JPS60235609A - Preparation of ion permselective membrane - Google Patents

Preparation of ion permselective membrane

Info

Publication number
JPS60235609A
JPS60235609A JP9262384A JP9262384A JPS60235609A JP S60235609 A JPS60235609 A JP S60235609A JP 9262384 A JP9262384 A JP 9262384A JP 9262384 A JP9262384 A JP 9262384A JP S60235609 A JPS60235609 A JP S60235609A
Authority
JP
Japan
Prior art keywords
heat
stage
anodized
film
oxide film
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.)
Granted
Application number
JP9262384A
Other languages
Japanese (ja)
Other versions
JPH0419889B2 (en
Inventor
Tetsuo Ishii
哲郎 石井
Masashi Yamashita
雅司 山下
Satoshi Fujioka
智 藤岡
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.)
Nippon Koki Co Ltd
Original Assignee
Nippon Koki 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 Nippon Koki Co Ltd filed Critical Nippon Koki Co Ltd
Priority to JP9262384A priority Critical patent/JPS60235609A/en
Publication of JPS60235609A publication Critical patent/JPS60235609A/en
Publication of JPH0419889B2 publication Critical patent/JPH0419889B2/ja
Granted legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To prepare a membrane capable of permeating cation selectively by a simple method by stripping off an anodized film from an anodized aluminium and heat-treating the film. CONSTITUTION:A cation permselective membrane is prepd. by a process consisting of a stage for anodizing aluminium in an electrolytic bath contg. aq. phosphoric acid added with an org. acid such as citric acid, a stage for stripping off the anodized film by dipping the anodized aluminium in a stripping bath contg. bromomethanol, a stage for heat treating the stripped anodized film by heating it at >=850 deg.C after it is dried, and a stage for diffusing alkali metal by dipping the heat-treated film in aq. caustic alkali and heat-treating again at >=900 deg.C, successively.

Description

【発明の詳細な説明】 C産業上の利用分野) 本発明は、陽イオンのみを選択的に透過させるイオン選
択膜の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application) The present invention relates to a method for producing an ion-selective membrane that selectively transmits only cations.

(従来技術) 近年、特定のイオンのみを選択的に透過させることので
きる物質、pklllll固体電解質の開発が進められ
ており、ナトリウムイオンを選択的に透過させる固体電
解質として、β−アルミナが知られている。ところか、
このβ−アルミナの実用化を図るにあたって、これを薄
膜状に形成することが大きな課題となっているが、未だ
そのようなイオン選択膜をm造する方法として適切なも
のは提案されていない。
(Prior art) In recent years, the development of solid electrolytes, which are substances that can selectively transmit only specific ions, has been progressing, and β-alumina is known as a solid electrolyte that selectively transmits sodium ions. ing. However,
In attempting to put β-alumina into practical use, forming it into a thin film is a major challenge, but no suitable method for manufacturing such an ion-selective membrane has yet been proposed.

(発明の目的) 本発明は、上記の点に鑑みてなされたもので、その目的
は、アルミニウムの陽極酸化皮膜を剥離熱処理するとい
う簡単な方法で陽イオンを選択透過し得るイオン選択膜
を製造せんとすることにある。
(Object of the Invention) The present invention has been made in view of the above points, and its purpose is to produce an ion-selective membrane that can selectively permeate cations by a simple method of heat-treating the anodic oxide film of aluminum. It's about trying.

(発明の構成) 本発明方法は、リン酸水浴液にクエン酸勢の有機酸を添
加してなる電解浴を用いてアルミニウムに陽極酸化処理
を施す陽am化工程と、陽極酸化処理後のアルミニウム
をブロムメタノール溶液からなる剥離浴に浸漬して酸化
皮膜を剥離する剥離工程と、該酸化皮膜を[操後ざ50
℃以上の温度で加熱処理する熱処理工程と、熱処理後の
酸化皮挾掌苛性アルカリ水溶液に浸漬した後り001以
上の温度で再加熱処理を施すアルカリ金属拡散工程とを
順次行なうことによって、陽イオンを選択透過するイオ
ン選択膜を製造することを特徴としている。
(Structure of the Invention) The method of the present invention includes an anodic oxidation process in which aluminum is anodized using an electrolytic bath prepared by adding a citric acid organic acid to a phosphoric acid water bath, and The oxide film is peeled off by immersing it in a stripping bath consisting of a bromine methanol solution;
By sequentially carrying out a heat treatment step in which heat treatment is carried out at a temperature of 0.degree. It is characterized by manufacturing an ion-selective membrane that selectively permeates.

