JP2022051582A - Titanium base material, method for manufacturing the same, electrode for water electrolysis and water electrolysis apparatus - Google Patents

Titanium base material, method for manufacturing the same, electrode for water electrolysis and water electrolysis apparatus Download PDF

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JP2022051582A
JP2022051582A JP2022008936A JP2022008936A JP2022051582A JP 2022051582 A JP2022051582 A JP 2022051582A JP 2022008936 A JP2022008936 A JP 2022008936A JP 2022008936 A JP2022008936 A JP 2022008936A JP 2022051582 A JP2022051582 A JP 2022051582A
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base material
titanium
titanium oxide
oxide film
water electrolysis
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JP7227543B2 (en
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陽祐 佐野
Yosuke Sano
信一 大森
Shinichi Omori
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Mitsubishi Materials Corp
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Abstract

PROBLEM TO BE SOLVED: To provide: a titanium base material especially excellent in conductivity and corrosion resistance and used even in severe corrosive environment; a method for manufacturing the same; an electrode for water electrolysis consisting of the titanium base material; and a water electrolysis apparatus.
SOLUTION: A titanium base material includes a base material main body consisting of titanium or titanium alloy. A Magneli phase titanium oxide film consisting of Magneli phase titanium oxide represented by the chemical formula TinO2n-1(4≤n≤10) is formed on the surface of the base material main body; the Magneli phase titanium oxide film including at least one or both of Ti4O7 and Ti5O9 has a porous structure having a nanometer order or a micrometer order; the total of the maximum peak intensities of Ti4O7 and Ti5O9 in the X-ray diffraction of the Magneli phase titanium oxide film is larger than the maximum peak intensities of the other Magneli phase titanium oxides; and the conductivity of the Magneli phase titanium oxide film is 1 S/cm or more.
SELECTED DRAWING: None
COPYRIGHT: (C)2022,JPO&INPIT

Description

本発明は、導電性及び耐食性に優れたチタン基材、チタン基材の製造方法、及び、このチタン基材からなる水電解用電極、水電解装置に関するものである。 The present invention relates to a titanium base material having excellent conductivity and corrosion resistance, a method for producing the titanium base material, an electrode for water electrolysis made of the titanium base material, and a water electrolysis apparatus.

チタンまたはチタン合金からなるチタン基材は、例えば特許文献１に示すように、電極等の通電部材の中でも、特に耐酸化性（耐食性）が要求される用途において用いられている。
しかしながら、例えば、固体高分子形燃料電池（ＰＥＦＣ）のカソード電極、水電解装置のアノード電極、リチウムイオン電池やリチウムイオンキャパシタ向け電極材など、高電位、酸素存在、強酸性雰囲気等の過酷な腐食環境下で使用される場合には、耐食性が十分とは言えず、使用時にチタン基材の表面に絶縁性のＴｉＯ２膜が形成されてしまい、電極等の通電部材としての性能が劣化するといった問題があった。 As shown in Patent Document 1, for example, a titanium base material made of titanium or a titanium alloy is used in applications where oxidation resistance (corrosion resistance) is particularly required among current-carrying members such as electrodes.
However, for example, the cathode electrode of a polymer electrolyte fuel cell (PEFC), the anode electrode of a water electrolyzer, the electrode material for lithium ion batteries and lithium ion capacitors, etc., are severely corroded by high potential, oxygen presence, strong acidic atmosphere, etc. When used in an environment, the corrosion resistance is not sufficient, and an insulating TiO 2 film is formed on the surface of the titanium base material during use, which deteriorates the performance as an energizing member such as an electrode. There was a problem.

このため、例えば特許文献２には、アルミニウム、ニッケル若しくはチタンからなる基材の表面に、金及び白金等の貴金属皮膜を形成し、導電性を確保したまま耐食性を向上させたものが提案されている。
また、特許文献３には、チタンまたはチタン合金の表面に、ＴｉＯ２のＸ回折ピークが見られない酸化被膜を成膜したチタン材が提案されている。
さらに、特許文献４には、純チタン若しくはチタン合金からなるチタン材の表面に、酸素とチタンの原子濃度比（Ｏ／Ｔｉ）が０．３以上１．７以下である酸化チタン層を有し、この酸化チタン層の上に、Ａｕ，Ｐｔ，Ｐｄから選択される少なくとも１種の貴金属を含む合金層を形成したものが提案されている。 Therefore, for example, Patent Document 2 proposes a substrate made of aluminum, nickel, or titanium in which a noble metal film such as gold and platinum is formed on the surface to improve corrosion resistance while ensuring conductivity. There is.
Further, Patent Document 3 proposes a titanium material having an oxide film formed on the surface of titanium or a titanium alloy in which the X diffraction peak of TIO 2 is not observed.
Further, Patent Document 4 has a titanium oxide layer having an atomic concentration ratio (O / Ti) of oxygen and titanium of 0.3 or more and 1.7 or less on the surface of a titanium material made of pure titanium or a titanium alloy. It has been proposed that an alloy layer containing at least one noble metal selected from Au, Pt, and Pd is formed on the titanium oxide layer.

特開２００３－２２６９９２号公報Japanese Patent Application Laid-Open No. 2003-226992 特開２０１０－１３５３１６号公報Japanese Unexamined Patent Publication No. 2010-135316 特許第５８３１６７０号公報Japanese Patent No. 5831670 特開２０１０－２３６０８３号公報Japanese Unexamined Patent Publication No. 2010-236083

Tsutomu Ioroi et; Stability of Corrosion-Resistant Magneli-Phase Ti4O7-Supported PEMFC Catalysts High Potentials,“Jornal of The Electorochemical Society”,155(4)B321-B326(2008)Tsutomu Ioroi et; Stability of Corrosion-Resistant Magneli-Phase Ti4O7-Supported PEMFC Catalysts High Potentials, “Jornal of The Electorochemical Society”, 155 (4) B321-B326 (2008)

ところで、特許文献２及び特許文献４に示すように、貴金属皮膜を形成した場合には、コストが非常に増加してしまい、広く使用することはできない。
また、特許文献３に記載された酸化被膜においては、導電性及び耐食性が不十分なため、過酷な環境下で使用する部材として適用することはできない。 By the way, as shown in Patent Document 2 and Patent Document 4, when a noble metal film is formed, the cost increases significantly and it cannot be widely used.
Further, the oxide film described in Patent Document 3 cannot be applied as a member used in a harsh environment because its conductivity and corrosion resistance are insufficient.

ここで、導電性及び耐食性に優れた材料としては、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンが挙げられる。このマグネリ相酸化チタンにおいては、ＴｉＯ２と同等の耐食性を有するとともに、グラファイトと同等の導電性を有している。
従来のマグネリ相酸化チタンとしては、例えば非特許文献１に示すように、ＴｉＯ２を高温で還元する熱還元法で製造されており、粉末形状のものが提供されている。
しかしながら、チタンまたはチタン合金からなる基材の表面にＴｉＯ２を形成して熱還元した場合には、酸素が基材側に拡散し、基材自体が酸化して、導電性等の特性が劣化してしまう。このため、マグネリ相酸化チタンの被膜を有するチタン基材等は提供されていなかった。 Here, examples of the material having excellent conductivity and corrosion resistance include magnetic phase titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10). This magnetic phase titanium oxide has corrosion resistance equivalent to that of TIO 2 and conductivity equivalent to that of graphite.
As the conventional magnetic phase titanium oxide, for example, as shown in Non-Patent Document 1, it is manufactured by a thermal reduction method in which TiO 2 is reduced at a high temperature, and a powder form is provided.
However, when TIO 2 is formed on the surface of a base material made of titanium or a titanium alloy and heat-reduced, oxygen diffuses to the base material side and the base material itself is oxidized, resulting in deterioration of properties such as conductivity. Resulting in. For this reason, a titanium base material or the like having a coating film of magnelli phase titanium oxide has not been provided.

本発明は、以上のような事情を背景としてなされたものであって、導電性及び耐食性に特に優れ、過酷な腐食環境下においても使用可能なチタン基材、チタン基材の製造方法、及び、このチタン基材からなる水電解用電極、水電解装置を提供することを目的としている。 The present invention has been made against the background of the above circumstances, and is a titanium base material which is particularly excellent in conductivity and corrosion resistance and can be used even in a harsh corrosive environment, a method for producing a titanium base material, and a method for producing a titanium base material. It is an object of the present invention to provide a water electrolysis electrode and a water electrolysis apparatus made of this titanium base material.

このような課題を解決して、前記目的を達成するために、本発明のチタン基材は、チタンまたはチタン合金からなる基材本体を有し、この基材本体の表面に、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜が形成されており、前記マグネリ相酸化チタン皮膜は、Ｔｉ４Ｏ７及びＴｉ５Ｏ９の少なくも一方又は両方を含有し、前記マグネリ相酸化チタン皮膜は、ナノメートルオーダー又はマイクロメートルオーダーのポーラス構造を有し、前記マグネリ相酸化チタン皮膜のＸ線回折におけるＴｉ４Ｏ７及びＴｉ５Ｏ９の最大ピーク強度の和が他のマグネリ相酸化チタンの最大ピーク強度よりも大きく、導電率が１Ｓ／ｃｍ以上であることを特徴としている。 In order to solve such a problem and achieve the above object, the titanium base material of the present invention has a base material main body made of titanium or a titanium alloy, and the surface of the base material main body has a chemical formula Tin O. A magnesium-phase titanium oxide film made of magnesium oxide represented by 2n-1 (4 ≦ n ≦ 10) is formed, and the magnesium-phase titanium oxide film is less than Ti 4 O 7 and Ti 5 O 9 . The magnesium oxide film has a porous structure on the order of nanometers or micrometers, and contains one or both of them, and Ti 4 O 7 and Ti 5 O 9 in the X-ray diffraction of the titanium oxide film of the magneti phase. The sum of the maximum peak intensities of the above is larger than the maximum peak intensities of other titanium oxides, and the conductivity is 1 S / cm or more.

