JPH0633482B2 - Method for manufacturing anode material - Google Patents

Method for manufacturing anode material

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Publication number
JPH0633482B2
JPH0633482B2 JP63330535A JP33053588A JPH0633482B2 JP H0633482 B2 JPH0633482 B2 JP H0633482B2 JP 63330535 A JP63330535 A JP 63330535A JP 33053588 A JP33053588 A JP 33053588A JP H0633482 B2 JPH0633482 B2 JP H0633482B2
Authority
JP
Japan
Prior art keywords
anode material
anode
titanium
nickel
current density
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 - Lifetime
Application number
JP63330535A
Other languages
Japanese (ja)
Other versions
JPH02175891A (en
Inventor
千博 滝
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.)
Eneos Corp
Original Assignee
Nippon 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 Nippon Mining Co Ltd filed Critical Nippon Mining Co Ltd
Priority to JP63330535A priority Critical patent/JPH0633482B2/en
Publication of JPH02175891A publication Critical patent/JPH02175891A/en
Publication of JPH0633482B2 publication Critical patent/JPH0633482B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アノード用材料、特に電解二酸化マンガン製
造用アノード材料、またはメッキ用、電気分解用アノー
ド材料の製造方法に関する。
Description: TECHNICAL FIELD The present invention relates to a method for producing an anode material, particularly an anode material for producing electrolytic manganese dioxide, or an anode material for plating and electrolysis.

〔従来の技術〕[Conventional technology]

電解二酸化マンガンは、主に乾電池の活物質として使用
されるが、この二酸化マンガンは一般には硫酸マンガン
0.5〜1.0mol/、遊離硫酸濃度0.2〜0.6mol/よりな
る硫酸・硫酸マンガン水溶液の電解により製造されてい
る。
Electrolytic manganese dioxide is mainly used as an active material for dry batteries, and this manganese dioxide is generally used as manganese sulfate.
It is produced by electrolysis of a sulfuric acid / manganese sulfate aqueous solution having a concentration of 0.5 to 1.0 mol / and a free sulfuric acid concentration of 0.2 to 0.6 mol /.

すなわち、上記水溶液を0.8A/dm2前後の直流にて電解
することにより、陽極に二酸化マンガンを析出させ、こ
れがある程度蓄積した段階で剥離し二酸化マンガンを採
取する。
That is, by electrolyzing the above aqueous solution with a direct current of about 0.8 A / dm 2 , manganese dioxide is deposited on the anode, and when it is accumulated to some extent, it is peeled off and manganese dioxide is collected.

なお、その際陰極からは水素が発生する。At that time, hydrogen is generated from the cathode.

最近ではこのような電解二酸化マンガン製造用陽極材料
としてチタンが用いられている。これは、チタン電極が
耐食性・比強度・加工性に優れているためである。
Recently, titanium has been used as an anode material for producing such electrolytic manganese dioxide. This is because the titanium electrode has excellent corrosion resistance, specific strength and workability.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかしながら、前記のチタン陽極は電流密度を高くする
と表面の不働態膜が成長し、浴電圧が上昇してしまい、
さらになお通電を継続すると遂には通電不能となるとい
う問題がある。そのために電流密度は0.8A/dm2前後に
押さえておく必要があった。
However, when the current density of the titanium anode is increased, a passivation film on the surface grows and the bath voltage rises,
Further, there is a problem that if the power is still applied, the power cannot be finally applied. Therefore, it was necessary to keep the current density at around 0.8 A / dm 2 .

このように電流密度は電解工業においては直接生産性に
結びつく問題であり、同じ電解槽であれば電流密度が高
い程大量生産が可能となり、また生産量一定とすれば電
流密度が高い程電解槽を小さくすることができ、電解槽
建設のための設備費を小さくすることができるという利
点がある。
In this way, current density is a problem that directly leads to productivity in the electrolysis industry.If the same electrolytic cell has a higher current density, mass production becomes possible. Can be reduced, and the facility cost for constructing the electrolytic cell can be reduced.

さらに、電解二酸化マンガン製造用アノード材以外で
も、チタンは陽極として用いられているが、前記したよ
うに電流密度を高くすると表面の不働態膜が成長し、通
電不能となるため現在では白金メッキ等の貴金属メッキ
を行ない使われている。
Furthermore, titanium is used as an anode other than the anode material for the production of electrolytic manganese dioxide, but as mentioned above, when the current density is increased, a passive film on the surface grows, and current cannot be supplied. It is used by plating precious metals.

