CN202936494U - Titanium-based lead dioxide anode plate - Google Patents
Titanium-based lead dioxide anode plate Download PDFInfo
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- CN202936494U CN202936494U CN 201220680503 CN201220680503U CN202936494U CN 202936494 U CN202936494 U CN 202936494U CN 201220680503 CN201220680503 CN 201220680503 CN 201220680503 U CN201220680503 U CN 201220680503U CN 202936494 U CN202936494 U CN 202936494U
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- titanium
- lead dioxide
- anode plate
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- oxide
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Abstract
The utility model provides a titanium-based lead dioxide anode plate which comprises a titanium material-based material, wherein a ruthenium and iridium oxide coating, a tin and antimony oxide coating, and an alpha lead dioxide film as well as a beta lead dioxide film are sequentially coated on the surface of the titanium-based material. According to the titanium-based lead dioxide anode plate, the film binding force of the titanium-based lead dioxide is improved, oxygen overpotential is improved, the oxidizing ability of the anode surface is improved, and organic matter can be directly oxidized and degraded on the anode surface, so that the organic matter in sewage can be directly or indirectly converted into CO2 and water through electrochemistry conversion, in the process, the environment is not polluted, so that the sewage is disposed in an environment-friendly manner; and furthermore, the corrosion resistance of a titanium substrate is improved, titanium dioxide with poor electric conductivity is prevented from being formed on the surface of the titanium substrate, and the conductivity of the anode plate is improved.
Description
Technical field
The utility model relates to a kind of ti-lead dioxide anode plate.
Background technology
Along with the development of industry and science and technology, traditional anode material more and more has limitation.For example: the platinum cost is too high, and graphite solidity to corrosion in chlorine industry is poor, and intensity is less; Alloy lead anode solidity to corrosion and conductivity are relatively poor, and energy consumption is larger.From energy-conservation, consumption reduction, so-called " green material " requirements such as pollution-free, we more need energy-conservation, the free of contamination type material anode of catalytic activity height.
The utility model content
The technical problem that the utility model solves: a kind of ti-lead dioxide anode plate is provided, first apply the transition layer that is formed by ruthenium and iridium oxide on the titanium base material, purpose is the passivation that overcomes Ti matrix in long-time electrolysis production process, strengthen the bonding force of PbO2 coating and matrix, prevent that coating from coming off, improve job stability and the work-ing life of PbO2 electrode, and the electroconductibility that improves electrode.Then apply the active layer that is comprised of tin and sb oxide on transition layer, electrolytic solution is difficult to be penetrated into titanium surface, Sauerstoffatom or O again
2-Ion also has been subject to stopping to the diffusion of titanium matrix, thereby has avoided TiO
2Generation.Plating middle layer α lead dioxide plating coat on active layer can strengthen the firmness of lead dioxide plating coat and electrode matrix combination, the generation of mitigation electrodeposition distortion, can also make β-PbO
2Be evenly distributed.
The technical solution adopted in the utility model: the ti-lead dioxide anode plate, have the titanium base material, described titanium substrate surface scribbles ruthenium and iridium oxide coating, tin and antimony oxide coated, α lead dioxide plating coat and beta lead dioxide coating successively.
Wherein, described ruthenium and iridium oxide be coated in the titanium substrate surface after tackiness agent mixes and form transition layer, described tin and sb oxide be coated in the transition layer surface after tackiness agent mixes and form active layer, described active layer electroplating surface α plumbic oxide forms the middle layer, and described interlayer surfaces is electroplated beta lead dioxide and formed serving.
Further, the thickness of described transition layer is 3-5 μ m, and the thickness of described active layer is 3-5 μ m, and the thickness in described middle layer is 30-50 μ m, and the thickness of described serving is 2-3mm.