この構成のチタン基材によれば、チタンまたはチタン合金からなる基材本体の表面に、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜が形成されているので、導電性及び耐食性に特に優れている。
よって、高電位、酸素存在、強酸性雰囲気等の過酷な腐食環境下においても、電極等の通電部材として使用することができる。 According to the titanium base material having this configuration, the surface of the base material main body made of titanium or a titanium alloy is subjected to the magnetic phase oxidation made of titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10). Since a titanium film is formed, it is particularly excellent in conductivity and corrosion resistance.
Therefore, it can be used as an energizing member such as an electrode even in a harsh corrosive environment such as a high potential, the presence of oxygen, and a strongly acidic atmosphere.

また、前記マグネリ相酸化チタン皮膜が、特に導電性及び耐食性に優れたＴｉ４Ｏ７及びＴｉ５Ｏ９の少なくも一方又は両方を含有しているので、高電位、酸素存在、強酸性雰囲気等の過酷な腐食環境下において使用される通電部材として特に適している。 Further, since the titanium oxide film of the magnety phase contains at least one or both of Ti 4 O 7 and Ti 5 O 9 , which are particularly excellent in conductivity and corrosion resistance, high potential, presence of oxygen, strong acid atmosphere, etc. It is particularly suitable as an energizing member used in the severely corroded environment of.

また、本発明のチタン基材においては、前記マグネリ相酸化チタン皮膜の膜厚が０．１μｍ以上３０μｍ以下の範囲内とされていることが好ましい。
この場合、前記マグネリ相酸化チタン皮膜の膜厚が０．１μｍ以上とされているので、十分な耐食性を確保することができる。
一方、前記マグネリ相酸化チタン皮膜の膜厚が３０μｍ以下とされているので、チタン基材として十分な導電性を確保することができる。
また、Ｔｉ基材を用いず、電極全体がマグネリ相酸化チタンから成る酸化物電極では、電極としての強度が不十分である。 Further, in the titanium substrate of the present invention, it is preferable that the film thickness of the magnesium phase oxide film is in the range of 0.1 μm or more and 30 μm or less.
In this case, since the film thickness of the magnetic phase titanium oxide film is 0.1 μm or more, sufficient corrosion resistance can be ensured.
On the other hand, since the film thickness of the magnetic phase titanium oxide film is 30 μm or less, sufficient conductivity can be ensured as a titanium base material.
Further, an oxide electrode in which the entire electrode is made of magnelli phase titanium oxide without using a Ti base material has insufficient strength as an electrode.

さらに、本発明のチタン基材においては、前記基材本体は、気孔率が３０％以上９７％以下の範囲内とされた多孔質体とされていることが好ましい。
この場合、チタンまたはチタン合金からなる基材本体が多孔質体とされており、その気孔率が３０％以上とされているので、比表面積が大きくなり、チタン基材の表面での反応を促進することができる。また、反応によって生成したガスを効率的に排出することができる。
一方、前記基材本体の気孔率が９７％以下とされているので、基材本体の強度を確保することができる。 Further, in the titanium base material of the present invention, it is preferable that the base material body is a porous body having a porosity in the range of 30% or more and 97% or less.
In this case, the main body of the base material made of titanium or a titanium alloy is a porous body, and the porosity is 30% or more, so that the specific surface area becomes large and the reaction on the surface of the titanium base material is promoted. can do. In addition, the gas generated by the reaction can be efficiently discharged.
On the other hand, since the porosity of the base material body is 97% or less, the strength of the base material body can be ensured.

本発明のチタン基材の製造方法は、上述のチタン基材の製造方法であって、チタンまたはチタン合金からなる基材本体の表面にＴｉＯ２皮膜を成膜するＴｉＯ２皮膜形成工程と、前記基材本体の表面に形成されたＴｉＯ２皮膜をマイクロ波プラズマ還元法によって還元し、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜とする還元処理工程と、を備えており、還元処理工程は、基板温度４００℃以下、処理時間１５分以下の条件で実施することを特徴としている。 The method for producing a titanium base material of the present invention is the above-mentioned method for producing a titanium base material, which comprises a TiO 2 film forming step of forming a TiO 2 film on the surface of a base body made of titanium or a titanium alloy, and the above-mentioned method. The TiO 2 film formed on the surface of the main body of the base material is reduced by the microwave plasma reduction method, and the magnesium oxide is composed of titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10). It includes a reduction treatment step of forming a film, and the reduction treatment step is characterized in that it is carried out under the conditions of a substrate temperature of 400 ° C. or lower and a treatment time of 15 minutes or less.

この構成のチタン基材の製造方法においては、チタンまたはチタン合金からなる基材本体の表面にＴｉＯ２皮膜を成膜するＴｉＯ２皮膜形成工程と、このＴｉＯ２皮膜をマイクロ波プラズマ還元法によって還元してマグネリ相酸化チタン皮膜とする還元処理工程と、を備えているので、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜を有するチタン基材を製造することが可能となる。
そして、還元処理工程を、基板温度４００℃以下、処理時間１５分以下の条件で実施しているので、酸素が基材本体側に拡散することを抑制でき、基材本体の特性の劣化を抑制することができる。
さらに、ＴｉＯ２皮膜形成工程においてＴｉＯ２皮膜の膜厚を調整することにより、マグネリ相酸化チタン皮膜の膜厚を制御することができる。 In the method for producing a titanium base material having this configuration, a TiO 2 film forming step of forming a TiO 2 film on the surface of a base body made of titanium or a titanium alloy, and the reduction of the TiO 2 film by a microwave plasma reduction method. Since it is provided with a reduction treatment step of forming a magnesium phase titanium oxide film, a magnesium phase titanium oxide film made of magnesium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) is formed. It becomes possible to manufacture a titanium base material having.
Since the reduction treatment step is carried out under the conditions of the substrate temperature of 400 ° C. or less and the treatment time of 15 minutes or less, it is possible to suppress the diffusion of oxygen to the base material main body side and suppress the deterioration of the characteristics of the base material main body. can do.
Further, by adjusting the film thickness of the TiO 2 film in the TiO 2 film forming step, the film thickness of the magnetic phase titanium oxide film can be controlled.

本発明の水電解用電極は、上述のチタン基材からなることを特徴としている。
この構成の水電解用電極によれば、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜が形成されたチタン基材で構成されているので、導電性及び耐食性に特に優れており、酸化による劣化を抑えることができ、使用寿命を大幅に向上させることができる。また、耐食性に優れているので、貴金属電極の代替として使用することができ、水電解用電極を低コストで構成することが可能となる。 The electrode for water electrolysis of the present invention is characterized by being made of the above-mentioned titanium base material.
According to the electrode for water electrolysis having this configuration, it is composed of a titanium base material on which a magnesium oxide titanium film composed of titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) is formed. Therefore, it is particularly excellent in conductivity and corrosion resistance, can suppress deterioration due to oxidation, and can greatly improve the service life. Further, since it has excellent corrosion resistance, it can be used as a substitute for a noble metal electrode, and an electrode for water electrolysis can be configured at low cost.

ここで、本発明の水電解用電極においては、２．５Ｖで１分保持及び０Ｖで１分保持を１サイクルとしたボルタンメトリー試験において、１２００サイクル後の電解効率が初期値に対して９０％以上１００％未満であることが好ましい。
この場合、水電解装置の起動停止を模したボルタンメトリー試験において、１２００サイクル後の電解効率が初期値に対して９０％以上に維持されているので、使用時における水電解用電極の劣化が確実に抑制されており、使用寿命を確実に向上させることが可能となる。 Here, in the electrode for water electrolysis of the present invention, in the voltammetry test in which holding at 2.5 V for 1 minute and holding at 0 V for 1 minute is one cycle, the electrolysis efficiency after 1200 cycles is 90% or more with respect to the initial value. It is preferably less than 100%.
In this case, in the voltammetry test that imitates the start and stop of the water electrolysis device, the electrolysis efficiency after 1200 cycles is maintained at 90% or more of the initial value, so that the deterioration of the water electrolysis electrode during use is certain. It is suppressed, and it is possible to surely improve the service life.