しかし、このような処理は非常に高価な貴金属を使うこ
と等により経済的負担が大きく、工業的利用上大きな問
題となっていた。
However, such a treatment imposes a heavy economic burden due to the use of a very expensive precious metal, which has been a serious problem in industrial use.

本発明は上記の事情に鑑みなされたものであり、従来使
用されていたチタン陽極材に代わり、より多くの高電流
密度が流せることを特徴とするチタン合金の陽極材料を
安価に提供することを目的としている。
The present invention has been made in view of the above circumstances, and in place of the titanium anode material that has been conventionally used, it is possible to inexpensively provide a titanium alloy anode material characterized by allowing a higher current density to flow. Has an aim.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明者は上記問題を解決するため鋭意研究の結果、本
発明を完成したものである。
The present inventors have completed the present invention as a result of earnest research to solve the above problems.

本発明の特徴はβ変態点以上に熱処理されたニッケル
0.1Wt%以上10Wt%以下で残部がチタン及び不
可避的な不純物からなるチタン合金を、その後400℃
以上800℃以下の温度で熱処理することにより優れた
アノード用材料を得ることができる製造方法である。
A feature of the present invention is that a titanium alloy heat-treated to a β transformation temperature or higher is 0.1 Wt% or more and 10 Wt% or less, and the balance is titanium and unavoidable impurities.
This is a manufacturing method in which an excellent anode material can be obtained by heat treatment at a temperature of 800 ° C. or lower.

本発明がチタンにニッケルを添加するのは、チタン中に
Ti2Niの金属間化合物を形成させることを目的としてい
る。このTi2Niはチタンと異なり、高電流密度で電流を
流しても陽極酸化はおきず、通電不能にならない特徴を
有しており、このTi2Niがチタン中に存在することによ
り、より多くの電流を流すことができる。
The present invention adds nickel to titanium because
The purpose is to form an intermetallic compound of Ti 2 Ni. The Ti 2 Ni Unlike titanium, anodic oxidation even by applying a current at a high current density Okizu has a characteristic that does not disable energization by the Ti 2 Ni is present in the titanium, more Can flow current.

ただし、ニッケルの含有量0.1wt%より少ないとTi2Niの
形成量が少なくなり、効果が明白に現われてこないので
ニッケルの下限を0.1wt%とした。またニッケルの含有
量が10wt%を越えると加工性が非常に悪くなるので、
その上限を10wt%とした。
However, if the content of nickel is less than 0.1 wt%, the amount of Ti 2 Ni formed will be small and the effect will not appear clearly, so the lower limit of nickel was made 0.1 wt%. Also, if the nickel content exceeds 10 wt%, the workability will be extremely poor.
The upper limit was set to 10 wt%.

さらに、製造上においてはアノード材料として一般に使
用されているような形状に加工するためには、熱間鍛造
や熱間圧延等のβ変態点を越えた温度域での加熱が必ず
必要となり、このような材料はたとえニッケルを含んで
いても十分な効果が得られないことがわかり、これを改
善するためその後に400℃以上800℃以下の温度で
熱処理することにより微細なTi2Ni粒(数μm)がチタ
ン中に析出し、高電流が流せることが可能となった。
Further, in manufacturing, in order to process into a shape that is generally used as an anode material, heating in a temperature range beyond the β transformation point such as hot forging and hot rolling is absolutely necessary. It has been found that such a material does not have a sufficient effect even if it contains nickel, and in order to improve this, it is subsequently heat treated at a temperature of 400 ° C or higher and 800 ° C or lower to obtain fine Ti 2 Ni particles (several (μm) was deposited in titanium, and it became possible to flow a high current.

〔実施例1〕 次に、本発明を具体的な実施例に基づき説明する。Example 1 Next, the present invention will be described based on specific examples.

まず、熱処理の効果を調べるため、ニッケルを3wt%含
んだTi−3%Niをアーク溶解にて溶解し、その後9
00℃にて鍛造し、再び950℃に加熱後熱間圧延によ
り厚さ6mmの熱間圧延板を作製した。この熱間圧延終了
時の材料温度は840℃であった。
First, in order to examine the effect of heat treatment, Ti-3% Ni containing 3 wt% of nickel was melted by arc melting, and then 9
After forging at 00 ° C., heating at 950 ° C. again, and hot rolling, a hot rolled plate having a thickness of 6 mm was produced. The material temperature at the end of this hot rolling was 840 ° C.

