JPH108268A - Partition membrane for electrolytic cell used for electrolytic regeneration of chloride-based etching solution - Google Patents

Partition membrane for electrolytic cell used for electrolytic regeneration of chloride-based etching solution

Info

Publication number
JPH108268A
JPH108268A JP16620496A JP16620496A JPH108268A JP H108268 A JPH108268 A JP H108268A JP 16620496 A JP16620496 A JP 16620496A JP 16620496 A JP16620496 A JP 16620496A JP H108268 A JPH108268 A JP H108268A
Authority
JP
Japan
Prior art keywords
film
partition membrane
dried
obtd
diaphragm
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
JP16620496A
Other languages
Japanese (ja)
Inventor
Masaaki Iorizaki
雅章 庵崎
Minoru Origasa
実 折笠
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.)
Nittetsu Mining Co Ltd
Original Assignee
Nittetsu Mining 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 Nittetsu Mining Co Ltd filed Critical Nittetsu Mining Co Ltd
Priority to JP16620496A priority Critical patent/JPH108268A/en
Publication of JPH108268A publication Critical patent/JPH108268A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a partition membrane which does not cause decrease in performance or strength even under rather high temp. condition and can realize improvement in sealing property without increase in voltage by laminating a tetrafluoroethylene resin porous body on a synthetic resin base body. SOLUTION: For example, a tetrafluoroethylene resin (PTFE)/PVAc copolymer is dissolved in methylethylketone to prepare 0.3wt.% soln. A porous PTFE film having 40μm thickness and 80% porosity is impregnated with the soln. thus prepared and then the film is fixed on a frame and dried at 60 deg.C for 5min. This procedure is repeated five times. Then the obtd. film is dipped in ethanol containing sodium methoxide and subjected to heat treatment for 30min. for saponification. The obtd. hydrophilic film is washed with water. Then the hydrophilic porous PTFE film is dipped in 1% methanol soln. for 30sec, taken out, fixed on a frame and dried at room temp. for 1hour. The dried film is laminated on a PP nonwoven fabric base body to obtain a partition membrane. The obtd. partition membrane can be used even under high temp. condition at about >60 deg.C.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、銅やニッケルを含
有する塩化物系エッチング液、例えば銅プリント基板、
半導体リードフレーム、ブラウン管シャドーマスク等の
製造工程で使用されるエッチング液の再生方法に関連
し、特に当該液を電解により再生する際に使用する電解
槽で用いられる隔膜に関するものである。
The present invention relates to a chloride-based etching solution containing copper or nickel, for example, a copper printed circuit board,
The present invention relates to a method for regenerating an etching solution used in a manufacturing process of a semiconductor lead frame, a cathode ray tube shadow mask, and the like, and particularly relates to a diaphragm used in an electrolytic cell used when regenerating the solution by electrolysis.

【0002】[0002]

【従来の技術】本出願人は過去に特開平5−11787
9号公報、特開平6−240475号公報等において、
銅やニッケルを含む塩化物系エッチング液の電解再生方
法を提案しているが、それら電解再生方法で使用する隔
膜電解槽の隔膜が備えるべき条件は、できるかぎり電
気抵抗が小さくて電圧上昇を極力抑えることができ、
陰極液、陽極液の混合を防ぐべく気密性が高く、耐薬
品性、とりわけ耐塩素化性に優れ、膜自体が電気的に
中性、即ち、極性を持たないことである。
2. Description of the Related Art The applicant of the present invention has disclosed in Japanese Patent Application Laid-Open No. HEI 5-11787.
No. 9, JP-A-6-240475, etc.
Electrolytic regeneration methods for chloride-based etchants containing copper and nickel have been proposed, but the conditions for the diaphragm of the diaphragm electrolyzer used in these electrolytic regeneration methods should be as low as possible, and the voltage rise should be as small as possible. Can be suppressed,
In order to prevent mixing of the catholyte and the anolyte, the airtightness is high, the chemical resistance is excellent, especially the chlorination resistance, and the film itself is electrically neutral, that is, has no polarity.