(作用) 本発明方法では、陽極酸化工程にてリン酸浴を用いるこ
とによって膜厚100μm以上の厚い酸化皮膜をアルミ
ニウム表面に形成し、この酸化皮膜を剥離工程にてアル
ミニウム地金から剥離した後、熱処理工程にて耐アルカ
リ性を付与し、酸化皮膜内へアルカリ金属を拡散せしめ
るアルカリ金属拡散工程によって、lイオンを選択透過
するイオン選択膜が得られるのである。
(Function) In the method of the present invention, a thick oxide film with a thickness of 100 μm or more is formed on the aluminum surface by using a phosphoric acid bath in the anodizing process, and after this oxide film is peeled off from the aluminum base metal in the peeling process. An ion-selective membrane that selectively permeates l ions can be obtained by imparting alkali resistance in the heat treatment step and by an alkali metal diffusion step in which the alkali metal is diffused into the oxide film.

($施例) (1)ramm化T3 20 (g/l)’)ン酸水mfeiニ0.3 (g/
l) ’lxン酸を添加してなる電解浴を用いて純アル
ミニウム板(縦3011A1横70闘、厚さ0.3期)
を陽極として60分間直流電解を施す、所謂陽極酸化処
理を行なう。この時の液温は、電解開始時10℃で、電
解終了特約ざ0℃となる如くコントロールし、且つ印加
電圧は電解開始時/20Vで、開始後IIo〜60分の
間で#、OVとなる如くコントロールする。すると、ア
ルミニウム表面に約720μlの膜厚を有する酸化皮膜
が形成される。本工程においては、リン酸浴を用いるこ
とによって生成する酸化皮膜の膜厚を大ならしめるとと
もに、クエン酸の存在によって酸化皮膜の孔径の拡大を
図り、膜厚増大に寄与せしめている。なお、クエン酸に
代えて、他の適当な有機酸を用いてもよいことは勿論で
ある。
($ Example) (1) RAMM T3 20 (g/l)') acid water mfei 0.3 (g/l)
l) Pure aluminum plate (vertical 3011A1 width 70cm, thickness 0.3cm) using an electrolytic bath made by adding acid
A so-called anodic oxidation treatment is performed in which direct current electrolysis is performed for 60 minutes using as an anode. The liquid temperature at this time was controlled so that it was 10℃ at the start of electrolysis and 0℃ at the end of electrolysis, and the applied voltage was 20V at the start of electrolysis, and # and OV between IIo and 60 minutes after the start. Control it as you see fit. Then, an oxide film having a thickness of about 720 μl is formed on the aluminum surface. In this step, the thickness of the oxide film produced is increased by using a phosphoric acid bath, and the pore size of the oxide film is expanded by the presence of citric acid, contributing to the increase in film thickness. Note that, of course, other suitable organic acids may be used in place of citric acid.

(1)剥離工程 前記陽極酸化工程にて酸化皮膜を生成されたアルミニウ
ムを30 W/v 96プロムメタノール溶液からなる
剥離浴に約3日間浸漬し、アルミニウム地金を溶解して
、酸化皮膜(At203を主成分とする)を得る。
(1) Stripping process The aluminum on which the oxide film was formed in the anodizing process was immersed in a stripping bath consisting of a 30 W/v 96 prom methanol solution for about 3 days to dissolve the aluminum base metal and remove the oxide film (At203 ) is obtained.

(1)熱処理工程 前記剥離工程にて剥離生成された酸化皮膜を一度乾燥さ
せ、rso℃以上の温度で7時間加熱して耐アルカリ性
を付与する。
(1) Heat treatment step The oxide film peeled off in the above peeling step is once dried and heated at a temperature of rso° C. or higher for 7 hours to impart alkali resistance.

(W)アルカリ金属拡散工程 前記熱処理工程後の酸化皮膜を20 W/V%苛性ソー
ダ水溶液に数分間浸漬した後、qoo℃以上で7時間加
熱処理して、酸化皮膜内にナトリウムを拡散せしめる。
(W) Alkali metal diffusion step The oxide film after the heat treatment step is immersed in a 20 W/V% caustic soda aqueous solution for several minutes, and then heat treated at qoo°C or higher for 7 hours to diffuse sodium into the oxide film.

上記工程により得られたイオン選択膜は、陽イオンのみ
を選択的に透過させる性質を有している。
The ion-selective membrane obtained through the above steps has the property of selectively allowing only cations to pass therethrough.