さらに、この材料を本発明方法に従い、熱処理したもの
とそれ以外の熱処理を行なった比較材を供試材として実
験に供した。
Further, this material was heat-treated in accordance with the method of the present invention and a comparative material heat-treated other than that was used as a test material in the experiment.

実験方法は、室温において0.35mol/H2SO4水溶液中に
てカソードに白金電極、アノードにバフ研摩上りの供試
材を用い、定電流電解試験を実施し、浴電圧上昇がどの
くらいの時間で起こるのか調べ、アノード特性を評価し
た。
The experimental method was to conduct a constant current electrolysis test in a 0.35 mol / H 2 SO 4 aqueous solution at room temperature using a platinum electrode as the cathode and a buff-polished test material as the anode. It was investigated whether it would occur, and the anode characteristics were evaluated.

第1表及び第2表に上記実験方法により得られた各供試
材の結果を示す。
Tables 1 and 2 show the results of each test material obtained by the above experimental method.

浴電圧の経時変化は、一般に時間とともに上昇してゆく
が、アノード特性優劣の判断規準として浴電圧が4Vを
越えるまでの時間を採用した。
The change with time of the bath voltage generally rises with time, but the time until the bath voltage exceeds 4 V was adopted as the criterion for judging the superiority and inferiority of the anode characteristics.

〔製造条件〕 インゴット(Ti−3%Ni)→鍛造(900℃)→熱
間圧延(950℃)→熱処理→供試材。
[Manufacturing conditions] Ingot (Ti-3% Ni) → forging (900 ° C.) → hot rolling (950 ° C.) → heat treatment → test material.

第1表はTi−3%Ni熱間圧延材を熱処理した場合の
浴電圧上昇の変化を見たものであり、400℃の温度か
ら熱処理の効果がはっきりと表われはじめている。
Table 1 shows changes in the bath voltage increase when the Ti-3% Ni hot rolled material is heat-treated, and the effect of the heat treatment is beginning to be clearly seen from the temperature of 400 ° C.

一方、800℃においては、その効果が600℃に比較
し低下しており、900℃では熱処理の効果が全くなく
なってしまうことが判った。
On the other hand, at 800 ° C., the effect was lower than that at 600 ° C., and it was found that at 900 ° C., the effect of heat treatment was completely lost.

この結果熱処理温度は400℃〜800℃にする必要が
あることが確認された。
As a result, it was confirmed that the heat treatment temperature needs to be 400 ° C to 800 ° C.

〔製造条件〕 インゴット→鍛造(900℃)→熱間圧延(950℃)
→熱処理(600℃で3時間)→供試材。
[Production conditions] Ingot → Forging (900 ° C) → Hot rolling (950 ° C)
→ Heat treatment (3 hours at 600 ℃) → Specimen.

第2表は、ニッケル添加量の効果を調べた試験結果を示
している。ニッケル添加量0.1wt%より浴電圧上昇時間
が長くなりはじめ、その傾向はニッケル添加量が増すに
したがい顕著になるのが判る。
Table 2 shows the test results for examining the effect of the added amount of nickel. It can be seen that the bath voltage rising time becomes longer than the nickel addition amount of 0.1 wt%, and this tendency becomes more remarkable as the nickel addition amount increases.

この結果からニッケルの下限は0.1wt%とし上限は加工
性の点より10.0wt%とする必要があることが確認され
た。
From this result, it was confirmed that the lower limit of nickel should be 0.1 wt% and the upper limit should be 10.0 wt% from the viewpoint of workability.

〔実施例2〕 次に、電解二酸化マンガン製造の場合におけるアノード
材について説明する。
Example 2 Next, an anode material in the case of electrolytic manganese dioxide production will be described.

電解二酸化マンガン製造での現状はアノード材として純
チタンが使われているが、これを本発明に係る方法によ
り製造された供試材をアノード材として用いた場合、ど
の程度電流が多く流せるかを調べた結果を第3表に示
す。
At present in the production of electrolytic manganese dioxide, pure titanium is used as an anode material, but how much current can be passed when using a test material manufactured by the method according to the present invention as the anode material The examined results are shown in Table 3.