【0003】そして、上記公報においてこれら条件を満
たすものとして選定された隔膜は、モドアクリルやポリ
エステル等の合成樹脂製の濾過布であり、安価で、60
℃以下の温度であれば十分に実用に耐えるものである。
The diaphragm selected to satisfy these conditions in the above-mentioned publication is a filter cloth made of synthetic resin such as modacrylic or polyester, and is inexpensive.
If the temperature is lower than ℃, it is sufficient for practical use.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このよ
うな合成樹脂性の濾過布は、60℃を越える高温での使
用については耐久性の点で問題があり、また気密性を一
段と高めようとすると、その編み目を詰ませたり、厚み
を増す必要があり、その結果、電圧上昇を伴うこととな
る。
However, such a synthetic resin filter cloth has a problem in terms of durability when used at a high temperature exceeding 60 ° C., and if the airtightness is to be further enhanced, It is necessary to close the stitches or increase the thickness, which results in an increase in voltage.

【0005】そこで本発明は、銅やニッケルを含有する
塩化物系エッチング液の電解再生の実施のための電解槽
に使用されるべき隔膜にして、60℃以上の高温下にお
いても性能低下や強度低下がなく、しかも電圧上昇を伴
うことなく気密性の改善を実現する隔膜を提供すること
を課題とする。
Therefore, the present invention provides a diaphragm to be used in an electrolytic cell for carrying out electrolytic regeneration of a chloride-based etching solution containing copper or nickel, and has a performance degradation and strength even at a high temperature of 60 ° C. or more. It is an object of the present invention to provide a diaphragm that does not decrease and that improves airtightness without increasing a voltage.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を、合
成樹脂基材に4フッ化エチレン樹脂(PTFE)の多孔
質体を積層して隔膜を形成することによって、解決し
た。合成樹脂基材にPTFE多孔質体を積層させる方法
としては、従来公知の方法、例えば、PTFE塗布液を
基材表面に塗布乾燥する方法や、予め形成したPTFE
膜を基材表面にラミネートする方法、PTFE塗布膜を
基材の多孔質構造内に含浸させる方法等が挙げられる。
The object of the present invention has been achieved by forming a diaphragm by laminating a porous body of tetrafluoroethylene resin (PTFE) on a synthetic resin base material. As a method of laminating the PTFE porous body on the synthetic resin substrate, a conventionally known method, for example, a method of applying a PTFE coating solution on the surface of the substrate and drying the same, and a method of laminating PTFE formed in advance.
A method of laminating the film on the surface of the substrate, a method of impregnating the porous structure of the substrate with the PTFE coating film, and the like can be given.

【0007】その際、合成樹脂基材として、ポリエステ
ル、ポリプロピレン、ポリ塩化ビニル、ポリ塩化ビニリ
デン、モドアクリル、アクリル、ポリエチレン、ポリサ
ルフォン、4フッ化エチレン、2フッ化ビニリデン等、
塩酸及び酸化剤に耐えうる樹脂製のネット、不織布、織
布が使用できる。ここでネットとは、合成樹脂を一体成
形して作る網状のもので、格子の形は丸状、ハニカム
状、スクエア状等、どうのようになっていてもよく、特
に制限されない。使用に適する機械的強度が必要である
が、厚みは特に50〜1000μmの範囲でできるだけ
薄い方が電気抵抗が少なくなって好ましい。基材が不織
布である場合には、織布やネットの基材に比べて、より
薄い厚みで機械的強度が十分な隔膜を得ることができ、
より一層好ましい。
At that time, as a synthetic resin substrate, polyester, polypropylene, polyvinyl chloride, polyvinylidene chloride, modacrylic, acrylic, polyethylene, polysulfone, tetrafluoroethylene, vinylidene difluoride, etc.
Resin nets, nonwoven fabrics and woven fabrics that can withstand hydrochloric acid and oxidizing agents can be used. Here, the net is a net formed by integrally molding a synthetic resin, and the shape of the lattice may be any shape such as a round shape, a honeycomb shape, and a square shape, and is not particularly limited. Although mechanical strength suitable for use is required, it is preferable that the thickness be as thin as possible in the range of 50 to 1000 μm, because the electric resistance is reduced. When the base material is a non-woven fabric, compared to the base material of a woven fabric or a net, it is possible to obtain a diaphragm having a smaller thickness and sufficient mechanical strength,
Even more preferred.