本発明の水電解装置は、上述の水電解用電極を備えたことを特徴としている。
この構成の水電解用電極によれば、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜が形成されたチタン基材で構成された水電解用電極を備えているので、使用時における水電解用電極の酸化による劣化を抑えることができ、長期間安定して使用することが可能となる。また、貴金属電極を用いる必要がなく、水電解装置の製造コストを大幅に削減することができる。 The water electrolysis apparatus of the present invention is characterized by including the above-mentioned electrode for water electrolysis.
According to the electrode for water electrolysis having this configuration, it is composed of a titanium base material on which a magnesium oxide film made of magnesium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) is formed. Since the water electrolysis electrode is provided, deterioration due to oxidation of the water electrolysis electrode during use can be suppressed, and stable use can be achieved for a long period of time. Moreover, it is not necessary to use a noble metal electrode, and the manufacturing cost of the water electrolyzer can be significantly reduced.

本発明によれば、導電性及び耐食性に特に優れ、過酷な腐食環境下においても使用可能なチタン基材、チタン基材の製造方法、及び、このチタン基材からなる水電解用電極、水電解装置を提供することができる。 According to the present invention, a titanium base material which is particularly excellent in conductivity and corrosion resistance and can be used even in a harsh corrosive environment, a method for producing a titanium base material, an electrode for water electrolysis made of this titanium base material, and water electrolysis. The device can be provided.

本発明の実施形態であるチタン基材の一例を示す説明図である。It is explanatory drawing which shows an example of the titanium base material which is an embodiment of this invention. 図１に示すチタン基材の表層部分の拡大模式図である。It is an enlarged schematic diagram of the surface layer portion of the titanium base material shown in FIG. 1. 図１に示すチタン基材の製造方法の一例を示すフロー図である。It is a flow chart which shows an example of the manufacturing method of the titanium base material shown in FIG. 図１に示すチタン基材を製造する製造工程を示す説明図である。図４（ａ）は基材本体準備工程Ｓ０１、図４（ｂ）はＴｉＯ２皮膜形成工程Ｓ０２、図４（ｃ）は還元処理工程Ｓ０３を示す。It is explanatory drawing which shows the manufacturing process which manufactures the titanium base material shown in FIG. FIG. 4A shows a substrate main body preparation step S01, FIG. 4B shows a TiO2 film forming step S02, and FIG. 4C shows a reduction treatment step S03. 本発明の実施形態である水電解用電極を備えた水電解装置の概略説明図である。It is a schematic explanatory drawing of the water electrolysis apparatus provided with the electrode for water electrolysis which is an embodiment of this invention. 実施例における本発明例２及び比較例１のＸＲＤ分析結果を示すグラフである。It is a graph which shows the XRD analysis result of this invention example 2 and comparative example 1 in an Example. 実施例における本発明例１のチタン基材の断面観察結果を示すＳＥＭ画像である。It is an SEM image which shows the cross-sectional observation result of the titanium base material of this invention Example 1 in an Example. 実施例における本発明例１１のチタン基材の断面観察結果を示すＳＥＭ画像である。It is an SEM image which shows the cross-sectional observation result of the titanium base material of this invention example 11 in an Example.

以下に、本発明の実施形態であるチタン基材、チタン基材の製造方法、及び、水電解用電極、水電解装置について、添付した図面を参照して説明する。 Hereinafter, the titanium base material, the method for producing the titanium base material, the electrode for water electrolysis, and the water electrolysis apparatus according to the embodiment of the present invention will be described with reference to the attached drawings.

＜チタン基材及びチタン基材の製造方法＞
本実施形態であるチタン基材１０は、例えば、固体高分子形燃料電池（ＰＥＦＣ）のカソード電極、水電解装置のアノード電極、リチウムイオン電池やリチウムイオンキャパシタ向け電極材等の通電部材として使用されるものである。 <Manufacturing method of titanium base material and titanium base material>
The titanium base material 10 of the present embodiment is used as an energizing member for, for example, a cathode electrode of a polymer electrolyte fuel cell (PEFC), an anode electrode of a water electrolyzer, an electrode material for a lithium ion battery or a lithium ion capacitor, and the like. It is a thing.

本実施形態であるチタン基材１０は、図１及び図２に示すように、チタンまたはチタン合金からなる基材本体１１と、この基材本体１１の表面に形成されたマグネリ相酸化チタン皮膜１６と、を備えている。 As shown in FIGS. 1 and 2, the titanium base material 10 of the present embodiment has a base material main body 11 made of titanium or a titanium alloy and a magnesium phase titanium oxide film 16 formed on the surface of the base material main body 11. And have.

本実施形態においては、基材本体１１は、図１に示すように、多孔質体とされており、３次元網目構造とされた骨格部１２と、この骨格部１２に囲まれた気孔部１３と、を備えている。
この基材本体１１は、その気孔率Ｐが３０％以上９７％以下の範囲内とされている。基材本体１１の気孔率Ｐは、以下の式で算出される。
Ｐ（％）＝（１－（Ｗ／（Ｖ×ＤＴ）））×１００
Ｗ：基材本体１１の質量（ｇ）
Ｖ：基材本体１１の体積（ｃｍ３）
ＤＴ：基材本体１１を構成するチタンまたはチタン合金の真密度（ｇ／ｃｍ３） In the present embodiment, as shown in FIG. 1, the base material main body 11 is a porous body, and has a skeleton portion 12 having a three-dimensional network structure and a pore portion 13 surrounded by the skeleton portion 12. And have.
The base material body 11 has a porosity P of 30% or more and 97% or less. The porosity P of the base material body 11 is calculated by the following formula.
P (%) = (1- (W / (V × DT ))) × 100
W: Mass (g) of the base material body 11
V: Volume of base material body 11 (cm 3 )
DT : True density of titanium or titanium alloy constituting the base material body 11 (g / cm 3 )

なお、本実施形態においては、この多孔質体からなる基材本体１１は、例えば、チタンを含むチタン焼結原料を焼結させたチタン焼結体で構成されている。
また、骨格部１２に囲まれた気孔部１３は、互いに連通するとともに、基材本体１１の外部に向けて開口した構造とされている。 In the present embodiment, the base material main body 11 made of this porous body is made of, for example, a titanium sintered body obtained by sintering a titanium sintering raw material containing titanium.
Further, the pore portions 13 surrounded by the skeleton portion 12 communicate with each other and have a structure that opens toward the outside of the base material main body 11.

そして、図２に示すように、この基材本体１１の表面に、マグネリ相酸化チタン皮膜１６が形成されている。
このマグネリ相酸化チタン皮膜１６は、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンで構成されている。 Then, as shown in FIG. 2, a magnetic phase titanium oxide film 16 is formed on the surface of the base material main body 11.
The magnetic phase titanium oxide film 16 is composed of a magnetic phase titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10).

本実施形態においては、マグネリ相酸化チタン皮膜１６は、Ｔｉ４Ｏ７及びＴｉ５Ｏ９の少なくも一方又は両方を含有するものとされている。このマグネリ相酸化チタン皮膜１６におけるチタン酸化物の構造については、Ｘ線回折分析（ＸＲＤ）法によって同定することができる。
なお、本実施形態のマグネリ相酸化チタン皮膜１６においては、Ｘ線回折（ＸＲＤ）におけるＴｉ４Ｏ７及びＴｉ５Ｏ９のＸＲＤピークを含み、両者の最大ピーク強度の和が他のマグネリ相酸化Ｔｉ（６≦ｎ≦１０）の最大ピーク強度よりも大きい。 In the present embodiment, the magnetic phase titanium oxide film 16 is supposed to contain at least one or both of Ti 4 O 7 and Ti 5 O 9 . The structure of the titanium oxide in this magnetic phase titanium oxide film 16 can be identified by the X-ray diffraction analysis (XRD) method.
The magnesium oxide film 16 of the present embodiment includes the XRD peaks of Ti 4 O 7 and Ti 5 O 9 in X-ray diffraction (XRD), and the sum of the maximum peak intensities of both is the sum of the other magnitude phase oxidation. It is larger than the maximum peak intensity of Ti (6 ≦ n ≦ 10).

ここで、マグネリ相酸化チタン皮膜１６の膜厚ｔを薄くすると、耐食性が低下するが導電性が向上することになる。一方、マグネリ相酸化チタン皮膜１６の膜厚ｔを厚くすると、耐食性が向上するが導電性が低下することになる。このため、マグネリ相酸化チタン皮膜１６の膜厚ｔは、チタン基材１０への要求特性に応じて適宜設定することが好ましい。
本実施形態においては、耐食性を十分に向上させるために、マグネリ相酸化チタン皮膜１６の膜厚ｔの下限を０．１μｍ以上としている。また、導電性を十分に向上させるために、マグネリ相酸化チタン皮膜１６の膜厚ｔの上限を３０μｍ以下としている。
なお、耐食性をさらに向上させるためには、マグネリ相酸化チタン皮膜１６の膜厚ｔの下限を０．２μｍ以上とすることが好ましく、０．３μｍ以上とすることがさらに好ましい。一方、導電性をさらに向上させるためには、マグネリ相酸化チタン皮膜１６の膜厚ｔの上限を５μｍ以下とすることが好ましく、３μｍ以下とすることがさらに好ましい。 Here, if the film thickness t of the magnetic phase titanium oxide film 16 is reduced, the corrosion resistance is lowered, but the conductivity is improved. On the other hand, if the film thickness t of the magnetic phase titanium oxide film 16 is increased, the corrosion resistance is improved, but the conductivity is lowered. Therefore, it is preferable that the film thickness t of the magnetic phase titanium oxide film 16 is appropriately set according to the required characteristics for the titanium base material 10.
In the present embodiment, in order to sufficiently improve the corrosion resistance, the lower limit of the film thickness t of the magnetic phase titanium oxide film 16 is set to 0.1 μm or more. Further, in order to sufficiently improve the conductivity, the upper limit of the film thickness t of the magnetic phase titanium oxide film 16 is set to 30 μm or less.
In order to further improve the corrosion resistance, the lower limit of the film thickness t of the magnesium phase titanium oxide film 16 is preferably 0.2 μm or more, and more preferably 0.3 μm or more. On the other hand, in order to further improve the conductivity, the upper limit of the film thickness t of the magnetic phase titanium oxide film 16 is preferably 5 μm or less, and more preferably 3 μm or less.

