの共重合体でイオン交換容量(AR)が
1.2鳳eq/gと1.8meq/gである2種のポリ
マーを夫々50JLと200ルの厚みのフィルムとし、
この2枚のフィルムを積層して陽イオン交換膜を得た。
[Example] Example I CF2 = CF2 and CF2 = CFO(CF2
Two types of hGOOclb copolymers with ion exchange capacities (AR) of 1.2 meq/g and 1.8 meq/g were made into films with a thickness of 50 JL and 200 JL, respectively.
These two films were laminated to obtain a cation exchange membrane.

この膜を加水分解処理した後AR1,2meq/g側を
陰極側として電槽に組み込み食塩電解を行なった。電流
効率が初期96%から85%に低下したので解体してピ
ンホール検査を行なった。
After this membrane was hydrolyzed, it was placed in a battery tank with the AR1,2 meq/g side as the cathode side, and salt electrolysis was performed. Since the current efficiency decreased from the initial 96% to 85%, it was dismantled and a pinhole inspection was performed.

膜を箱状の枠に気密に組み込み片側より50鵬農Hgの
加圧ガスを導入し、反対側の面にオレイン酸ソーダの0
.1%水溶液を塗布したところ気泡の発生がおこりピン
ホールが検出された。このピンホールへイオン交換膜フ
ィルムをカバーし熱圧着して補修した後再度同様にピン
ホール検査を行なったがピンホールは検出されなかった
。この膜を再度食塩電解に用いたところ、電流効率は9
6%となり摺電圧は3.Ovの正常値を示した。
The membrane was airtightly assembled in a box-shaped frame, and pressurized gas of 50 Hg was introduced from one side, and 0% of sodium oleate was introduced to the other side.
.. When a 1% aqueous solution was applied, bubbles were generated and pinholes were detected. After repairing this pinhole by covering it with an ion exchange membrane film and bonding it under heat, a pinhole inspection was conducted again in the same manner, but no pinholes were detected. When this membrane was used again for salt electrolysis, the current efficiency was 9.
6% and the sliding voltage is 3. It showed a normal value of Ov.

比較例1 実施例1において界面活性剤としてノニオン系界面活性
剤であるポリオキシエチレン・ノニルフェニルエーテル
を用いた他は同様に行なったところ、ピンホール補修後
の膜性能は電流効率88%であり、摺電圧は3.3■で
あった。
Comparative Example 1 The same procedure as in Example 1 was carried out except that polyoxyethylene nonylphenyl ether, which is a nonionic surfactant, was used as the surfactant.The membrane performance after pinhole repair was 88% in current efficiency. , the sliding voltage was 3.3■.

実施例2 実施例1において界面活性剤としてパー2ルオロオクタ
ン酸アンモニウムを用いた他は同様に行なったところ、
ピンホール補修後の膜性部は′ii流効率96%で摺電
圧は3.OVであった。
Example 2 The same procedure as in Example 1 was performed except that ammonium per-2-fluorooctanoate was used as the surfactant.
After pinhole repair, the membrane part had a current efficiency of 96% and a sliding voltage of 3. It was OV.

比較例2 実施例1において界面活性剤としてカチオン系界面活性
剤のn−オクタデジルアミン塩酸塩を用いる他は同様に
行なったところピンホール補修後の膜性能は電流効率8
0%と低く摺電圧は3.5vと高かった。
Comparative Example 2 The same procedure as in Example 1 was carried out except that the cationic surfactant n-octadecylamine hydrochloride was used as the surfactant. The film performance after pinhole repair was 8 in current efficiency.
The sliding voltage was as low as 0% and as high as 3.5V.

実施例3 実施例1において界面活性剤としてパーフルオロオクタ
ンスルホン酸アンモニウムを用いた他は同様に行なった
ところピンホール補修後の膜性源は電流効率96%で摺
電圧は3.OVであった。
Example 3 The same procedure as in Example 1 was carried out except that ammonium perfluorooctane sulfonate was used as the surfactant. After repairing the pinholes, the membrane source had a current efficiency of 96% and a sliding voltage of 3. It was OV.

[発明の効果] 本発明の方法によるときはピンホール等を簡単に、且つ
洩れなく検出でき、しかもピンホール検出後イオン交換
膜を水洗いしたり、後処理したりする必要がない。
[Effects of the Invention] When using the method of the present invention, pinholes and the like can be detected easily and without leakage, and there is no need to wash the ion exchange membrane with water or perform post-treatment after pinhole detection.

