AU2012210549A1 - Electrode for oxygen evolution in industrial electrochemical processes - Google Patents
Electrode for oxygen evolution in industrial electrochemical processesInfo
- Publication number
- AU2012210549A1 AU2012210549A1 AU2012210549A AU2012210549A AU2012210549A1 AU 2012210549 A1 AU2012210549 A1 AU 2012210549A1 AU 2012210549 A AU2012210549 A AU 2012210549A AU 2012210549 A AU2012210549 A AU 2012210549A AU 2012210549 A1 AU2012210549 A1 AU 2012210549A1
- Authority
- AU
- Australia
- Prior art keywords
- tantalum
- oxides
- iridium
- electrode according
- electrode
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Description
ELECTRODE FOR OXYGEN EVOLUTION IN INDUSTRIAL ELECTROCHEMICAL
PROCESSES
FIELD OF THE INVENTION
The invention relates to an electrode suitable for operating as anode in electrochemical cells, for instance as oxygen-evolving anode in electrolysis cells for electrometallurgical processes. BACKGROUND OF THE INVENTION
The invention relates to an electrode for use in industrial electrochemical processes, for instance in electrolytic applications contemplating the evolution of oxygen at the anode. Anodes for oxygen evolution are widely used in different electrolysis applications, several of which pertain to the field of electrometallurgy, covering a wide range in terms of applied current density, which can be very reduced (for instance a few hundred A/m2, such as the case of electrowinning processes) or also very high (for instance in high speed electroplating, which can operate in excess of 10 kA/m2, referred to the anodic surface); another field of application of oxygen-evolving anodes is cathodic protection under impressed current. Electrodes suitable for anodic evolution of oxygen can be obtained starting from substrates of valve metals, for instance titanium and alloys thereof, coated with catalytic compositions based on transition metals or oxides thereof, characterised by their capability of lowering the overvoltage of the oxygen anodic discharge reaction, which is much too high to allow the execution of industrial processes in the absence of catalytic systems. A composition suitable for catalysing the anodic oxygen evolution reaction for instance consists of a mixture of oxides of iridium and of tantalum, wherein iridium plays the role of catalytically active species and tantalum facilitates the formation of a compact coating, capable of protecting the valve metal substrate from corrosion phenomena, especially when operating with aggressive electrolytes. An anode formulation suitable for anodic oxygen evolution in many industrial electrochemical processes comprises a titanium substrate and a catalytic coating consisting of oxides of iridium and tantalum with a molar composition referred to the metals of 65% Ir and 35% Ta. In some cases, for instance to be able to operate with
very acidic or otherwise corrosive electrolytes, it can be advantageous to interpose an intermediate protective layer between titanium substrate and catalytic coating, for instance consisting of titanium and tantalum oxides with a molar composition of 80% Ti and 20% Ta referred to the metals. This type of electrodes can be prepared in different ways, for example by thermal decomposition of a precursor solution at high
temperature, for instance 400 to 600°C. Electrodes with the above specified
composition can satisfy the needs of several industrial applications, both at low and at high current density, with reasonable operative lifetimes. The economy of some manufacturing processes, especially in the field of metallurgy (for instance copper deposition in galvanic processes for the production of printed circuits and copper foil) nevertheless requires electrodes of increasingly high duration, combined with a suitably reduced oxygen evolution potential even at high current density: the potential of oxygen evolution is in fact one of the main factors determining the process operative voltage and thus the overall energy consumption. Moreover, the operative lifetime of anodes based on noble metals or oxides thereof on valve metal substrates is remarkably reduced in the presence of particularly aggressive contaminants, which can establish accelerated phenomena of corrosion or of anode surface pollution. It has therefore been evidenced the need for oxygen-evolving anodes characterised by a low oxygen evolution overpotential and by higher operative lifetimes even in particularly critical process conditions, such as a high current density or the presence of particularly aggressive electrolytes, for instance due to the presence of contaminant species.
SUMMARY OF THE INVENTION Various aspects of the invention are set out in the accompanying claims.
In one embodiment, the present invention relates to an electrode for oxygen evolution in electrochemical processes comprising a valve metal substrate, a catalytic coating comprising an internal layer of oxides of iridium and tantalum of molar composition Ir 60-70%, Ta 30-40% referred to the metals and an external coating containing 2 to 7
For the purpose of the invention, by valve metal oxide it is intended herein a metal which, when oxidized, allows current to pass if used as a cathode but opposes the flow of current when used as an anode, according to the definition set forth in US 6,287,673. Examples of valve metals include magnesium, thorium, cadmium, tungsten, tin, iron, silver, silicon, tantalum, titanium, aluminium, zirconium and niobium.