また、本実施形態においては、マグネリ相酸化チタン皮膜１６は、その膜内にナノメートル又はマイクロメートルオーダーのポーラス構造を有する。 Further, in the present embodiment, the magnetic phase titanium oxide film 16 has a porous structure on the order of nanometers or micrometer in the film.

以下に、本実施形態であるチタン基材１０の製造方法について、図３のフロー図及び図４の工程図等を参照して説明する。 Hereinafter, the method for manufacturing the titanium base material 10 according to the present embodiment will be described with reference to the flow chart of FIG. 3 and the process chart of FIG.

（基材本体準備工程Ｓ０１）
まず、図４（ａ）で示す、チタン及びチタン合金からなる基材本体１１を準備する。本実施形態では、基材本体１１として、多孔質のチタン焼結体を準備する。
この多孔質のチタン焼結体からなる基材本体１１は、例えば、以下のような工程で製造することができる。チタンを含む焼結原料を、有機バインダー、発泡剤、可塑剤、水及び必要に応じて界面活性剤を混合して、発泡性スラリーを作製する。この発泡性スラリーを、ドクターブレード（塗布装置）を用いて塗布し、シート状の成形体を成形する。このシート状の成形体を加熱して発泡させて発泡成形体を得る。そして、これを脱脂した後で焼結する。これにより、多孔質のチタン焼結体からなる基材本体１１が作製される。（例えば、特開２００６－１３８００５号公報、特開２００３－０８２４０５号公参照） (Base material main body preparation step S01)
First, the base material main body 11 made of titanium and a titanium alloy shown in FIG. 4A is prepared. In the present embodiment, a porous titanium sintered body is prepared as the base material main body 11.
The base material main body 11 made of this porous titanium sintered body can be manufactured, for example, by the following steps. The sintered raw material containing titanium is mixed with an organic binder, a foaming agent, a plasticizer, water and, if necessary, a surfactant to prepare an effervescent slurry. This effervescent slurry is applied using a doctor blade (coating device) to form a sheet-shaped molded product. This sheet-shaped molded product is heated and foamed to obtain a foamed molded product. Then, after degreasing this, it is sintered. As a result, the base material main body 11 made of a porous titanium sintered body is produced. (For example, refer to JP-A-2006-138005 and JP-A-2003-082405).

（ＴｉＯ２皮膜形成工程Ｓ０２）
次に、図４（ｂ）に示すように、基材本体１１の表面に、ＴｉＯ２皮膜２６を形成する。このＴｉＯ２皮膜形成工程Ｓ０２においては、酸素が基材本体１１側に拡散することを抑制するために、１００℃以下の温度条件で実施する。
温度条件の下限値は限定されないが、０℃までの範囲で、以下のプラズマ電解酸化処理を効率よく行うことができる。 (TiO 2 film forming step S02)
Next, as shown in FIG. 4 (b), the TiO 2 film 26 is formed on the surface of the base material main body 11. This TiO 2 film forming step S02 is carried out under a temperature condition of 100 ° C. or lower in order to prevent oxygen from diffusing toward the base material main body 11.
Although the lower limit of the temperature condition is not limited, the following plasma electrolytic oxidation treatment can be efficiently performed in the range up to 0 ° C.

本実施形態では、通常の陽極酸化よりも高電圧を印加し、基材表面にアーク放電を発生させ酸化を進める、プラズマ電解酸化法によってＴｉＯ２皮膜２６を成膜している。具体的には、Ｋ３ＰＯ４，Ｎａ３ＰＯ４，Ｋ４Ｐ２Ｏ７，Ｎａ２Ｐ２Ｏ７等の水溶液浴中で、プラズマ電解酸化処理を実施した。
ここで、ＴｉＯ２皮膜２６の膜厚ｔ０は、０．１μｍ以上３０μｍ以下の範囲内とすることが好ましい。 In the present embodiment, the TiO 2 film 26 is formed by a plasma electrolytic oxidation method in which a voltage higher than that of normal anodic oxidation is applied to generate an arc discharge on the surface of the substrate to promote the oxidation. Specifically, plasma electrolytic oxidation treatment was carried out in an aqueous solution bath of K 3 PO 4 , Na 3 PO 4 , K 4 P 2 O 7 , Na 2 P 2 O 7 , and the like.
Here, the film thickness t0 of the TiO 2 film 26 is preferably in the range of 0.1 μm or more and 30 μm or less.

（還元処理工程Ｓ０３）
次に、ＴｉＯ２皮膜２６に対して、ガスにマイクロ波を照射して生成したプラズマを用いて還元処理を行う（マイクロ波プラズマ還元処理）ことで、図４（ｃ）に示すように、ＴｉＯ２皮膜２６を、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜１６とする。この還元処理工程Ｓ０３においては、酸素が基材本体１１側に拡散することを抑制するために、基板温度４００℃以下、処理時間１５分以下の条件で実施する。
還元処理工程Ｓ０３の基板温度の下限値は０℃、処理時間の下限値は０．０１分とすることができる。 (Reduction processing step S03)
Next, the dio 2 film 26 is subjected to a reduction treatment using the plasma generated by irradiating the gas with microwaves (microwave plasma reduction treatment), so that the TiO is shown in FIG. 4 (c). The two films 26 are designated as a magnesium phase titanium oxide film 16 made of titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10). In this reduction treatment step S03, in order to suppress the diffusion of oxygen to the base material main body 11, the substrate temperature is 400 ° C. or lower and the treatment time is 15 minutes or less.
The lower limit of the substrate temperature in the reduction treatment step S03 can be 0 ° C., and the lower limit of the treatment time can be 0.01 minutes.

なお、ＴｉＯ２皮膜２６の全体を還元処理してマグネリ相酸化チタン皮膜１６とすることにより、ＴｉＯ２皮膜２６の膜厚ｔ０が、マグネリ相酸化チタン皮膜１６の膜厚ｔとなる。よって、ＴｉＯ２皮膜形成工程Ｓ０２におけるＴｉＯ２皮膜２６の膜厚ｔ０を調整することにより、マグネリ相酸化チタン皮膜１６の膜厚ｔを制御することが可能となる。 By reducing the entire TiO 2 film 26 to form the magnetic phase titanium oxide film 16, the film thickness t0 of the TiO 2 film 26 becomes the film thickness t of the magnetic phase titanium oxide film 16. Therefore, by adjusting the film thickness t0 of the TiO 2 film 26 in the TiO 2 film forming step S02, it is possible to control the film thickness t of the magnetic phase titanium oxide film 16.

上述の製造方法により、チタンまたはチタン合金からなる基材本体１１の表面に、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜１６が形成されたチタン基材１０が製造されることになる。 By the above-mentioned manufacturing method, a magnesium phase titanium oxide film 16 made of a magnesium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) is formed on the surface of a base material main body 11 made of titanium or a titanium alloy. The titanium base material 10 on which the above is formed will be manufactured.

＜水電解用電極及び水電解装置＞
本実施形態である水電解用電極及び水電解装置の概略図を図５に示す。なお、本実施形態の水電解装置は、電解効率及び生成時の水素純度が高い、固体高分子形水分解装置とされている。 <Electrodes for water electrolysis and water electrolysis equipment>
FIG. 5 shows a schematic view of the water electrolysis electrode and the water electrolysis apparatus according to the present embodiment. The water electrolysis device of the present embodiment is a solid polymer electrolysis device having high electrolysis efficiency and hydrogen purity at the time of production.

本実施形態の水電解装置３０は、図５に示すように、対向配置されたアノード極３２及びカソード極３３と、これらアノード極３２とカソード極３３との間に配置されたイオン透過膜３４と、を備えた水電解セル３１を備えている。なお、イオン透過膜３４の両面（アノード極３２との接触面及びカソード極３３との接触面）には、それぞれ触媒層３５，３６が形成されている。
ここで、カソード極３３、イオン透過膜３４、触媒層３５，３６については、従来の一般的な固体高分子形水電解装置で使用されているものを適用することができる。 As shown in FIG. 5, the water electrolyzer 30 of the present embodiment includes an anode pole 32 and a cathode pole 33 arranged to face each other, and an ion permeation film 34 arranged between the anode pole 32 and the cathode pole 33. The water electrolysis cell 31 with the above is provided. The catalyst layers 35 and 36 are formed on both surfaces of the ion permeation membrane 34 (contact surface with the anode electrode 32 and contact surface with the cathode electrode 33), respectively.
Here, as the cathode electrode 33, the ion permeable membrane 34, and the catalyst layers 35, 36, those used in a conventional general polymer electrolyte water electrolyzer can be applied.