本冥施例で得られたイオン選択膜を用いると図法の如き
電油を構成することができる。即ち、イオン選択膜/に
よって画成された二つのM2 、3に0.IN苛性ソー
ダ水浴液と0.7N塩酸水溶液とを収容し、1llll
杢2.3にグラファイト電極1.jを配設する。すると
、苛性ソーダ水溶液側からナトリウムイオン(%cx”
)が塩酸水溶液側へ透過して塩化ナトリウムを生成する
結果、塩酸水浴液側が正電位となる一方、苛性ソーダ水
溶液側が負電位となり、Ii+1電極り、5間に起電力
が生じる。実験によれば、このll池の起電力は0.3
/2 Vであった。但し、故意110(at)、水温3
0′″Cとする。
By using the ion-selective membrane obtained in this example, an electrolyte as shown in the diagram can be constructed. That is, two M2, 3 and 0. Contain IN caustic soda water bath solution and 0.7N hydrochloric acid aqueous solution, 1lllll
Graphite electrode 1. on heather 2.3. Place j. Then, sodium ions (%cx”
) permeates to the hydrochloric acid aqueous solution side and generates sodium chloride, and as a result, the hydrochloric acid aqueous solution side becomes a positive potential, while the caustic soda aqueous solution side becomes a negative potential, and an electromotive force is generated between the Ii+1 and 5 electrodes. According to experiments, the electromotive force of this ll pond is 0.3
/2V. However, intentional 110 (at), water temperature 3
0′″C.

(発明の効果) 軟土の如く、本発明によれば、リーレ酸浴にて得られた
陽極酸化皮膜を剥IIII後、熱処理し、死にアルカリ
金属拡散処理を施すという簡単な製法によって、陽イオ
ンのみを選択的に透過させるイオン選択膜を製造するこ
とができるという優れた効果がある。
(Effects of the Invention) Like soft soil, according to the present invention, cations can be removed by a simple manufacturing method of peeling off the anodic oxide film obtained in a Liele acid bath, followed by heat treatment, and then an alkali metal diffusion treatment. This has the excellent effect of being able to manufacture an ion-selective membrane that selectively permeates only ions.

又、得られたイオン選択膜は、機械的強度を維持するに
十分な膜厚を有しており、実用に十分耐え得るものであ
る。
Moreover, the obtained ion-selective membrane has a sufficient membrane thickness to maintain mechanical strength, and is sufficiently durable for practical use.

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

図面は本発明方法で製造されたイオン選択膜の応用例で
あるgIi池の模式図である。 l・・・・・イオン選択膜
The drawing is a schematic diagram of a gIi pond, which is an application example of the ion-selective membrane produced by the method of the present invention. l...Ion selective membrane

Claims (1)

【特許請求の範囲】[Claims] /、リン酸水浴液にクエン酸等の有機酸を添加してなる
電解浴を用いてアルミニウムに陽極酸化処理を施したも
のを、ブロムメタノール溶液からなる剥離浴に浸漬して
酸化皮膜を剥離した後、該酸化皮膜を乾a後に50℃以
上の温度で加熱処理し、次いで苛性アルカリ水溶液に浸
漬し、更に900 ’C以上の温度で再度加熱処理を施
すことを特徴とするイオン選択膜の製造方法。
/, Aluminum was anodized using an electrolytic bath made by adding an organic acid such as citric acid to a phosphoric acid water bath, and the oxide film was removed by immersing it in a stripping bath made of bromine methanol solution. After that, the oxide film is dried and then heat-treated at a temperature of 50° C. or higher, then immersed in a caustic alkali aqueous solution, and further heat-treated at a temperature of 900° C. or higher. Method.
JP9262384A 1984-05-08 1984-05-08 Preparation of ion permselective membrane Granted JPS60235609A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9262384A JPS60235609A (en) 1984-05-08 1984-05-08 Preparation of ion permselective membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9262384A JPS60235609A (en) 1984-05-08 1984-05-08 Preparation of ion permselective membrane

Publications (2)

Publication Number Publication Date
JPS60235609A true JPS60235609A (en) 1985-11-22
JPH0419889B2 JPH0419889B2 (en) 1992-03-31

Family

ID=14059562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9262384A Granted JPS60235609A (en) 1984-05-08 1984-05-08 Preparation of ion permselective membrane

Country Status (1)

Country Link
JP (1) JPS60235609A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62153161A (en) * 1985-11-29 1987-07-08 ベルンハルト テイ−ル Manufacture of thin formed body made from ceramic and thin film for audiomodifier
JPS62185898A (en) * 1986-02-03 1987-08-14 アルカン・インタ−ナシヨナル・リミテツド Porous anodic oxidation aluminum film and its production

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62153161A (en) * 1985-11-29 1987-07-08 ベルンハルト テイ−ル Manufacture of thin formed body made from ceramic and thin film for audiomodifier
JPS62185898A (en) * 1986-02-03 1987-08-14 アルカン・インタ−ナシヨナル・リミテツド Porous anodic oxidation aluminum film and its production

Also Published As

Publication number Publication date
JPH0419889B2 (en) 1992-03-31

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