In one embodiment, the external coating consists of a single valve metal oxide. This can have the advantage of preserving the valve metal behaviour of the external layer, since the interaction of the valve metal of the external layer with another element of different valence could bring about a doping effect and hamper the opposition to the anodic current flow.
The inventors have surprisingly observed that the addition of an external coating of valve metal oxides at the specified loading is capable of remarkably increasing the duration of an electrode used for anodic evolution of oxygen, meanwhile improving its tolerance to the presence of contaminating species, with little effect on the oxygen evolution potential.
In one embodiment, the catalytic coating consists of multiple layers and comprises also a second intermediate layer of oxides of iridium, tantalum and titanium of molar composition Ir 76-84%, Ta 15-23%, Ti 0.2-1 .3% referred to the metals, interposed between the first catalytic layer and the external layer. This can have the advantage of further enhancing the electrode duration. In one embodiment, the valve metal oxides of the external layer are oxides of tantalum or of tin or of zirconium.
In one embodiment, the specific loading of iridium in the catalytic layer is 5 to 50 g/m2. In one embodiment the specific loading of oxides in the external layer of the catalytic layer according to the invention is 2.9 to 3.5 g/m2. This can have the advantage of ensuring that the effect on the oxygen evolution potential becomes negligible or nil.
In one embodiment the electrode comprises an intermediate protection layer based on oxides of titanium or of tantalum interposed between the substrate and the catalytic coating. Under another aspect, the invention relates to a method of manufacturing of an electrode with the above described characteristics, comprising the formation of an external layer having a composition as hereinbefore described, by application and subsequent thermal decomposition of a solution containing a precursor of tantalum or tin or zirconium.
Under another aspect, the invention relates to an industrial electrochemical process comprising the anodic evolution of oxygen from an electrolytic bath on an electrode having the above described characteristics. Some of the most significant results obtained by the inventors are presented in the following examples, which are not intended as a limitation of the domain of the invention.
EXAMPLE 1
A titanium sheet grade 1 of 200 x 200 x 3 mm size was degreased and subjected first to sandblasting with iron grit until obtaining a value of superficial roughness Rz of 70 to 100 μηπ, then to etching in 20% by weight HCI at a temperature of 90-100°C for 20 minutes.
After drying, a protective layer based on titanium and tantalum oxides at a 80:20 weight ratio was applied to the sheet, with an overall loading of 0.6 g/m2 referred to the metals (equivalent to 0.87 g/m2 referred to the oxides). The application of the protective layer was carried out by painting in three coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4 - and subsequent thermal decomposition at 500°C.
A catalytic coating based on oxides of iridium and tantalum at a 65:35 weight ratio (equivalent to a molar ratio of about 66.3:36.7) was then applied on the protective layer, with an overall loading of iridium of 10 g/m2. The electrode was thermally treated for 2 h at 515°C, then the application of the external coating (3 g/m2 referred to the oxides) was carried out by painting in 2 coats of an aqueous solution of TaCI5, acidified with HCI.
Three samples of 1 cm2 surface were cut out from the thus obtained electrode and submitted to an accelerated lifetime test under anodic oxygen evolution, measuring the deactivation time (defined as the operating time required to observe a potential increase of 1 V) in H2S04 at 150 g/l, at a temperature of 60°C and at a current density of 30 kA/m2. The average deactivation time for the three samples was 1370 hours. EXAMPLE 2
A titanium sheet grade 1 of 200 x 200 x 3 mm size was degreased and subjected first to sandblasting with iron grit until obtaining a value of superficial roughness Rz of 70 to 100 μηπ, then to etching in 20% by weight HCI at a temperature of 90-100°C for 20 minutes.
After drying, a protective layer based on titanium and tantalum oxides at a 80:20 weight ratio was applied to the sheet, with an overall loading of 0.6 g/m2 referred to the metals (equivalent to 0.87 g/m2 referred to the oxides). The application of the protective layer was carried out by painting in three coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4 - and subsequent thermal decomposition at 500°C.
A catalytic coating based on oxides of iridium and tantalum at a 65:35 weight ratio (equivalent to a molar ratio of about 66.3:36.7) was then applied on the protective layer, with an overall loading of iridium of 10 g/m2. The electrode was thermally treated for 2 h
at 515°C, then the application of the external coating (3.4 g/m2 referred to the oxides) was carried out by painting in 2 coats of a 0.9 M acetic solution of Sn.