そして、上述のアノード極３２が、本実施形態である水電解用電極とされている。このアノード極３２（水電解用電極）は、上述した本実施形態であるチタン基材１０で構成されており、チタンまたはチタン合金からなる基材本体１１と、この基材本体１１の表面に形成されたマグネリ相酸化チタン皮膜１６と、を備えている。また、基材本体１１が、多孔質体とされており、３次元網目構造とされた骨格部１２と、この骨格部１２に囲まれた気孔部１３と、を備えた構造とされている。
ここで、本実施形態である水電解用電極（アノード極３２）においては、２．５Ｖで１分保持及び０Ｖで１分保持を１サイクルとしたボルタンメトリー試験において、１２００サイクル後の電解効率が初期値に対して９０％以上であることが好ましい。 The anode electrode 32 described above is the electrode for water electrolysis according to the present embodiment. The anode electrode 32 (electrode for water electrolysis) is composed of the titanium base material 10 of the present embodiment described above, and is formed on the base material main body 11 made of titanium or a titanium alloy and the surface of the base material main body 11. The magneti phase titanium oxide film 16 is provided. Further, the base material main body 11 is a porous body, and has a structure including a skeleton portion 12 having a three-dimensional network structure and a pore portion 13 surrounded by the skeleton portion 12.
Here, in the water electrolysis electrode (anode electrode 32) of the present embodiment, in the voltammetry test in which holding at 2.5 V for 1 minute and holding at 0 V for 1 minute is one cycle, the electrolysis efficiency after 1200 cycles is initial. It is preferably 90% or more with respect to the value.

上述の水電解装置３０（水電解セル３１）においては、図５に示すように、アノード極３２側から水（Ｈ２Ｏ）が供給されるとともに、アノード極３２及びカソード極３３に通電される。すると、水の電解によって生じた酸素（Ｏ２）がアノード極３２から排出され、水素（Ｈ２）がカソード極３３から排出されることになる。
ここで、アノード極３２においては、上述のように、水（液体）と酸素（気体）が流通することになるので、これら液体及び気体を安定して流通させるために、高い気孔率を有することが好ましい。また、アノード極３２は酸素に晒されるため、優れた耐食性が求められる。このため、本実施形態であるチタン基材１０からなる水電解用電極が、アノード極３２として特に適している。 In the water electrolysis device 30 (water electrolysis cell 31) described above, as shown in FIG. 5, water ( H2O ) is supplied from the anode pole 32 side, and the anode pole 32 and the cathode pole 33 are energized. .. Then, oxygen (O 2 ) generated by electrolysis of water is discharged from the anode pole 32, and hydrogen (H 2 ) is discharged from the cathode pole 33.
Here, since water (liquid) and oxygen (gas) flow through the anode electrode 32 as described above, the anode pole 32 has a high porosity in order to allow these liquids and gas to flow stably. Is preferable. Further, since the anode electrode 32 is exposed to oxygen, excellent corrosion resistance is required. Therefore, the electrode for water electrolysis made of the titanium base material 10 of the present embodiment is particularly suitable as the anode electrode 32.

以上のような構成とされた本実施形態であるチタン基材１０によれば、チタンまたはチタン合金からなる基材本体１１の表面に、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜１６が形成されているので、導電性及び耐食性に特に優れている。
よって、高電位、酸素存在、強酸性雰囲気等の過酷な腐食環境下においても、電極等の通電部材として使用することができる。 According to the titanium base material 10 of the present embodiment having the above configuration, the surface of the base material main body 11 made of titanium or a titanium alloy has the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10). Since the magnelli phase titanium oxide film 16 made of the represented magnelli phase titanium oxide is formed, it is particularly excellent in conductivity and corrosion resistance.
Therefore, it can be used as an energizing member such as an electrode even in a harsh corrosive environment such as a high potential, the presence of oxygen, and a strongly acidic atmosphere.

また、本実施形態においては、マグネリ相酸化チタン皮膜１６が、マグネリ相酸化チタンとして、特に導電性及び耐食性に優れたＴｉ４Ｏ７及びＴｉ５Ｏ９の少なくとも一方又は両方を含有しているので、高電位、酸素存在、強酸性雰囲気等の過酷な腐食環境下において使用される通電部材として特に適している。
さらに、本実施形態においては、マグネリ相酸化チタン皮膜１６の膜厚ｔが０．１μｍ以上３０μｍ以下の範囲内とされているので、耐食性と導電性をバランス良く向上させることが可能となる。 Further, in the present embodiment, the magnetic phase titanium oxide film 16 contains at least one or both of Ti 4 O 7 and Ti 5 O 9 which are particularly excellent in conductivity and corrosion resistance as the magnetic phase titanium oxide. It is particularly suitable as an energizing member used in a harsh corrosive environment such as high potential, presence of oxygen, and strong acid atmosphere.
Further, in the present embodiment, since the film thickness t of the magnetic phase titanium oxide film 16 is within the range of 0.1 μm or more and 30 μm or less, it is possible to improve the corrosion resistance and the conductivity in a well-balanced manner.

また、本実施形態においては、チタンまたはチタン合金からなる基材本体１１が多孔質体とされており、その気孔率Ｐが３０％以上とされているので、比表面積が大きくなり、チタン基材１０の表面での反応を促進することができる。また、反応によって生成したガスを効率的に排出することができる。よって、電極部材として特に適している。
一方、多孔質体とされた基材本体１１の気孔率Ｐが９７％以下とされているので、基材本体１１の強度を確保することができる。 Further, in the present embodiment, the base material main body 11 made of titanium or a titanium alloy is a porous body, and its porosity P is 30% or more, so that the specific surface area becomes large and the titanium base material is used. The reaction on the surface of 10 can be promoted. In addition, the gas generated by the reaction can be efficiently discharged. Therefore, it is particularly suitable as an electrode member.
On the other hand, since the porosity P of the base material main body 11 made of a porous body is 97% or less, the strength of the base material main body 11 can be ensured.

また、本実施形態においては、マグネリ相酸化チタン皮膜１６がナノメートル又はマイクロメートルオーダーのポーラス構造をなしており、電極基材の表面積をさらに向上させることが可能となる。 Further, in the present embodiment, the magnesium phase titanium oxide film 16 has a porous structure on the order of nanometers or micrometers, which makes it possible to further improve the surface area of the electrode base material.

本実施形態であるチタン基材１０の製造方法においては、チタンまたはチタン合金からなる基材本体１１を準備する基材本体準備工程Ｓ０１と、この基材本体１１の表面にＴｉＯ２皮膜２６を成膜するＴｉＯ２皮膜形成工程Ｓ０２と、このＴｉＯ２皮膜２６をマイクロ波プラズマ還元法によって還元して、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜１６とする還元処理工程Ｓ０３と、を備えているので、耐食性及び導電性に特に優れたチタン基材１０を製造することが可能となる。 In the method for manufacturing the titanium base material 10 according to the present embodiment, the base material main body preparation step S01 for preparing the base material main body 11 made of titanium or a titanium alloy and the TiO 2 film 26 are formed on the surface of the base material main body 11. It is composed of the TIO 2 film forming step S02 to be filmed and the magnelli phase titanium oxide represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) by reducing the TIO 2 film 26 by a microwave plasma reduction method. Since the reduction treatment step S03 for forming the magnetic phase titanium oxide film 16 is provided, it is possible to manufacture the titanium base material 10 having particularly excellent corrosion resistance and conductivity.

そして、ＴｉＯ２皮膜形成工程Ｓ０２を１００℃以下で実施し、還元処理工程Ｓ０３を、基板温度４００℃以下、処理時間１５分以下の条件で実施しているので、酸素が基材本体１１側に拡散することを抑制でき、基材本体１１の特性の劣化を抑制することができる。
さらに、ＴｉＯ２皮膜形成工程Ｓ０２において成膜するＴｉＯ２皮膜２６の膜厚ｔ０を調整することにより、マグネリ相酸化チタン皮膜１６の膜厚ｔを精度良く制御することができる。 Then, since the TiO 2 film forming step S02 is carried out at 100 ° C. or lower and the reduction treatment step S03 is carried out under the conditions of a substrate temperature of 400 ° C. or lower and a treatment time of 15 minutes or less, oxygen is applied to the substrate main body 11 side. Diffusion can be suppressed, and deterioration of the characteristics of the base material main body 11 can be suppressed.
Further, by adjusting the film thickness t0 of the TiO 2 film 26 to be formed in the TiO 2 film forming step S02, the film thickness t of the magnetic phase titanium oxide film 16 can be controlled with high accuracy.

本実施形態である水電解用電極（アノード極３２）においては、上述したチタン基材１０で構成されているので、導電性及び耐食性に特に優れており、酸化による劣化を抑えることができ、使用寿命を大幅に向上させることができる。また、耐食性に優れているので、貴金属電極の代替として使用することができ、水電解用電極（アノード極３２）を低コストで構成することができる。 Since the water electrolysis electrode (anode electrode 32) of the present embodiment is composed of the titanium base material 10 described above, it is particularly excellent in conductivity and corrosion resistance, can suppress deterioration due to oxidation, and is used. The life can be greatly improved. Further, since it has excellent corrosion resistance, it can be used as a substitute for a noble metal electrode, and a water electrolysis electrode (anode electrode 32) can be configured at low cost.