The utility model has compared with prior art improved the binding force of cladding material of ti-supported lead dioxide electric, improved oxygen overpotential, strengthened the oxidation capacity of anode surface, direct oxidative degradation organism on anode surface, make the organism in sewage pass through electrochemical conversion, direct or indirect CO2 and the water of being converted into can not pollute in this process, is called as Green Water and processes; Strengthened simultaneously the corrosion resistance of titanium matrix, prevented that the titanium matrix surface from forming the poor titanium dioxide of electric conductivity, strengthened the electroconductibility of positive plate.
Description of drawings
Fig. 1 is the utility model structural representation.
Embodiment
Below in conjunction with accompanying drawing 1, a kind of embodiment of the present utility model is described.
The ti-lead dioxide anode plate has titanium base material 1, and described titanium base material 1 surface scribbles ruthenium and iridium oxide coating, tin and antimony oxide coated, α lead dioxide plating coat and beta lead dioxide coating successively.Wherein, described ruthenium and iridium oxide be coated in titanium base material 1 surface after tackiness agent mixes and form transition layer 2, described tin and sb oxide be coated in transition layer 2 surfaces after tackiness agent mixes and form active layers 3, described active layer 3 electroplating surface α plumbic oxide form middle layer 4, and described middle layer 4 electroplating surface beta lead dioxides 5 form serving 5.Wherein, the thickness of described transition layer 2 is 3-5 μ m, and the thickness of described active layer 3 is 3-5 μ m, and the thickness in described middle layer 4 is 30-50 μ m, and the thickness of described serving 5 is 2-3mm.
Ruthenium and iridium oxide (RuO
2IrO
2) and tackiness agent be coated in titanium base material 1 surface after mixing, the surface at titanium base material 1 after sintering forms transition layer 2, the oxide S nO of tin
2Oxide S b with antimony
2O
5Be coated in transition layer 2 surfaces, form active layers 3 on transition layer 2 surfaces after sintering, the α plumbic oxide is electroplated in containing plumbous plating tank and is formed middle layer 4, and beta lead dioxide forms serving 5 in leaded plating tank.This practical employing ruthenium iridium has improved the electric conductivity of anode as transition layer 2, adopts tin-antimony oxide as active layer 3, has improved the corrosion resistance nature of titanium matrix, prevents that the titanium matrix surface from forming nonconducting titanium dioxide.The α plumbic oxide can strengthen the firmness of lead dioxide plating coat and electrode matrix combination, the generation of mitigation electrodeposition distortion as the middle layer, can also make β-PbO
2Be evenly distributed, the Direct Electroplating beta lead dioxide forms serving 5 on middle layer 4, can make anode of lead dioxide in treatment of Organic Wastewater, direct oxidative degradation organism on anode surface, make the organism in sewage pass through electrochemical conversion, direct or indirect CO2 and the water of being converted into has reduced the pollution to environment.
The utility model is easy to produce, and erosion resistance is strong, and oxidisability is strong, and oxygen overpotential is high, is applicable to organic waste water and phenolic wastewater treatment industry.Being widely used at present the fields such as plating, smelting, wastewater treatment, cathodic protection, is that many other electrode materialss (as DSA, plumbous, titanium platinum plating) can't replace.
Above-described embodiment is preferred embodiment of the present utility model, is not to limit the utility model practical range, thus all equivalence variations of being done with the described content of the utility model claim, within all should being included in the utility model claim scope.
Claims (3)
1. the ti-lead dioxide anode plate, have titanium base material (1), it is characterized in that: described titanium base material (1) surface scribbles ruthenium and iridium oxide coating, tin and antimony oxide coated, α lead dioxide plating coat and beta lead dioxide coating successively.
2. ti-lead dioxide anode plate according to claim 1, it is characterized in that: described ruthenium and iridium oxide be coated in titanium base material (1) surface after tackiness agent mixes and form transition layer (2), described tin and sb oxide be coated in transition layer (2) surface after tackiness agent mixes and form active layer (3), described active layer (3) electroplating surface α plumbic oxide forms middle layer (4), and described middle layer (4) electroplating surface beta lead dioxide (5) forms serving (5).