Three samples of 1 cm2 surface were cut out from the thus obtained electrode and submitted to an accelerated lifetime test under anodic oxygen evolution, measuring the deactivation time (defined as the operating time required to observe a potential increase of 1 V) in H2S04 at 150 g/l, at a temperature of 60°C and at a current density of 30 kA/m2. The average deactivation time for the three samples was 1440 hours. EXAMPLE 3
A titanium sheet grade 1 of 200 x 200 x 3 mm size was degreased and subjected first to sandblasting with iron grit until obtaining a value of superficial roughness Rz of 70 to 100 μηπ, then to etching in 20% by weight HCI at a temperature of 90-100°C for 20 minutes.
After drying, a protective layer based on titanium and tantalum oxides at a 80:20 weight ratio was applied to the sheet, with an overall loading of 0.6 g/m2 referred to the metals (equivalent to 0.87 g/m2 referred to the oxides). The application of the protective layer was carried out by painting in three coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4 - and subsequent thermal decomposition at 500°C.
A catalytic coating consisting of two distinct layers was then applied on the protective layer: a first (internal) layer based on oxides of iridium and tantalum in a 65:35 weight ratio (equivalent to a molar ratio of about 66.3:36.7), with an overall loading of iridium of 2 g/m2, and a second (external) layer based on oxides of iridium, tantalum and titanium, at a 78:20:2 weight ratio (corresponding to a molar ratio of about 80.1 : 19.4:0.5), with an overall loading of iridium of 10 g/m2.
The application of the internal catalytic layer was carried out by painting in 2 coats of a precursor solution - obtained by addition of H2lrCI6 to an aqueous TaCI5 solution, until reaching an Ir concentration of 76 g/l - and subsequent thermal decomposition at 520°C.
The application of the external catalytic layer was carried out by painting in 4 coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4, then of H2lrCI6 until reaching an Ir concentration of 195 g/l - and subsequent thermal decomposition at 480°C. The electrode was thermally treated for 2 h at 515°C, then the application of the external coating (3 g/m2 referred to the oxides) was carried out by painting in 2 coats of an aqueous solution of TaCI5, acidified with HCI.
Three samples of 10 cm2 surface were cut out from the thus obtained electrode and submitted to an accelerated lifetime test under anodic oxygen evolution, measuring the deactivation time (defined as the operating time required to observe a potential increase of 1 V) in H2S04 at 150 g/l, at a temperature of 60°C and at a current density of 30 kA/m2. The average deactivation time for the three samples was 2420 hours. EXAMPLE 4
A titanium sheet grade 1 of 200 x 200 x 3 mm size was degreased and subjected first to sandblasting with iron grit until obtaining a value of superficial roughness Rz of 70 to 100 μηπ, then to etching in 20% by weight HCI at a temperature of 90-100°C for 20 minutes.
After drying, a protective layer based on titanium and tantalum oxides at a 80:20 weight ratio was applied to the sheet, with an overall loading of 0.6 g/m2 referred to the metals (equivalent to 0.87 g/m2 referred to the oxides). The application of the protective layer was carried out by painting in three coats of a precursor solution - obtained by addition
of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4 - and subsequent thermal decomposition at 500°C.
A catalytic coating consisting of two distinct layers was then applied on the protective layer: a first (internal) layer based on oxides of iridium and tantalum in a 65:35 weight ratio (equivalent to a molar ratio of about 66.3:36.7), with an overall loading of iridium of 2 g/m2, and a second (external) layer based on oxides of iridium, tantalum and titanium, at a 78:20:2 weight ratio (corresponding to a molar ratio of about 80.1 : 19.4:0.5), with an overall loading of iridium of 10 g/m2.
The application of the internal catalytic layer was carried out by painting in 2 coats of a precursor solution - obtained by addition of H2lrCI6 to an aqueous TaCI5 solution, until reaching an Ir concentration of 76 g/l - and subsequent thermal decomposition at 520°C.
The application of the external catalytic layer was carried out by painting in 4 coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4, then of H2lrCI6 until reaching an Ir concentration of 195 g/l - and subsequent thermal decomposition at 480°C. The electrode was thermally treated for 2 h at 515°C, then the application of the external coating (3.4 g/m2 referred to the oxides) was carried out by painting in 2 coats of a 0.9 M acetic solution of Sn.