また、本実施形態の水電解用電極（アノード極３２）において、２．５Ｖで１分保持及び０Ｖで１分保持を１サイクルとしたボルタンメトリー試験において、１２００サイクル後の電解効率が初期値に対して９０％以上である場合には、使用時における水電解用電極の劣化が確実に抑制されており、使用寿命を確実に向上させることが可能となる。 Further, in the voltammetry test in which the water electrolysis electrode (anode electrode 32) of the present embodiment has one cycle of holding at 2.5 V for 1 minute and holding at 0 V for 1 minute, the electrolysis efficiency after 1200 cycles is relative to the initial value. When it is 90% or more, deterioration of the water electrolysis electrode during use is surely suppressed, and it is possible to surely improve the use life.

本実施形態である水電解装置３０においては、上述したチタン基材１０で構成された水電解用電極をアノード極３２に用いているので、酸素ガスに晒される使用環境下においても、水電解用電極（アノード極３２）の酸化による劣化を抑えることができ、長期間安定して使用することが可能となる。また、耐食性に優れていることから、貴金属電極を用いる必要がなく、水電解装置３０の製造コストを大幅に削減することができる。さらに、チタン基材１０が上述した構造の多孔質体で構成されているので、水と酸素ガスを良好に流通させることが可能となる。 In the water electrolysis apparatus 30 of the present embodiment, since the water electrolysis electrode made of the titanium base material 10 described above is used for the anode electrode 32, it is used for water electrolysis even in a usage environment exposed to oxygen gas. Deterioration due to oxidation of the electrode (anode electrode 32) can be suppressed, and stable use can be achieved for a long period of time. Further, since it is excellent in corrosion resistance, it is not necessary to use a noble metal electrode, and the manufacturing cost of the water electrolyzer 30 can be significantly reduced. Further, since the titanium base material 10 is composed of the porous body having the above-mentioned structure, water and oxygen gas can be satisfactorily circulated.

以上、本発明の実施形態について説明したが、本発明はこれに限定されることはなく、その発明の技術的思想を逸脱しない範囲で適宜変更可能である。
例えば、本実施形態では、基材本体１１を多孔質体として説明したが、これに限定されることはなく、板、線、棒、管等の形状の基材本体１１であってもよい。また、基材本体１１がチタン焼結体で構成されたものとして説明したが、これに限定されることはなく、メッシュ板等を用いてもよい。 Although the embodiments of the present invention have been described above, the present invention is not limited to this, and can be appropriately changed without departing from the technical idea of the invention.
For example, in the present embodiment, the base material main body 11 has been described as a porous body, but the present invention is not limited to this, and the base material main body 11 in the shape of a plate, a wire, a rod, a tube, or the like may be used. Further, although the description is made assuming that the base material main body 11 is made of a titanium sintered body, the present invention is not limited to this, and a mesh plate or the like may be used.

また、本実施形態においては、マグネリ相酸化チタン皮膜は、Ｔｉ４Ｏ７及びＴｉ５Ｏ９の少なくも一方又は両方を含有するものとして説明したが、これに限定されることはなく、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンで構成されていればよい。
さらに、本実施形態においては、マグネリ相酸化チタン皮膜の膜厚を０．１μｍ以上３０μｍ以下の範囲内としたもので説明したが、これに限定されることはなく、マグネリ相酸化チタン皮膜の膜厚は、チタン基材への要求特性に応じて適宜設定することが好ましい。
また、本実施形態においては、マグネリ相酸化チタン皮膜は、ポーラス構造を有することと説明したが、これに限定されることはない。 Further, in the present embodiment, the magnetic phase titanium oxide film has been described as containing at least one or both of Ti 4 O 7 and Ti 5 O 9 , but the chemical formula Ti is not limited thereto. It suffices to be composed of titanium oxide in the magnety phase represented by n O 2n-1 (4 ≦ n ≦ 10).
Further, in the present embodiment, the film thickness of the magnetic phase titanium oxide film has been described as being within the range of 0.1 μm or more and 30 μm or less, but the present invention is not limited to this, and the film of the magnetic phase titanium oxide film is not limited to this. The thickness is preferably set as appropriate according to the required characteristics for the titanium substrate.
Further, in the present embodiment, it has been described that the magnetic phase titanium oxide film has a porous structure, but the present invention is not limited to this.

さらに、本実施形態では、図５に示す構造の水電解装置（水電解セル）を例に挙げて説明したが、これに限定されることはなく、本実施形態であるチタン基材からなる水電解用電極を備えていれば、その他の構造の水電解装置（水電解セル）であってもよい。 Further, in the present embodiment, the water electrolysis device (water electrolysis cell) having the structure shown in FIG. 5 has been described as an example, but the present invention is not limited to this, and water made of a titanium base material according to the present embodiment is used. As long as it is provided with an electrode for electrolysis, it may be a water electrolysis device (water electrolysis cell) having another structure.

（実施例１）
以下に、本発明の効果を確認すべく行った確認実験の結果について説明する。
まず、表１に示す基材本体を準備する。なお、表１において「チタン」は純度９９．９ｍａｓｓ％以上の純チタンとし、「チタン合金」はＴｉ－０．１５ｍａｓｓ％Ｐｄのチタン合金とした。
用意した各基材本体の寸法は、幅５０ｍｍ×長さ６０ｍｍ×厚さ０．３ｍｍとした。 (Example 1)
The results of the confirmation experiment conducted to confirm the effect of the present invention will be described below.
First, the base material main body shown in Table 1 is prepared. In Table 1, "titanium" was pure titanium having a purity of 99.9 mass% or more, and "titanium alloy" was a titanium alloy having Ti-0.15 mass% Pd.
The dimensions of each prepared base material were 50 mm in width × 60 mm in length × 0.3 mm in thickness.

次に、この基材本体の表面にＴｉＯ２皮膜を成膜する。Ｋ３ＰＯ４の水溶液中で、プラズマ電解酸化処理を施した。陰極として高密度カーボン板を用いて、温度１００℃以下、電圧４５０Ｖ、時間０～３００分の条件で実施した。なお、プラズマ電解酸化処理の時間を調整することで、ＴｉＯ２皮膜の膜厚を表１に示す値とした。 Next, a TiO 2 film is formed on the surface of the base material body. Plasma electrolytic oxidation treatment was performed in an aqueous solution of K 3 PO 4 . Using a high-density carbon plate as a cathode, the test was carried out under the conditions of a temperature of 100 ° C. or lower, a voltage of 450 V, and a time of 0 to 300 minutes. By adjusting the time of the plasma electrolytic oxidation treatment, the film thickness of the TiO 2 film was set to the value shown in Table 1.

次に、ＴｉＯ２皮膜を成膜した基材本体を、マイクロ波プラズマ還元装置に装入し、装置内を一度真空（３．８×１０－２ｔｏｒｒ（５Ｐａ）以下）まで減圧した。その後、装置内に水素ガスを導入して圧力を３０Ｐａとし、２．４５ＧＨｚのマイクロ波を照射した。還元時間が０．１～１５分とした。
なお、比較例１，３及び比較例７においては、還元処理を実施しなかった。また、比較例４，５においては、熱還元法によって還元処理を実施した。 Next, the main body of the base material on which the TIM 2 film was formed was charged into a microwave plasma reducing device, and the inside of the device was once depressurized to a vacuum (3.8 × 10-2 torr (5 Pa) or less). After that, hydrogen gas was introduced into the apparatus to set the pressure to 30 Pa, and the microwave was irradiated with 2.45 GHz. The reduction time was 0.1 to 15 minutes.
In Comparative Examples 1 and 3 and Comparative Example 7, the reduction treatment was not carried out. Further, in Comparative Examples 4 and 5, the reduction treatment was carried out by the thermal reduction method.

以上のようにして、チタンまたはチタン合金からなる基材本体の表面に、酸化チタン皮膜（本発明例では、マグネリ相酸化チタン皮膜）を成膜したチタン基材を得た。
得られたチタン基材について、酸化チタン皮膜の同定、酸化チタン皮膜の厚さ、導電性、耐食性を、以下のように評価した。 As described above, a titanium base material having a titanium oxide film (in the example of the present invention, a magnesium phase titanium oxide film) formed on the surface of a base material main body made of titanium or a titanium alloy was obtained.
For the obtained titanium substrate, the identification of the titanium oxide film, the thickness of the titanium oxide film, the conductivity, and the corrosion resistance were evaluated as follows.