【0008】また、膜の気密性の目安となる透水量は、
差圧2kg/cm2Gにおいて0.5ml/cm2・秒以
下とすることが、電流効率を上げることができて好まし
い。
[0008] The amount of water permeability, which is a measure of the airtightness of the membrane, is:
At a differential pressure of 2 kg / cm 2 G, the pressure is preferably 0.5 ml / cm 2 · second or less, because current efficiency can be increased.

【0009】電解処理での使用の際、隔膜における陽極
液に接する面は、塩素ガス等の強い酸化力に耐えうる必
要があり、一方、陰極液に接する面は、帯電や陰極で析
出した金属粒子の付着による当該面への金属析出を防ぐ
必要があるが、隔膜の両面にPTFE多孔質体を積層す
ることで、これらの条件を満たすことができる。
When used in electrolytic treatment, the surface of the diaphragm that contacts the anolyte must be able to withstand strong oxidizing power such as chlorine gas, while the surface that contacts the catholyte is charged or charged by the metal deposited on the cathode. Although it is necessary to prevent metal deposition on the surface due to adhesion of particles, these conditions can be satisfied by laminating a PTFE porous body on both surfaces of the diaphragm.

【0010】[0010]

【実施例】以下に、本発明の詳細を、実施例に基づい
て、説明する。 (隔膜の製造)4フッ化エチレン/酢酸ビニルコポリマ
ーをメチルエチルケトンに溶かし、0.3重量%溶液に
調製した。厚さ40μm、空孔率80%の多孔質PTF
E膜を上記溶液で含浸した後、枠に固定し、60℃で5
分間乾燥した。同様な工程を5回繰り返した。得られた
膜をナトリウムメトキシド含有エタノール中に浸漬して
30分間加熱処理してケン化処理した親水性膜を水洗し
た。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The details of the present invention will be described below based on embodiments. (Production of diaphragm) A tetrafluoroethylene / vinyl acetate copolymer was dissolved in methyl ethyl ketone to prepare a 0.3% by weight solution. Porous PTF having a thickness of 40 μm and a porosity of 80%
After impregnating the E film with the above solution, it was fixed on a frame, and
Dried for minutes. The same process was repeated five times. The obtained membrane was immersed in ethanol containing sodium methoxide and heated for 30 minutes to wash the saponified hydrophilic membrane with water.

【0011】この親水性の多孔質PTFE膜を1%メタ
ノール溶液中に30秒間浸漬し、取り出してから枠に固
定した後、室温で1時間乾燥した。基材としてポリプロ
ピレン不織布を用い、上記乾燥膜をラミネートして、隔
膜を作製した(厚み100μm、孔径0.5μm)。そ
の性状を調べたところ、差圧2kg/cm2Gで0.2
ml/cm2・秒の透水量を示した。
The hydrophilic porous PTFE membrane was immersed in a 1% methanol solution for 30 seconds, taken out, fixed on a frame, and dried at room temperature for 1 hour. Using a polypropylene nonwoven fabric as a base material, the above-mentioned dried film was laminated to prepare a diaphragm (thickness: 100 μm, pore size: 0.5 μm). Examination of its properties revealed that the differential pressure was 0.2 kg / cm 2 G at 0.2 kg / cm 2 G.
The amount of water permeation of ml / cm 2 · sec was shown.

【0012】(電解処理)上記のように作製された隔膜
を備えた電解槽を用いて、塩化銅溶液をバッチ方式によ
り電解処理した。原液組成は、2価銅23g/l、塩素
105g/lで、この液1100mlを電解槽に満たし
た。隔膜で仕切られた陰極室側の陰極板は、チタンのエ
キスパンドメタルを用い、陽極板としてはRuO2/T
i(DSA、所謂寸法安定アノード)のエキスパンドメ
タルを用いた。幾何面積基準の電流密度は125mA/
cm2、全電流10Aで電解した。通電時間は30分間
とし、電解後の液は、陰極液、陽極液を混合して組成を
分析した。結果は以下の通りである。
(Electrolytic Treatment) Using the electrolytic cell provided with the diaphragm prepared as described above, a copper chloride solution was subjected to electrolytic treatment by a batch method. The composition of the stock solution was 23 g / l of divalent copper and 105 g / l of chlorine, and 1100 ml of this solution was filled in an electrolytic cell. The cathode plate on the cathode chamber side partitioned by a diaphragm uses expanded metal of titanium, and the anode plate is RuO 2 / T.
i (DSA, so-called dimensionally stable anode) expanded metal was used. The current density based on the geometric area is 125 mA /
Electrolysis was performed at a total current of 10 A in cm 2 . The energization time was 30 minutes, and the composition after the electrolysis was analyzed by mixing a catholyte and an anolyte. The results are as follows.

