[go: up one dir, main page]

CN1772955A - A kind of mixed metal oxide electrode and preparation method thereof - Google Patents

A kind of mixed metal oxide electrode and preparation method thereof Download PDF

Info

Publication number
CN1772955A
CN1772955A CN 200510104253 CN200510104253A CN1772955A CN 1772955 A CN1772955 A CN 1772955A CN 200510104253 CN200510104253 CN 200510104253 CN 200510104253 A CN200510104253 A CN 200510104253A CN 1772955 A CN1772955 A CN 1772955A
Authority
CN
China
Prior art keywords
intermediate layer
metal oxide
titanium
electrode
mixed metal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN 200510104253
Other languages
Chinese (zh)
Inventor
徐海波
王佳
姜俊峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ocean University of China
Original Assignee
Ocean University of China
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ocean University of China filed Critical Ocean University of China
Priority to CN 200510104253 priority Critical patent/CN1772955A/en
Publication of CN1772955A publication Critical patent/CN1772955A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Inert Electrodes (AREA)

Abstract

The mixed metal oxide electrode features the metal substrate with one intermediate layer coated via physical and/or chemical process and one mixed metal oxide coating formed through painting, several times of thermal decomposition and sintering on the intermediate layer. The metal substrate is made of Ti, Ta, Nb, Zr, W, Al or stainless steel; and the intermediate layer is one or several of nitride, boride or carbide of Ti, Ta and Nb. The mixed metal oxide electrode has the advantages of high electric catalytic activity, high electric conductivity, high anode oxidation resistance, long service life and low production cost.

Description

一种混合金属氧化物电极及其制备方法A kind of mixed metal oxide electrode and preparation method thereof

技术领域technical field

本发明涉及一种电化学工程用的混合金属氧化物电极及其制备方法,特别是涉及一种含有中间层的混合金属氧化物电极及其制备方法。The invention relates to a mixed metal oxide electrode for electrochemical engineering and a preparation method thereof, in particular to a mixed metal oxide electrode containing an intermediate layer and a preparation method thereof.

背景技术Background technique

电化学工业和电冶金工业都离不开电极,电极材料的选择极为重要。电极过程的方向和动力学、电极和电解槽的结构型式与电槽寿命、维修费用和劳动力消耗以及工艺过程的动力指标等都在很大程度上取决于电极的结构和所用的材料,尤其是在进行电极型式和电槽结构设计时,都和电极材料的耐用性、导电性、电催化活性和电能消耗值有着密切的关系,不断研制性能优越的新型电极材料始终受到很大的关注。Both the electrochemical industry and the electrometallurgical industry are inseparable from electrodes, and the selection of electrode materials is extremely important. The direction and kinetics of the electrode process, the structure type of the electrode and the electrolytic cell and the life of the cell, the maintenance cost and labor consumption, and the dynamic index of the process all depend to a large extent on the structure of the electrode and the materials used, especially The electrode type and cell structure design are closely related to the durability, conductivity, electrocatalytic activity and power consumption value of the electrode material. The continuous development of new electrode materials with superior performance has always received great attention.