（酸化チタン皮膜におけるチタン酸化物の同定）
Ｘ線回折分析（ＸＲＤ）法によって、酸化チタン皮膜のチタン酸化物を同定した。加速電圧を３０ｋｅＶとし、測定には８ｋｅＶのＣｕのＫａ線を用いた。測定範囲は２θ＝１５°～３５°とした。Ｔｉ４Ｏ７及びＴｉ５Ｏ９の存在の有無については、それぞれ２１°と２６°と３０°（Ｔｉ４Ｏ７）、２２°と２６°と２９°（Ｔｉ５Ｏ９）付近のいずれかでのピークの有無で確認した。評価結果を表２に示す。また、図６に、本発明例２及び比較例１のＸＲＤ分析結果を示す。 (Identification of titanium oxide in titanium oxide film)
The titanium oxide of the titanium oxide film was identified by the X-ray diffraction analysis (XRD) method. The acceleration voltage was 30 keV, and 8 keV Cu Ka line was used for the measurement. The measurement range was 2θ = 15 ° to 35 °. Regarding the presence or absence of Ti 4 O 7 and Ti 5 O 9 , either 21 °, 26 ° and 30 ° (Ti 4 O 7 ), 22 °, 26 ° and 29 ° (Ti 5 O 9 ), respectively. It was confirmed by the presence or absence of the peak in. The evaluation results are shown in Table 2. Further, FIG. 6 shows the XRD analysis results of Example 2 of the present invention and Comparative Example 1.

（酸化チタン皮膜の厚さ）
成膜後のサンプルを樹脂埋めし、酸化チタン皮膜の厚さ方向に対して垂直方向に切断して断面を露出させる。この断面をＳＥＭ観察し、倍率５０００倍で観察したＳＥＭ画像内に写る酸化チタン皮膜層の端から端までを均等に５点取り、それぞれ厚みを算出した。そして、測定した５点の平均値から酸化チタン皮膜の厚みを求めた。
基材本体を板材とした本発明例１のチタン基材の断面観察結果（ＳＥＭ画像）を図７に示す。
また、基材本体を多孔質体とした本発明例１１のチタン基材の断面観察結果（ＳＥＭ画像）を図８に示す。 (Thickness of titanium oxide film)
The sample after film formation is embedded in resin and cut in the direction perpendicular to the thickness direction of the titanium oxide film to expose the cross section. This cross section was observed by SEM, and 5 points were evenly scored from one end to the other of the titanium oxide film layer reflected in the SEM image observed at a magnification of 5000, and the thickness was calculated for each. Then, the thickness of the titanium oxide film was obtained from the average value of the five measured points.
FIG. 7 shows a cross-sectional observation result (SEM image) of the titanium base material of Example 1 of the present invention using the base material body as a plate material.
Further, FIG. 8 shows a cross-sectional observation result (SEM image) of the titanium base material of the present invention Example 11 in which the base material body is a porous body.

（導電性）
得られたチタン基材から、幅３０ｍｍ×長さ４０ｍｍ×厚さ０．３ｍｍの短冊状とした試験片を作成し、４探針法で導電率を測定した。導電率の測定値が１Ｓ／ｃｍ以上のものを「〇」、１Ｓ／ｃｍ未満のものを「×」と評価した。評価結果を表２に示す。 (Conductivity)
From the obtained titanium base material, a strip-shaped test piece having a width of 30 mm, a length of 40 mm, and a thickness of 0.3 mm was prepared, and the conductivity was measured by a 4-probe method. Those having a measured conductivity of 1 S / cm or more were evaluated as "◯", and those having a measured conductivity of less than 1 S / cm were evaluated as "x". The evaluation results are shown in Table 2.

（耐食性）
１Ｍの硫酸で満たした半径４ｃｍのセル中において、作成したチタン基材を作用極とし、コイル状のＰｔ線を対極として、サイクリックボルタンメトリー測定を行った。参照電極として用いたＡｇ／ＡｇＣｌ電極に対して０－２Ｖの間で掃引を繰り返した。サイクリックボルタンメトリーを１０００サイクル測定し、ＣＶの波形に変化が見られなかったものを「〇」、変化が認められたものを「×」と評価した。評価結果を表２に示す。 (Corrosion resistance)
Cyclic voltammetry measurement was performed in a cell filled with 1 M sulfuric acid and having a radius of 4 cm, using the prepared titanium base material as a working electrode and a coiled Pt wire as a counter electrode. Sweeping was repeated between 0-2V with respect to the Ag / AgCl electrode used as the reference electrode. Cyclic voltammetry was measured for 1000 cycles, and those in which no change was observed in the CV waveform were evaluated as "○", and those in which no change was observed were evaluated as "x". The evaluation results are shown in Table 2.

Figure 2022051582000001
Figure 2022051582000001

Figure 2022051582000002
Figure 2022051582000002

プラズマ電解酸化後の基材本体にマイクロ波プラズマ還元を施さなかった比較例１及び比較例７においては、マグネリ相酸化チタン皮膜が形成されておらず、導電性が不十分であった。このため、耐食性については評価しなかった。
プラズマ電解酸化の処理時間を１秒と短くしてＴｉＯ２皮膜の厚みを薄くし、その後マイクロ波プラズマ還元を実施した比較例２においては、マグネリ相酸化チタン皮膜が形成されておらず、かつ、酸化チタン皮膜の厚みが０．０１μｍと薄くなり、耐食性が不十分であった。プラズマ電解酸化では、０．１μｍ以下のＴｉＯ２皮膜を安定して成膜することができず、その後のマイクロ波プラズマ還元によってもマグネリ相酸化チタン皮膜が十分に形成されなかったためと推測される。 In Comparative Example 1 and Comparative Example 7 in which the main body of the substrate after plasma electrolytic oxidation was not subjected to microwave plasma reduction, the magnetic phase titanium oxide film was not formed, and the conductivity was insufficient. Therefore, the corrosion resistance was not evaluated.
In Comparative Example 2 in which the plasma electrolytic oxidation treatment time was shortened to 1 second to reduce the thickness of the TiO 2 film, and then microwave plasma reduction was performed, the magnetic phase titanium oxide film was not formed and the TIO 2 film was not formed. The thickness of the titanium oxide film was as thin as 0.01 μm, and the corrosion resistance was insufficient. It is presumed that the TiO 2 film of 0.1 μm or less could not be stably formed by plasma electrolytic oxidation, and the magnetic phase titanium oxide film was not sufficiently formed by the subsequent microwave plasma reduction.

大気酸化によってＴｉＯ２皮膜の成膜を試みた比較例３においては、処理温度を、４００℃を超える温度にする必要があった。このため、基材本体に酸素が拡散し、基材本体の劣化が認められた。よって、導電性、耐食性の評価を実施しなかった。
プラズマ電解酸化後の基材本体に対して真空中での熱還元を実施した比較例４，５においては、熱還元の処理温度を８００℃以上とする必要があった。このため、基材本体に酸素が拡散し、基材本体の劣化が認められた。よって、導電性、耐食性の評価を実施しなかった。 In Comparative Example 3 in which an attempt was made to form a TiO 2 film by atmospheric oxidation, the treatment temperature had to be set to a temperature exceeding 400 ° C. Therefore, oxygen diffused into the main body of the base material, and deterioration of the main body of the base material was observed. Therefore, the evaluation of conductivity and corrosion resistance was not carried out.
In Comparative Examples 4 and 5 in which heat reduction in vacuum was performed on the base material body after plasma electrolytic oxidation, it was necessary to set the heat reduction treatment temperature to 800 ° C. or higher. Therefore, oxygen diffused into the main body of the base material, and deterioration of the main body of the base material was observed. Therefore, the evaluation of conductivity and corrosion resistance was not carried out.

プラズマ電解酸化後の基材本体にマイクロ波プラズマ還元処理を温度６５０℃、処理時間３０分の条件で実施した比較例６においては、処理温度が高く、処理時間も長いため、目標とするマグネリ相酸化Ｔｉを得ることができなかった。また、わずかながら、比較例４、５と同様に、Ｔｉ基材本体への酸素拡散による基材の劣化も認められたため、導電性、耐食性の評価を実施しなかった。 In Comparative Example 6 in which the microwave plasma reduction treatment was carried out on the main body of the substrate after plasma electrolytic oxidation under the conditions of a temperature of 650 ° C. and a treatment time of 30 minutes, the treatment temperature was high and the treatment time was long, so that the target magnetic phase was achieved. Ti oxide could not be obtained. Further, as in Comparative Examples 4 and 5, the substrate was slightly deteriorated due to oxygen diffusion into the main body of the Ti substrate, so that the conductivity and corrosion resistance were not evaluated.

これに対して、マグネリ相酸化チタン皮膜が形成された本発明例１－１１においては、導電性、耐食性に優れていることが確認された。また、図７、８に示すように、本発明例１及び本発明例１１のチタン基材においては、マグネリ相酸化チタン皮膜がポーラス構造を有していることが確認された。さらに、図８に示すように、基材本体が多孔質体で構成された場合であっても、マグネリ相酸化チタン皮膜が基材本体の表面に比較的均一に形成されていることが確認された。 On the other hand, it was confirmed that in Example 1-11 of the present invention in which the magnetic phase titanium oxide film was formed, the conductivity and corrosion resistance were excellent. Further, as shown in FIGS. 7 and 8, it was confirmed that the magnesium phase titanium oxide film had a porous structure in the titanium substrates of the present invention Example 1 and the present invention Example 11. Further, as shown in FIG. 8, it was confirmed that the magnesium phase titanium oxide film was relatively uniformly formed on the surface of the base material body even when the base material body was composed of a porous body. rice field.