3. ti-lead dioxide anode plate according to claim 2, it is characterized in that: the thickness of described transition layer (2) is 3-5 μ m, the thickness of described active layer (3) is 3-5 μ m, and the thickness of described middle layer (4) is 30-50 μ m, and the thickness of described serving (5) is 2-3mm.
Priority Applications (1)
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CN 201220680503 CN202936494U (en) | 2012-12-11 | 2012-12-11 | Titanium-based lead dioxide anode plate |
Applications Claiming Priority (1)
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CN 201220680503 CN202936494U (en) | 2012-12-11 | 2012-12-11 | Titanium-based lead dioxide anode plate |
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CN202936494U true CN202936494U (en) | 2013-05-15 |
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CN 201220680503 Expired - Lifetime CN202936494U (en) | 2012-12-11 | 2012-12-11 | Titanium-based lead dioxide anode plate |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109516616A (en) * | 2019-01-04 | 2019-03-26 | 中冶华天工程技术有限公司 | A kind of electrochemical repair method of antimony pollution waste water |
CN111943327A (en) * | 2019-05-14 | 2020-11-17 | 宝山钢铁股份有限公司 | Having RuO for acidic wastewater treatment2-IrO2Electrode material of intermediate layer and preparation method |
CN111962121A (en) * | 2020-08-19 | 2020-11-20 | 西安交通大学 | Method for quickly constructing titanium substrate three-dimensional porous lead dioxide active layer |
CN112158919A (en) * | 2020-09-03 | 2021-01-01 | 广东臻鼎环境科技有限公司 | Sandwich structure composite lead dioxide anode and preparation method thereof |
CN113394408A (en) * | 2021-06-17 | 2021-09-14 | 昆明高聚科技有限公司 | Long-life light composite positive grid and preparation method thereof, and positive electrode plate and preparation method thereof |
CN115125594A (en) * | 2022-07-22 | 2022-09-30 | 西安泰金工业电化学技术有限公司 | Lead dioxide anode for zinc electrodeposition and rapid preparation method thereof |
-
2012
- 2012-12-11 CN CN 201220680503 patent/CN202936494U/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109516616A (en) * | 2019-01-04 | 2019-03-26 | 中冶华天工程技术有限公司 | A kind of electrochemical repair method of antimony pollution waste water |
CN111943327A (en) * | 2019-05-14 | 2020-11-17 | 宝山钢铁股份有限公司 | Having RuO for acidic wastewater treatment2-IrO2Electrode material of intermediate layer and preparation method |
CN111962121A (en) * | 2020-08-19 | 2020-11-20 | 西安交通大学 | Method for quickly constructing titanium substrate three-dimensional porous lead dioxide active layer |
CN111962121B (en) * | 2020-08-19 | 2021-11-19 | 西安交通大学 | Method for quickly constructing titanium substrate three-dimensional porous lead dioxide active layer |
CN112158919A (en) * | 2020-09-03 | 2021-01-01 | 广东臻鼎环境科技有限公司 | Sandwich structure composite lead dioxide anode and preparation method thereof |
CN113394408A (en) * | 2021-06-17 | 2021-09-14 | 昆明高聚科技有限公司 | Long-life light composite positive grid and preparation method thereof, and positive electrode plate and preparation method thereof |
CN115125594A (en) * | 2022-07-22 | 2022-09-30 | 西安泰金工业电化学技术有限公司 | Lead dioxide anode for zinc electrodeposition and rapid preparation method thereof |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20220208 Address after: Block h, phase I, Baoji high end equipment Industrial Park, No. 95, Shuxiang Road South, Baoji hi tech Development Zone, Shaanxi Province, 721000 Patentee after: Baoji Titanium Prius Titanium Anode Technology Co.,Ltd. Address before: 721013 Xuguang Industrial Park, Maying Town, Weibin District, Baoji City, Shaanxi Province Patentee before: BAOJI CHANGLI SPECIAL METAL Co.,Ltd. |
|
TR01 | Transfer of patent right | ||
CX01 | Expiry of patent term |
Granted publication date: 20130515 |
|
CX01 | Expiry of patent term |