Three samples of 10 cm2 surface were cut out from the thus obtained electrode and submitted to an accelerated lifetime test under anodic oxygen evolution, measuring the deactivation time (defined as the operating time required to observe a potential increase of 1 V) in H2S04 at 150 g/l, at a temperature of 60°C and at a current density of 30 kA/m2. The average deactivation time for the three samples was 1800 hours.
COUNTEREXAMPLE 1
A titanium sheet grade 1 of 200 x 200 x 3 mm size was degreased and subjected first to sandblasting with iron grit until obtaining a value of superficial roughness Rz of 70 to 100 μηπ, then to etching in 20% by weight HCI at a temperature of 90-100°C for 20 minutes.
After drying, a protective layer based on titanium and tantalum oxides at a 80:20 weight ratio was applied to the sheet, with an overall loading of 0.6 g/m2 referred to the metals (equivalent to 0.87 g/m2 referred to the oxides). The application of the protective layer was carried out by painting in three coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4 - and subsequent thermal decomposition at 500°C.
A catalytic coating based on oxides of iridium and tantalum at a 65:35 weight ratio (equivalent to a molar ratio of about 66.3:36.7) was then applied on the protective layer, with an overall loading of iridium of 10 g/m2.
Three samples of 1 cm2 surface were cut out from the thus obtained electrode and submitted to an accelerated lifetime test under anodic oxygen evolution, measuring the deactivation time (defined as the operating time required to observe a potential increase of 1 V) in H2S04 at 150 g/l, at a temperature of 60°C and at a current density of 30 kA/m2.
The average deactivation time for the three samples was 660 hours. COUNTEREXAMPLE 2
A titanium sheet grade 1 of 200 x 200 x 3 mm size was degreased and subjected first to sandblasting with iron grit until obtaining a value of superficial roughness Rz of 70 to 100 μηπ, then to etching in 20% by weight HCI at a temperature of 90-100°C for 20 minutes.
After drying, a protective layer based on titanium and tantalum oxides at a 80:20 weight ratio was applied to the sheet, with an overall loading of 0.6 g/m2 referred to the metals (equivalent to 0.87 g/m2 referred to the oxides). The application of the protective layer
was carried out by painting in three coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4 - and subsequent thermal decomposition at 500°C. A catalytic coating consisting of two distinct layers was then applied on the protective layer: a first (internal) layer based on oxides of iridium and tantalum in a 65:35 weight ratio (equivalent to a molar ratio of about 66.3:36.7), with an overall loading of iridium of 2 g/m2, and a second (external) layer based on oxides of iridium, tantalum and titanium, at a 78:20:2 weight ratio (corresponding to a molar ratio of about 80.1 : 19.4:0.5), with an overall loading of iridium of 10 g/m2.
The application of the internal catalytic layer was carried out by painting in 2 coats of a precursor solution - obtained by addition of H2lrCI6 to an aqueous TaCI5 solution, until reaching an Ir concentration of 76 g/l - and subsequent thermal decomposition at 520°C.
The application of the external catalytic layer was carried out by painting in 4 coats of a precursor solution - obtained by addition of an aqueous TaCI5 solution, acidified with HCI, to an aqueous solution of TiCI4, then of H2lrCI6 until reaching an Ir concentration of 195 g/l - and subsequent thermal decomposition at 480°C.
Three samples of 10 cm2 surface were cut out from the thus obtained electrode and submitted to an accelerated lifetime test under anodic oxygen evolution, measuring the deactivation time (defined as the operating time required to observe a potential increase of 1 V) in H2S04 at 150 g/l, at a temperature of 60°C and at a current density of 30 kA/m2.
The average deactivation time for the three samples was 1320 hours. The previous description shall not be intended as limiting the invention, which may be used according to different embodiments without departing from the scopes thereof, and whose extent is univocally defined by the appended claims.
Throughout the description and claims of the present application, the term "comprise" and variations thereof such as "comprising" and "comprises" are not intended to exclude the presence of other elements or additives. The discussion of documents, acts, materials, devices, articles and the like is included in this specification solely for the purpose of providing a context for the present invention. It is not suggested or represented that any or all of these matters formed part of the prior art base or were common general knowledge in the field relevant to the present invention before the priority date of each claim of this application.