现有的涂层钛电极以金属钛作为电极基体,其表面涂覆以铂族金属氧化物为主要组分的活性涂层。涂层钛电极又称金属阳极,国内外一般称为DSA。Henry Beer首先向人们揭示金属氧化物的电催化活性,于1965年在南非获得氧化钌涂层专利,并于1967年在比利时公布了钛基混合氧化钌涂层专利。这之后,Vittorio de Nora把H.Beer的发明付诸了工业化。有关学者认为,DSA的发明是对电化学领域划时代的贡献,是20世纪电化学中最重大的发明之一。目前有关DSA的理论研究和发明已有很多的报道,其目的无外乎是提高电极的电催化性能和使用寿命。影响涂层钛电极的寿命有两个方面:一个是催化层的活性溶解,另一个是钛基体的氧化致钝。催化层的活性溶解,可以从催化层的组分、配比和烧结工艺上加以控制。而有关抑制钛基体的氧化致钝造成电极失效,有关文献曾经提出采用钽作为中间层,但这种方法的一个致命缺点是制造电极的成本太高,而丧失了应用价值。也有文献指出,通过增加催化层的涂刷次数,增加催化层的厚度,来降低钛基体的氧化致钝时间,但这无疑大大提高了电极的制造成本,而且从最终效果来说对电极寿命的提高也是有限的。因此,如何在保证电极的电催化性能的前提下,开发低成本、高寿命的新型电极成为电化学工业目前急需解决的一个关键问题。The existing coated titanium electrode uses metal titanium as the electrode substrate, and its surface is coated with an active coating mainly composed of platinum group metal oxides. Coated titanium electrodes are also called metal anodes, generally called DSA at home and abroad. Henry Beer first revealed the electrocatalytic activity of metal oxides, obtained a patent for ruthenium oxide coating in South Africa in 1965, and published a patent for titanium-based mixed ruthenium oxide coating in Belgium in 1967. After that, Vittorio de Nora put H. Beer's invention into industrialization. Relevant scholars believe that the invention of DSA is an epoch-making contribution to the field of electrochemistry and one of the most important inventions in electrochemistry in the 20th century. At present, there have been many reports on the theoretical research and invention of DSA, and its purpose is nothing more than to improve the electrocatalytic performance and service life of the electrode. There are two aspects affecting the life of the coated titanium electrode: one is the active dissolution of the catalytic layer, and the other is the oxidation passivation of the titanium substrate. The active dissolution of the catalytic layer can be controlled from the composition, ratio and sintering process of the catalytic layer. Regarding the inhibition of electrode failure caused by the passivation of the titanium substrate, relevant literature has proposed the use of tantalum as the intermediate layer, but a fatal shortcoming of this method is that the cost of manufacturing the electrode is too high, and the application value is lost. It is also pointed out in the literature that the oxidation passivation time of the titanium substrate can be reduced by increasing the number of coatings of the catalytic layer and increasing the thickness of the catalytic layer, but this undoubtedly greatly increases the manufacturing cost of the electrode, and in terms of the final effect, it affects the life of the electrode. Improvement is also limited. Therefore, under the premise of ensuring the electrocatalytic performance of the electrode, how to develop a new type of electrode with low cost and long life has become a key problem that the electrochemical industry needs to solve urgently.

发明内容Contents of the invention

本发明的目的是提供一种混合金属氧化物电极及其制备方法,它能解决现有技术中存在的上述问题。The object of the present invention is to provide a mixed metal oxide electrode and its preparation method, which can solve the above-mentioned problems in the prior art.

一种混合金属氧化物电极,其特征在于有一金属基体,在上涂覆一层中间层,在中间层上涂覆混合金属氧化物涂层;所述的金属基体是钛、钽、铌、锆、钨、铝或不锈钢中的一种,所述的中间层是钛或钽或铌的氮化物或硼化物或碳化物中的一种或几种。A mixed metal oxide electrode is characterized in that there is a metal substrate, coated with an intermediate layer, and a mixed metal oxide coating is coated on the intermediate layer; the metal substrate is titanium, tantalum, niobium, zirconium , tungsten, aluminum, or stainless steel, and the intermediate layer is one or more of titanium, tantalum, or niobium nitrides, borides, or carbides.

上述的混合金属氧化物电极的制备方法,其特征在于在金属基体上通过物理或/和化学方法涂覆一中间层,而后再在中间层上涂覆并通过多次热分解烧结而形成的混合金属氧化物涂层;所述的金属基体是钛、钽、铌、锆、钨、铝或不锈钢中的一种,所述的中间层是钛或钽或铌的氮化物或硼化物或碳化物中的一种或几种。The preparation method of the above-mentioned mixed metal oxide electrode is characterized in that an intermediate layer is coated on the metal substrate by physical or/and chemical methods, and then the mixed layer is coated on the intermediate layer and formed by multiple times of thermal decomposition and sintering. Metal oxide coating; the metal substrate is one of titanium, tantalum, niobium, zirconium, tungsten, aluminum or stainless steel, and the intermediate layer is nitride or boride or carbide of titanium or tantalum or niobium one or more of them.

本发明的电极具有电催化活性高,导电性能好,抗阳极氧化性能强,使用寿命长,生产成本低的优点。The electrode of the invention has the advantages of high electrocatalytic activity, good electrical conductivity, strong anodic oxidation resistance, long service life and low production cost.