【0013】[0013]

【表1】 [Table 1]

【0014】[0014]

【発明の効果】本発明に係る隔膜を使用することによっ
て、低電圧で且つ高い電流効率をもって電解が可能とな
り、電解装置を小型化することができることとなる。即
ち、電流効率が上がることで、電源容量を下げることが
でき、電極面積を縮小できる。それに伴い、ランニング
コストの低減化も引き出すことが可能となった。
By using the diaphragm according to the present invention, electrolysis can be performed with low voltage and high current efficiency, and the size of the electrolysis apparatus can be reduced. That is, by increasing the current efficiency, the power supply capacity can be reduced, and the electrode area can be reduced. Along with this, it has become possible to bring out a reduction in running costs.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 合成樹脂基材にPTFE多孔質体を積層
してなる、エッチング液再生に用いられる電解槽用の隔
膜。
1. A diaphragm for an electrolytic cell used for regenerating an etchant, comprising a PTFE porous body laminated on a synthetic resin base material.
【請求項2】 前記基材が、ポリエステル、ポリプロピ
レン、ポリ塩化ビニル、ポリ塩化ビニリデン、モドアク
リル、アクリル、ポリエチレン、ポリサルフォン、4フ
ッ化エチレン、2フッ化ビニリデンの群から選択された
少なくとも1種の合成樹脂からなることを特徴とする請
求項1に記載の隔膜。
2. The method according to claim 1, wherein the substrate is at least one selected from the group consisting of polyester, polypropylene, polyvinyl chloride, polyvinylidene chloride, modacrylic, acrylic, polyethylene, polysulfone, tetrafluoroethylene, and vinylidene fluoride. The diaphragm according to claim 1, comprising a resin.
【請求項3】 前記合成樹脂基材を不織布から構成し、
その両面にPTFE多孔質体を積層することを特徴とす
る請求項1又は請求項2に記載の隔膜。
3. The synthetic resin substrate is made of a nonwoven fabric,
The diaphragm according to claim 1 or 2, wherein a porous PTFE body is laminated on both surfaces thereof.
【請求項4】 透水量が差圧2kg/cm2Gで0.5
ml/cm2・秒以下であることを特徴とする請求項1
〜3のいずれか一項に記載の隔膜。
4. The water permeability is 0.5 at a differential pressure of 2 kg / cm 2 G.
2. The flow rate is not more than ml / cm 2 · second.
The diaphragm according to any one of claims 3 to 3.
JP16620496A 1996-06-26 1996-06-26 Partition membrane for electrolytic cell used for electrolytic regeneration of chloride-based etching solution Pending JPH108268A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16620496A JPH108268A (en) 1996-06-26 1996-06-26 Partition membrane for electrolytic cell used for electrolytic regeneration of chloride-based etching solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16620496A JPH108268A (en) 1996-06-26 1996-06-26 Partition membrane for electrolytic cell used for electrolytic regeneration of chloride-based etching solution

Publications (1)

Publication Number Publication Date
JPH108268A true JPH108268A (en) 1998-01-13

Family

ID=15827028

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16620496A Pending JPH108268A (en) 1996-06-26 1996-06-26 Partition membrane for electrolytic cell used for electrolytic regeneration of chloride-based etching solution

Country Status (1)

Country Link
JP (1) JPH108268A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8882972B2 (en) 2011-07-19 2014-11-11 Ecolab Usa Inc Support of ion exchange membranes

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8882972B2 (en) 2011-07-19 2014-11-11 Ecolab Usa Inc Support of ion exchange membranes

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