Claims (1)
- Electrode for oxygen evolution in electrochemical processes comprising a valve metal substrate, a catalytic coating comprising a first layer of oxides of iridium and tantalum having a molar composition Ir 60-70%, Ta 30-40% referred to the metals and an external coating containing 2 to 7 g/m2 of a valve metal oxide.The electrode according to claim 1 wherein said external coating consists of 2.9 to 3.5 g/m2 of a valve metal oxide selected between tantalum oxide, tin oxide and zirconium oxide.The electrode according to claim 1 or 2 wherein said catalytic coating further comprises a second layer of oxides of iridium, tantalum and titanium having a molar composition Ir 76-84%, Ta 1 5-23%, Ti 0.2-1 .3% referred to the metals interposed between said first catalytic layer and said external coating.The electrode according to claim 1 wherein said valve metal oxide is selected from the group consisting of tantalum oxide, tin oxide and zirconium oxide.The electrode according to any one of claims 1 to 4 wherein said catalytic coating has a specific loading of iridium of 5 to 50 g/m2.The electrode according to any one of claims 1 to 5 comprising an intermediate protective layer based on oxides of titanium or tantalum interposed between said substrate and said catalytic coating.The electrode according to claim 6 wherein said catalytic coating has a specific loading of iridium of 8 to 15 g/m2. Method of manufacturing an electrode according to any one of claims 1 to 7 comprising the formation of said external coating by application and subsequent thermal decomposition of a solution containing a precursor of tantalum or tin or zirconium.Industrial electrochemical process comprising the anodic evolution of oxygen from an electrolytic bath on an electrode according to any one of claims 1 to 7.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT000089A ITMI20110089A1 (en) | 2011-01-26 | 2011-01-26 | ELECTRODE FOR EVOLUTION OF OXYGEN IN INDUSTRIAL ELECTROCHEMICAL PROCESSES |
| ITMI2011A000089 | 2011-01-26 | ||
| PCT/EP2012/051079 WO2012101141A1 (en) | 2011-01-26 | 2012-01-25 | Electrode for oxygen evolution in industrial electrochemical processes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU2012210549A1 true AU2012210549A1 (en) | 2013-08-08 |
| AU2012210549B2 AU2012210549B2 (en) | 2017-05-04 |
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ID=43975424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2012210549A Active AU2012210549B2 (en) | 2011-01-26 | 2012-01-25 | Electrode for oxygen evolution in industrial electrochemical processes |
Country Status (18)
| Country | Link |
|---|---|
| US (1) | US20130306489A1 (en) |
| EP (1) | EP2668315B1 (en) |
| JP (1) | JP5918273B2 (en) |
| KR (1) | KR101789358B1 (en) |
| CN (1) | CN103328689B (en) |
| AR (1) | AR084772A1 (en) |
| AU (1) | AU2012210549B2 (en) |
| BR (1) | BR112013018556B1 (en) |
| CA (1) | CA2824815C (en) |
| EA (1) | EA023880B1 (en) |
| HK (1) | HK1187963A1 (en) |
| IT (1) | ITMI20110089A1 (en) |
| MX (1) | MX354202B (en) |
| MY (1) | MY176682A (en) |
| PL (1) | PL2668315T3 (en) |
| SG (2) | SG10201510610RA (en) |
| TW (1) | TWI579410B (en) |
| WO (1) | WO2012101141A1 (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ITMI20122035A1 (en) * | 2012-11-29 | 2014-05-30 | Industrie De Nora Spa | ELECTRODE FOR EVOLUTION OF OXYGEN IN INDUSTRIAL ELECTROCHEMICAL PROCESSES |
| KR102433461B1 (en) * | 2014-10-21 | 2022-08-17 | 에보쿠아 워터 테크놀로지스 엘엘씨 | Electrode with two layer coating, method of use, and preparation thereof |
| ES2792910T3 (en) | 2014-11-10 | 2020-11-12 | Nat Univ Corp Yokohama Nat Univ | Oxygen Generating Anode |
| EA034359B1 (en) * | 2015-06-23 | 2020-01-30 | Индустрие Де Нора С.П.А. | Electrode for electrolytic processes |