附图说明Description of drawings

附图1.为有氮化钛中间层的钛基混合金属氧化物涂层的结构示意图。Accompanying drawing 1. is the structural representation of the titanium base mixed metal oxide coating that has titanium nitride intermediate layer.

附图2.为有和没有氮化钛中间层的钛基混合金属氧化物电极的电催化性能比较的效果图。Accompanying drawing 2. It is the effect diagram comparing the electrocatalytic performance of the titanium-based mixed metal oxide electrode with and without the titanium nitride interlayer.

附图3.为有和没有氮化钛中间层的钛基混合金属氧化物电极的加速寿命试验结果比较图。Accompanying drawing 3. It is the comparison graph of the accelerated life test result of titanium-based mixed metal oxide electrode with and without titanium nitride intermediate layer.

具体实施方式Detailed ways

本发明的混合金属氧化物电极的结构如图1所示,它是在金属基体1上涂覆一中间层2,在中间层2上涂覆混合金属氧化物涂层3;所述的金属基体1是钛、钽、铌、锆、钨、铝或不锈钢中的一种,所述的中间层2是钛或钽或铌的氮化物或硼化物或碳化物中的一种或几种。金属基体1是经过去油污和酸蚀刻的基体。中间层2的厚度为0.1μm~20μm范围内。The structure of mixed metal oxide electrode of the present invention is as shown in Figure 1, and it is to coat an intermediate layer 2 on metal base 1, and coat mixed metal oxide coating 3 on intermediate layer 2; Described metal base 1 is one of titanium, tantalum, niobium, zirconium, tungsten, aluminum or stainless steel, and the intermediate layer 2 is one or more of nitrides, borides or carbides of titanium, tantalum or niobium. The metal substrate 1 is a substrate that has undergone degreasing and acid etching. The thickness of the intermediate layer 2 is in the range of 0.1 μm to 20 μm.

制备时,在金属基体1上通过物理或/和化学的方法涂覆一中间层2,而后再在中间层2上涂覆并通过多次热分解烧结而形成的混合金属氧化物涂层3;中间层2可以采用多种物理或/和化学的方法来制备,这些方法包括离子渗氮、离子注入、热喷涂、物理气相沉积、化学气相沉积、等离子体辅助化学气相沉积。混合金属氧化物涂层3至少有一种活性组分和至少有一种惰性组分混合组成,该活性组分是铂族金属或其氧化物,惰性组分是非铂族金属或其氧化物。混合金属氧化物涂层3的热分解制备过程是将活性组分和惰性组分的前驱体化合物混合在有机溶剂中配成溶液,将该溶液通过喷涂、滚涂或刷涂的方法涂覆在中间层2上,然后经干燥,再在高温下进行烧结,之后再重复上述涂覆过程至少三次。高温烧结过程的烧结温度为400~560℃。During preparation, an intermediate layer 2 is coated on the metal substrate 1 by physical or/and chemical methods, and then the mixed metal oxide coating 3 formed by coating the intermediate layer 2 and forming by multiple times of thermal decomposition and sintering; The intermediate layer 2 can be prepared by various physical or/and chemical methods, including ion nitriding, ion implantation, thermal spraying, physical vapor deposition, chemical vapor deposition, and plasma-assisted chemical vapor deposition. The mixed metal oxide coating 3 is composed of at least one active component and at least one inert component. The active component is a platinum group metal or its oxide, and the inert component is a non-platinum group metal or its oxide. The thermal decomposition preparation process of the mixed metal oxide coating 3 is to mix the precursor compounds of the active component and the inert component in an organic solvent to form a solution, and apply the solution on the surface by spraying, rolling or brushing. The intermediate layer 2 is then dried and then sintered at a high temperature, and then the above coating process is repeated at least three times. The sintering temperature in the high temperature sintering process is 400-560°C.

具体操作时,首先将工业纯钛TA2用金属清洗剂清洗,或在10%(重量百分数)NaOH水溶液中将钛板作为阴极进行电解除油,而后在10%草酸水溶液中,在微沸下处理2~3h,再用水冲洗干净,放置备用。在含有氮化钛层的情况下,采用离子镀的方法在上述钛基体镀上一层厚约1μm的氮化钛层。During the specific operation, at first the commercially pure titanium TA2 is cleaned with a metal cleaning agent, or the titanium plate is used as the cathode in 10% (weight percent) NaOH aqueous solution to carry out electrolytic degreasing, and then in 10% oxalic acid aqueous solution, treat it under slight boiling 2 to 3 hours, then rinse with water, and set aside. In the case of containing a titanium nitride layer, a layer of titanium nitride layer with a thickness of about 1 μm is plated on the above-mentioned titanium substrate by ion plating.