（実施例２）
次に、表３に示すように、マグネリ相酸化チタン皮膜が形成されたチタン基材（本発明例１１）及びマグネリ相酸化チタン皮膜ではない酸化チタン皮膜（絶縁性の酸化チタン皮膜）が形成されたチタン基材（比較例７）を、それぞれアノード極として用いて、図５に示す構造の固体高分子形の水電解セル（面積４ｃｍ×４ｃｍ）を構成し、本発明例１０１及び比較例１０１とした。
なお、比較例１０２では、多孔質体からなる基材本体の表面に酸化チタン皮膜を形成していないチタン基材をアノード極として用いた。 (Example 2)
Next, as shown in Table 3, a titanium substrate on which a magnesium phase titanium oxide film was formed (Example 11 of the present invention) and a titanium oxide film (insulating titanium oxide film) which was not a magnesium phase titanium oxide film were formed. Using the titanium base material (Comparative Example 7) as an anode electrode, a solid polymer type water electrolysis cell (area 4 cm × 4 cm) having the structure shown in FIG. 5 was formed, and the present invention example 101 and the comparative example 101 were formed. And said.
In Comparative Example 102, a titanium substrate having no titanium oxide film formed on the surface of the substrate body made of a porous body was used as the anode electrode.

この水電解セルに対して、２．５Ｖで１分保持及び０Ｖで１分保持を１サイクルとしたボルタンメトリー試験を実施した。水電解によりセルに流れた電流密度を測定した。なお、試験温度は８０℃とした。評価結果を表３に示す。
ここで、表３には、１０サイクル目の電流密度を初期値とし、この初期値を基準値（１．０）とし、各サイクル後の電流密度の初期値に対する比率を示した。 A voltammetry test was carried out on this water electrolysis cell with a cycle of holding at 2.5 V for 1 minute and holding at 0 V for 1 minute. The current density flowing through the cell by water electrolysis was measured. The test temperature was 80 ° C. The evaluation results are shown in Table 3.
Here, Table 3 sets the current density at the 10th cycle as the initial value, sets this initial value as the reference value (1.0), and shows the ratio of the current density after each cycle to the initial value.

Figure 2022051582000003
Figure 2022051582000003

マグネリ相酸化チタン皮膜ではない酸化チタン皮膜（絶縁性の酸化チタン皮膜）が形成されたチタン基材（比較例７）をアノード極として用いた比較例１０１においては、初期段階での電流密度が０．１Ａ／ｃｍ２以下と非常に低くなった。このため、ボルタンメトリー試験を実施しなかった。
また、多孔質体からなる基材本体の表面に酸化チタン皮膜を形成していないチタン基材をアノード極として用いた比較例１０２においては、電流密度が４００サイクル後で初期値の０．６５となり、１２００サイクル後では初期値の０．５９となった。アノード極（チタン基材）が酸化して劣化したためと推測される。 In Comparative Example 101 in which a titanium base material (Comparative Example 7) having a titanium oxide film (insulating titanium oxide film) formed instead of a magnetic phase titanium oxide film was used as an anode electrode, the current density at the initial stage was 0. It was very low, 1 A / cm 2 or less. Therefore, the voltammetry test was not performed.
Further, in Comparative Example 102 in which a titanium substrate having no titanium oxide film formed on the surface of the substrate body made of a porous body was used as the anode electrode, the current density became the initial value of 0.65 after 400 cycles. After 1200 cycles, the initial value was 0.59. It is presumed that the anode electrode (titanium base material) was oxidized and deteriorated.

これに対して、マグネリ相酸化チタン皮膜が形成されたチタン基材（本発明例１１）をアノード極として用いた本発明例１０１においては、電流密度が４００サイクル後で初期値の０．９７、８００サイクル後で初期値の１．０５、１２００サイクル後では初期値の０．９３となり、サイクル数が増加しても初期値から大きく変化しなかった。アノード極（チタン基材）の酸化による劣化が抑制されたためと推測される。 On the other hand, in Example 101 of the present invention in which the titanium base material (Example 11 of the present invention) on which the magnesium oxide film was formed was used as the anode electrode, the current density was 0.97, which was the initial value after 400 cycles. After 800 cycles, the initial value was 1.05, and after 1200 cycles, the initial value was 0.93, and even if the number of cycles increased, there was no significant change from the initial value. It is presumed that the deterioration of the anode electrode (titanium base material) due to oxidation was suppressed.

以上の実験結果から、本発明例によれば、導電性及び耐食性に特に優れ、過酷な腐食環境下においても使用可能なチタン基材、チタン基材の製造方法、及び、このチタン基材からなる水電解用電極、水電解装置を提供可能であることが確認された。 From the above experimental results, according to the example of the present invention, it is composed of a titanium base material which is particularly excellent in conductivity and corrosion resistance and can be used even in a harsh corrosion environment, a method for producing a titanium base material, and this titanium base material. It was confirmed that it is possible to provide electrodes for water electrolysis and water electrolysis equipment.

１０ チタン基材
１１ 基材本体
１６ マグネリ相酸化チタン皮膜
２６ ＴｉＯ２皮膜
３０ 水電解装置
３２ アノード極（水電解用電極） 10 Titanium base material 11 Base material body 16 Magneti phase Titanium oxide film 26 TIO 2 film 30 Water electrolyzer 32 Anode electrode (electrode for water electrolysis)

Claims (7)

チタンまたはチタン合金からなる基材本体を有し、
この基材本体の表面に、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜が形成されており、
前記マグネリ相酸化チタン皮膜は、Ｔｉ４Ｏ７及びＴｉ５Ｏ９の少なくも一方又は両方を含有し、前記マグネリ相酸化チタン皮膜は、ナノメートルオーダー又はマイクロメートルオーダーのポーラス構造を有し、
前記マグネリ相酸化チタン皮膜のＸ線回折におけるＴｉ４Ｏ７及びＴｉ５Ｏ９の最大ピーク強度の和が他のマグネリ相酸化チタンの最大ピーク強度よりも大きく、
導電率が１Ｓ／ｃｍ以上であることを特徴とするチタン基材。 It has a base material body made of titanium or titanium alloy and has a base material body.
A magnesium phase titanium oxide film made of titanium oxide having a magnesium phase represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) is formed on the surface of the base material body.
The magnetic phase titanium oxide film contains at least one or both of Ti 4 O 7 and Ti 5 O 9 , and the magnetic phase titanium oxide film has a porous structure on the order of nanometers or micrometer.
The sum of the maximum peak intensities of Ti 4 O 7 and Ti 5 O 9 in the X-ray diffraction of the magnetic phase titanium oxide film is larger than the maximum peak intensities of other magnetic phase titanium oxides.
A titanium base material having a conductivity of 1 S / cm or more. 前記マグネリ相酸化チタン皮膜の膜厚が０．１μｍ以上３０μｍ以下の範囲内とされていることを特徴とする請求項１に記載のチタン基材。 The titanium base material according to claim 1, wherein the thickness of the magnetic phase titanium oxide film is in the range of 0.1 μm or more and 30 μm or less. 前記基材本体は、気孔率が３０％以上９７％以下の範囲内とされた多孔質体とされていることを特徴とする請求項１又は請求項２に記載のチタン基材。 The titanium base material according to claim 1 or 2, wherein the base material body is a porous body having a porosity in the range of 30% or more and 97% or less. 請求項１から請求項３のいずれか一項に記載のチタン基材の製造方法であって、
チタンまたはチタン合金からなる基材本体の表面にＴｉＯ２皮膜を成膜するＴｉＯ２皮膜形成工程と、
前記基材本体の表面に形成されたＴｉＯ２皮膜をマイクロ波プラズマ還元法によって還元し、化学式ＴｉｎＯ２ｎ－１（４≦ｎ≦１０）で表されるマグネリ相酸化チタンからなるマグネリ相酸化チタン皮膜とする還元処理工程と、
を備えており、
還元処理工程は、基板温度４００℃以下、処理時間１５分以下の条件で実施することを特徴とするチタン基材の製造方法。 The method for producing a titanium base material according to any one of claims 1 to 3.
A TiO 2 film forming step of forming a TiO 2 film on the surface of a base material made of titanium or a titanium alloy, and
The TiO 2 film formed on the surface of the base material body is reduced by a microwave plasma reduction method, and the magnesium phase oxidation represented by the chemical formula Tin O 2n-1 (4 ≦ n ≦ 10) is composed of titanium oxide. The reduction treatment process to make a titanium film and
Equipped with
A method for producing a titanium base material, wherein the reduction treatment step is carried out under the conditions of a substrate temperature of 400 ° C. or lower and a treatment time of 15 minutes or less. 請求項１から請求項３のいずれか一項に記載のチタン基材からなることを特徴とする水電解用電極。 An electrode for water electrolysis, which comprises the titanium base material according to any one of claims 1 to 3. ２．５Ｖで１分保持及び０Ｖで１分保持を１サイクルとしたボルタンメトリー試験において、１２００サイクル後の電解効率が初期値に対して９０％以上１００％未満であることを特徴とする請求項５に記載の水電解用電極。 Claim 5 is characterized in that the electrolysis efficiency after 1200 cycles is 90% or more and less than 100% with respect to the initial value in the voltammetry test in which the holding for 1 minute at 2.5 V and the holding for 1 minute at 0 V are one cycle. The electrode for water electrolysis described in. 請求項５又は請求項６に記載の水電解用電極を備えたことを特徴とする水電解装置。 A water electrolysis apparatus comprising the electrode for water electrolysis according to claim 5 or 6.
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