| CN106367779A (en) * | 2016-11-07 | 2017-02-01 | 南昌专腾科技有限公司 | Titanium-based porous electrode material and preparation method thereof |
| CN107829109B (en) * | 2017-10-20 | 2019-09-27 | 上海同臣环保有限公司 | A kind of titanium-based iridium dioxide coated electrode and preparation method thereof |
| US20210198792A1 (en) * | 2018-08-22 | 2021-07-01 | The University Of North Carolina At Greensboro | Compositions and methods for enhancing electrocatalytic efficiencies |
| CN112553657B (en) * | 2019-09-10 | 2023-06-02 | 马赫内托特殊阳极（苏州）有限公司 | Electrode and preparation method and application thereof |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6022075B2 (en) * | 1983-01-31 | 1985-05-30 | ペルメレック電極株式会社 | Durable electrolytic electrode and its manufacturing method |
| IT1208128B (en) * | 1984-11-07 | 1989-06-06 | Alberto Pellegri | ELECTRODE FOR USE IN ELECTROCHEMICAL CELLS, PROCEDURE FOR ITS PREPARATION AND USE IN THE ELECTROLYSIS OF DISODIUM CHLORIDE. |
| US5156726A (en) * | 1987-03-24 | 1992-10-20 | Tdk Corporation | Oxygen-generating electrode and method for the preparation thereof |
| US5314601A (en) * | 1989-06-30 | 1994-05-24 | Eltech Systems Corporation | Electrodes of improved service life |
| JPH0499294A (en) * | 1990-08-09 | 1992-03-31 | Daiso Co Ltd | Oxygen generating anode and its production |
| KR100196094B1 (en) * | 1992-03-11 | 1999-06-15 | 사토 히로시 | Oxygen generating electrode |
| JP3152499B2 (en) * | 1992-04-14 | 2001-04-03 | ティーディーケイ株式会社 | Electrode for oxygen generation and method for producing the same |
| JP3653296B2 (en) * | 1995-01-23 | 2005-05-25 | 石福金属興業株式会社 | Electrode for electrolysis and method for producing the same |
| US6287673B1 (en) | 1998-03-03 | 2001-09-11 | Acktar Ltd. | Method for producing high surface area foil electrodes |
| JP3810043B2 (en) * | 1998-09-30 | 2006-08-16 | ペルメレック電極株式会社 | Chrome plating electrode |
| US6527939B1 (en) * | 1999-06-28 | 2003-03-04 | Eltech Systems Corporation | Method of producing copper foil with an anode having multiple coating layers |
| US6589405B2 (en) * | 2000-05-15 | 2003-07-08 | Oleh Weres | Multilayer oxide coated valve metal electrode for water purification |
| ITMI20021128A1 (en) * | 2002-05-24 | 2003-11-24 | De Nora Elettrodi Spa | ELECTRODE FOR GAS DEVELOPMENT AND METHOD FOR ITS OBTAINING |
| AU2006303991A1 (en) * | 2005-10-12 | 2007-04-26 | Go Green Fuel N.A., L.P. | Internal combustion apparatus and method utilizing electrolysis cell |
-
2011
- 2011-01-26 IT IT000089A patent/ITMI20110089A1/en unknown
- 2011-11-25 TW TW100143218A patent/TWI579410B/en active
-
2012
- 2012-01-03 AR ARP120100011A patent/AR084772A1/en active IP Right Grant
- 2012-01-25 CA CA2824815A patent/CA2824815C/en active Active
- 2012-01-25 PL PL12701115T patent/PL2668315T3/en unknown
- 2012-01-25 KR KR1020137022422A patent/KR101789358B1/en active IP Right Grant
- 2012-01-25 WO PCT/EP2012/051079 patent/WO2012101141A1/en active Application Filing
- 2012-01-25 BR BR112013018556-2A patent/BR112013018556B1/en active IP Right Grant
- 2012-01-25 SG SG10201510610RA patent/SG10201510610RA/en unknown
- 2012-01-25 CN CN201280006534.4A patent/CN103328689B/en active Active
- 2012-01-25 AU AU2012210549A patent/AU2012210549B2/en active Active
- 2012-01-25 MX MX2013008525A patent/MX354202B/en active IP Right Grant
- 2012-01-25 EP EP12701115.3A patent/EP2668315B1/en active Active
- 2012-01-25 JP JP2013550860A patent/JP5918273B2/en active Active
- 2012-01-25 EA EA201391083A patent/EA023880B1/en unknown
- 2012-01-25 SG SG2013051172A patent/SG191424A1/en unknown
- 2012-01-25 MY MYPI2013002781A patent/MY176682A/en unknown
- 2012-01-25 US US13/981,383 patent/US20130306489A1/en not_active Abandoned
-
2014
- 2014-01-29 HK HK14100948.7A patent/HK1187963A1/en unknown
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