混合金属氧化物涂层3选择工业上广泛应用的析氧电极使用的铱钽混合氧化物涂层,其典型的涂覆母液为:H2IrCl6·xH2O(溶于盐酸中)+TaCl5(溶于乙醇中)混合溶液,其中Ir/Ta摩尔比为7∶6,再用浓盐酸稀释至金属总浓度为0.2mol/L。用软呢绒刷笔将上述溶液分别涂覆于含有和不含有TiN中间层2的上述钛基体上,在120℃烘箱中烘干6~15min后,置于箱式电炉中于400~560℃不同温度下烧结10min,取出空冷后,重复上述步骤10次,最后一次在该烧结温度下退火一小时。从而分别制得在烧结温度400℃、420℃、440℃、460℃、480℃、500℃、520℃、540℃和560℃下,含有和不含有TiN中间层的钛基铱钽混合氧化物电极各9片。Mixed metal oxide coating 3 Select the iridium-tantalum mixed oxide coating used in the oxygen evolution electrode widely used in industry, and its typical coating mother solution is: H 2 IrCl 6 xH 2 O (dissolved in hydrochloric acid)+TaCl 5 (dissolved in ethanol) mixed solution, wherein the Ir/Ta molar ratio is 7:6, and then diluted with concentrated hydrochloric acid to a total metal concentration of 0.2mol/L. Use a woolen brush to apply the above solution on the above-mentioned titanium substrate with and without the TiN intermediate layer 2, and dry it in an oven at 120°C for 6-15 minutes, then place it in a box-type electric furnace at 400-560°C. Sinter at the same temperature for 10 minutes, take it out for air cooling, repeat the above steps 10 times, and anneal at the sintering temperature for one hour for the last time. In this way, titanium-based iridium-tantalum mixed oxides with and without TiN intermediate layers were prepared at sintering temperatures of 400°C, 420°C, 440°C, 460°C, 480°C, 500°C, 520°C, 540°C and 560°C, respectively. 9 electrodes each.

对本发明的电极进行了电催化性能评价的结果如图2所示。电催化性能评价是在0.5mol/L硫酸水溶液中采用恒电位于+1.4V(相对于饱和甘汞电极),测量其阳极电流密度。该阳极电流密度值越大,表明催化性能越高。从图2中可以看到,含有TiN中间层2的电极与不含有TiN中间层2的电极的电流密度非常接近,表明引入TiN中间层2并没有对电极的电催化性能带来负面影响。The result of evaluating the electrocatalytic performance of the electrode of the present invention is shown in FIG. 2 . The evaluation of electrocatalytic performance is to measure its anode current density in 0.5mol/L sulfuric acid aqueous solution with a constant current at +1.4V (relative to a saturated calomel electrode). The larger the value of the anode current density, the higher the catalytic performance. It can be seen from Figure 2 that the current density of the electrode containing the TiN interlayer 2 is very close to that of the electrode without the TiN interlayer 2, indicating that the introduction of the TiN interlayer 2 does not have a negative impact on the electrocatalytic performance of the electrode.

对本发明的电极进行了强化寿命评价的结果如图3所示。在1mol/L硫酸水溶液中,采用恒电流方法,控制电流密度为2A/cm2,测量其槽压随时间的变化。当槽压升高幅度超过5V时,即认为电极已失效。从图3中可以看出,含有TiN中间层的电极强化寿命时间普遍都大于不含有TiN中间层的电极,尤其是烧结温度为460℃的电极,其强化寿命是不含有TiN中间层的2倍左右。Fig. 3 shows the results of the enhanced lifetime evaluation of the electrodes of the present invention. In 1mol/L sulfuric acid aqueous solution, adopt the constant current method, control the current density to 2A/cm 2 , and measure the change of the cell pressure with time. When the cell voltage rise exceeds 5V, the electrode is considered to have failed. It can be seen from Figure 3 that the strengthened life time of the electrode containing the TiN interlayer is generally longer than that of the electrode without the TiN interlayer, especially for the electrode with a sintering temperature of 460 ° C, its strengthened life is twice that of the electrode without the TiN interlayer about.