Claims (4)

【特許請求の範囲】[Claims] (1)塩化アルカリ電解用含フッ素樹脂陽イオン交換膜
にアニオン系界面活性剤溶液を付与 し、該膜の一方の面の気圧を他方の面の気圧より大なら
しめ、該膜に存在するピンホール等を通過する気体に起
因して発生する気泡によりピンホール等を検出すること
を特徴とするピンホール等の検出方法。
(1) Apply an anionic surfactant solution to a fluorine-containing resin cation exchange membrane for alkali chloride electrolysis, make the pressure on one side of the membrane greater than the pressure on the other side, and remove the pins present in the membrane. A method for detecting pinholes, etc., characterized in that the pinholes, etc. are detected by bubbles generated due to gas passing through the holes, etc.
(2)アニオン系界面活性剤は一般式R−Xで表わされ
る化合物であることを特徴とする特許請求の範囲第1項
記載のピンホール等の検出方法。 R:C_5以上のアルキル基又はフロロアルキル基 X:−COOM、−SO_3M、−OSO_3M、−P
O_3M_2、又はOPO_3M_2 M:アルカリ金属又はNH_4
(2) The method for detecting pinholes and the like according to claim 1, wherein the anionic surfactant is a compound represented by the general formula R-X. R: C_5 or more alkyl group or fluoroalkyl group X: -COOM, -SO_3M, -OSO_3M, -P
O_3M_2, or OPO_3M_2 M: Alkali metal or NH_4
(3)アニオン系界面活性剤溶液の濃度は0.001〜
5重量%であることを特徴とする特許請求の範囲第2項
、又は第3項記載のピンホール等の検出方法。
(3) The concentration of anionic surfactant solution is 0.001~
The method for detecting pinholes, etc. according to claim 2 or 3, characterized in that the amount is 5% by weight.
(4)含フッ素樹脂陽イオン交換膜がパーフルオロカー
ボンポリマーよりなるカチオン膜であることを特徴とす
る特許請求の範囲第1項乃至第3項記載のピンホール等
の検出方法。
(4) The method for detecting pinholes and the like according to claims 1 to 3, wherein the fluorine-containing resin cation exchange membrane is a cation membrane made of perfluorocarbon polymer.
JP26144185A 1985-11-22 1985-11-22 Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride Pending JPS62121733A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26144185A JPS62121733A (en) 1985-11-22 1985-11-22 Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26144185A JPS62121733A (en) 1985-11-22 1985-11-22 Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride

Publications (1)

Publication Number Publication Date
JPS62121733A true JPS62121733A (en) 1987-06-03

Family

ID=17361934

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26144185A Pending JPS62121733A (en) 1985-11-22 1985-11-22 Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride

Country Status (1)

Country Link
JP (1) JPS62121733A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5030616A (en) * 1987-07-28 1991-07-09 Sumitomo Electric Industries, Ltd. Method for producing an elongated sintered article

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5030616A (en) * 1987-07-28 1991-07-09 Sumitomo Electric Industries, Ltd. Method for producing an elongated sintered article

Similar Documents

Publication Publication Date Title
GB1497749A (en) Process for the electrolysis of sodium chloride
CA1072057A (en) Electrolytic cell membrane conditioning
JPS63297406A (en) Sulfonic fluoro polymer with low equivalent weight
JPS5858365B2 (en) Manufacturing method of cation exchange membrane
US4168216A (en) Heat-treated fluorocarbon sulfonamide cation exchange membrane and process therefor
JPS5833886B2 (en) Cation exchange membrane and its manufacturing method
CA1208867A (en) Method of regenerating cation exchange membrane
JPS62121733A (en) Detection of pinhole or the like in fluororesin cation exchange membrane for electrolysis of alkali chloride
CA1185922A (en) Electrolytic cell ion-exchange membranes
US4030988A (en) Process for producing halogen and metal hydroxides with cation exchange membranes of improved permselectivity
JPS63312301A (en) Hydrolysis of fluorine-based ion-exchange polymer membrane
US4051002A (en) Electrodialysis for aqueous solution of base
GB2052382A (en) A process for joining fluorinated polymer cation exchange membrane
US4026783A (en) Electrolysis cell using cation exchange membranes of improved permselectivity
CA1145236A (en) Process for fusion bonding of fluorocarbon type polymers
US4217198A (en) Coated perfluorosulfonic acid resin membranes and a method for their preparation
US4172931A (en) Welding of membranes of fluorinated polymers
CN106268984A (en) A kind of renovation process of the cation exchange membrane of the polyethyleneimine-modified of inefficacy
JPS6018692B2 (en) Composite membrane manufacturing method
GB2040222A (en) A method for joining a fluorinated polymer film and a fluorinated polymer cation exchange membrane
JPS6116291B2 (en)
JPS5939452B2 (en) Treatment method for cation exchanger
PH11928A (en) Apparatus for electrolysis of alkali metal halide brines
US4246353A (en) Melt processing of fluorinated polymers
GB2040803A (en) A method for joining fluorinated polymer cation exchange membranes