試験方法は95℃の0.35mol/H2SO4+0.55mol/MnS
O4水溶液にて、カソードにカーボン、アノードにサンド
ブラスト処理した供試材を用い通常純チタンに流してい
る0.8A/dm2の電流密度及びそれ以上の電流密度を流
し、浴電圧7Vを越えた時間を測定した。
The test method is 95 ° C 0.35mol / H 2 SO 4 + 0.55mol / MnS
Using a carbon dioxide as the cathode and a sandblasted test material as the anode in an O 4 aqueous solution, a current density of 0.8 A / dm 2 which is usually applied to pure titanium and a current density higher than that were applied, and the bath voltage exceeded 7V. The time was measured.

その結果、アノードとして純チタンを用いた場合、1.2
A/dm2流すと100時間以内に浴電圧が7Vを越えて
しまうのに対し、本発明方法により製造された供試材
(製造条件)は、1.4A/dm2電流を流しても浴電圧の
上昇はおきず非常に優れたアノード材であることが判っ
た。
As a result, when using pure titanium as the anode, 1.2
The bath voltage exceeds 7 V within 100 hours when A / dm 2 is passed, whereas the test material (manufacturing condition) produced by the method of the present invention has a bath voltage of 1.4 A / dm 2 It was found that the anode material was a very excellent anode material without any increase.

また、同じNi濃度であっても熱間圧延材に比べて本発
明方法により製造されたアノード材料の方がより高い電
流密度が流せることもわかった。
It was also found that even with the same Ni concentration, the anode material produced by the method of the present invention can flow a higher current density than the hot rolled material.

さらに、このようにして高電流密度にて製造されたMnO2
を電池に組み立て放電特性を測定したところ、従来品の
MnO2と同程度か、より優れた放電特性が得られ工業的に
も使用できることがわかった。
In addition, MnO 2 produced at high current density in this way
When assembled into a battery and measured the discharge characteristics,
It was found that a discharge characteristic equal to or better than that of MnO 2 was obtained and that it could be used industrially.

〔発明の効果〕〔The invention's effect〕

以上、説明したとおり本発明方法により製造されたTi
−Ni合金をアノード材として用いると、純チタンにく
らべ非常に高い電流密度を流すことができ、電解二酸化
マンガン製造用アノード、その他メッキ、電気分解用ア
ノードとしても使用可能となり、工業的価値が非常に優
れたアノード用材料を得ることができる。
As described above, Ti produced by the method of the present invention
When Ni alloy is used as an anode material, it can pass a much higher current density than pure titanium, and it can be used as an anode for electrolytic manganese dioxide production, other plating, and an anode for electrolysis. An excellent anode material can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】β変態点以上に熱処理されたニッケル0.
1Wt%以上10Wt%以下で残部がチタン及び不可的
な不純物からなるチタン合金を、その後400℃以上8
00℃以下の温度で熱処理することを特徴とするチタン
合金からなるアノード用材料の製造方法。
1. Nickel that has been heat treated to a β transformation point or higher.
A titanium alloy containing 1 Wt% or more and 10 Wt% or less and the balance of titanium and undesired impurities, and then 400 ° C. or more 8
A method for producing a material for an anode made of a titanium alloy, which comprises performing heat treatment at a temperature of 00 ° C. or less.
JP63330535A 1988-12-27 1988-12-27 Method for manufacturing anode material Expired - Lifetime JPH0633482B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63330535A JPH0633482B2 (en) 1988-12-27 1988-12-27 Method for manufacturing anode material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63330535A JPH0633482B2 (en) 1988-12-27 1988-12-27 Method for manufacturing anode material

Publications (2)

Publication Number Publication Date
JPH02175891A JPH02175891A (en) 1990-07-09
JPH0633482B2 true JPH0633482B2 (en) 1994-05-02

Family

ID=18233721

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63330535A Expired - Lifetime JPH0633482B2 (en) 1988-12-27 1988-12-27 Method for manufacturing anode material

Country Status (1)

Country Link
JP (1) JPH0633482B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2468126C1 (en) * 2011-11-11 2012-11-27 ООО "Компания МеталлРесурс" Method for production of insoluble anode on titanium base

Also Published As

Publication number Publication date
JPH02175891A (en) 1990-07-09

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