TiN属于金属键陶瓷,具有比钛高得多的导电性能,其耐蚀性类似于钛,也有很好的抗阳极氧化性能,而且在阳极氧化过程中仍然保持很高的导电性能,而不至于象钛的阳极氧化膜是不导电的,正是由于它的这些特点,把它作为中间层势必可以减缓钛基体的致钝现象发生,从而提高电极的使用寿命。而且TiN的制造成本非常低廉,可以批量生产,能满足工业化生产的要求。TiN belongs to metal bond ceramics, which has much higher electrical conductivity than titanium, its corrosion resistance is similar to that of titanium, and it also has good anodic oxidation resistance, and it still maintains high electrical conductivity during anodic oxidation without The anodic oxide film like titanium is non-conductive. It is precisely because of its characteristics that it can be used as an intermediate layer to slow down the passivation of the titanium substrate, thereby improving the service life of the electrode. Moreover, the manufacturing cost of TiN is very low, it can be produced in batches, and can meet the requirements of industrial production.

本发明所述的其它金属基体(钽、铌、锆、钨、铝或不锈钢)与上述的钛基体具有相似的性质,所述的其它中间层(钛的硼化物或碳化物,钽或铌的氮化物或硼化物或碳化物中的一种或几种)也与上述的TiN具有类似的性质,用它们来实现本发明所制备的电极也具有同样的功能效果,这里就不再一一累述。Other metal substrates (tantalum, niobium, zirconium, tungsten, aluminum or stainless steel) of the present invention have similar properties to the above-mentioned titanium substrates, and the other intermediate layers (titanium boride or carbide, tantalum or niobium) One or more of nitrides or borides or carbides) also have similar properties with the above-mentioned TiN, and the electrode prepared by using them to realize the present invention also has the same functional effect, so it will not be exhausted here. stated.

利用本发明的制备方法得到的新型电极可以广泛应用于氯碱、水电解、污水处理、有机物电合成、电渗析及电沉积工业中,既可以作为阳极使用,也可以作为阴极使用。The novel electrode obtained by the preparation method of the present invention can be widely used in chlor-alkali, water electrolysis, sewage treatment, organic electrosynthesis, electrodialysis and electrodeposition industries, and can be used as an anode or a cathode.

Claims (7)

1.一种混合金属氧化物电极,其特征在于有一金属基体(1),在金属基体(1)上涂覆一中间层(2),在中间层(2)上涂覆混合金属氧化物涂层(3);所述的金属基体(1)是钛、钽、铌、锆、钨、铝或不锈钢中的一种,所述的中间层(2)是钛或钽或铌的氮化物或硼化物或碳化物中的一种或几种。1. A mixed metal oxide electrode is characterized in that there is a metal substrate (1), an intermediate layer (2) is coated on the metal substrate (1), and a mixed metal oxide coating is applied on the intermediate layer (2). layer (3); the metal substrate (1) is one of titanium, tantalum, niobium, zirconium, tungsten, aluminum or stainless steel, and the intermediate layer (2) is titanium or tantalum or niobium nitride or One or more of borides or carbides. 2.根据权利要求1所述的电极,其特征在于所述的金属基体(1)为经过去油污和酸蚀刻的基体。2. The electrode according to claim 1, characterized in that the metal substrate (1) is a substrate that has undergone degreasing and acid etching. 3.根据权利要求1所述的电极,其特征在于所述的中间层(2)的厚度为0.1μm~20μm。3. The electrode according to claim 1, characterized in that the thickness of the intermediate layer (2) is 0.1 μm˜20 μm. 4.根据权利要求1所述的电极,其特征在于所述的混合金属氧化物涂层(3)至少有一种活性组分和至少有一种惰性组分混合组成,该活性组分是铂族金属或其氧化物,惰性组分是非铂族金属或其氧化物。4. The electrode according to claim 1, characterized in that the mixed metal oxide coating (3) has at least one active component and at least one inert component mixed composition, and the active component is a platinum group metal Or its oxide, the inert component is a non-platinum group metal or its oxide. 5.权利要求1所述的混合金属氧化物电极的制备方法,其特征在于在金属基体(1)上通过物理或/和化学方法涂覆一中间层(2),而后再在中间层(2)上涂覆并通过多次热分解烧结而形成的混合金属氧化物涂层(3);所述的金属基体(1)是钛、钽、铌、锆、钨、铝或不锈钢中的一种,所述的中间层(2)是钛或钽或铌的氮化物或硼化物或碳化物中的一种或几种。5. the preparation method of mixed metal oxide electrode described in claim 1 is characterized in that on metal substrate (1) by physical or/and chemical method coating an intermediate layer (2), then in intermediate layer (2) ) and a mixed metal oxide coating (3) formed by multiple thermal decomposition and sintering; the metal substrate (1) is one of titanium, tantalum, niobium, zirconium, tungsten, aluminum or stainless steel , the intermediate layer (2) is one or more of titanium, tantalum, or niobium nitrides, borides, or carbides. 6.根据权利要求5所述的制备方法,其特征在于所述的制备中间层(2)的物理或/和化学方法包括离子渗氮、离子注入、热喷涂、物理气相沉积、化学气相沉积、等离子体辅助化学气相沉积。6. The preparation method according to claim 5, characterized in that the physical or/and chemical methods for preparing the intermediate layer (2) include ion nitriding, ion implantation, thermal spraying, physical vapor deposition, chemical vapor deposition, Plasma Assisted Chemical Vapor Deposition. 7.根据权利要求5所述的制备方法,其特征在于所述的热分解烧结是将活性组分和惰性组分的前驱体化合物混合在有机溶剂中配成溶液,将该溶液通过喷涂、滚涂或刷涂涂覆在金属基体(1)上,然后经干燥,再在高温下进行烧结,烧结温度为400~560℃。7. The preparation method according to claim 5, characterized in that the thermal decomposition and sintering is to mix the precursor compound of the active component and the inert component in an organic solvent to form a solution, and the solution is sprayed, rolled It is coated on the metal substrate (1) by painting or brushing, then dried, and then sintered at high temperature, and the sintering temperature is 400-560°C.
CN 200510104253 2005-10-12 2005-10-12 A kind of mixed metal oxide electrode and preparation method thereof Pending CN1772955A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200510104253 CN1772955A (en) 2005-10-12 2005-10-12 A kind of mixed metal oxide electrode and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200510104253 CN1772955A (en) 2005-10-12 2005-10-12 A kind of mixed metal oxide electrode and preparation method thereof

Publications (1)

Publication Number Publication Date
CN1772955A true CN1772955A (en) 2006-05-17

Family

ID=36760092

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200510104253 Pending CN1772955A (en) 2005-10-12 2005-10-12 A kind of mixed metal oxide electrode and preparation method thereof

Country Status (1)

Country Link
CN (1) CN1772955A (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101016632B (en) * 2006-12-22 2010-11-24 扬州大学 Process method for preparing metal oxide electrodes by thermal decomposition of polymeric precursors
CN101567269B (en) * 2009-06-05 2011-01-05 中南大学 Coating and thermal decomposition process for preparing RuO* electrode material of super-capacitor
CN101528985B (en) * 2006-10-16 2011-06-22 德诺拉工业有限公司 Anode for electrolysis
CN101490301B (en) * 2006-07-14 2012-05-30 丹佛斯公司 Method for treating titanium objects with a surface layer of mixed tantalum and titanium oxides
CN103345958A (en) * 2013-06-07 2013-10-09 河北工业大学 Composite electrode material containing reactive plasma spraying nanometer TiN middle layer and preparation method thereof
CN104591342A (en) * 2014-11-10 2015-05-06 牛军峰 Preparation method of Ti/Ebonex/PbO2 electrode for sewage deep-treatment
CN104846399A (en) * 2015-05-29 2015-08-19 华北水利水电大学 A Titanium-Based TiNx/TiO2-RuO2 Nano-coated Anode
CN104947143A (en) * 2015-05-29 2015-09-30 华北水利水电大学 A Titanium-Based TiNx/TiO2-RuO2 Coated Anode
CN104988535A (en) * 2015-05-22 2015-10-21 东南大学 Mixed metal oxide coating electrode and preparation method thereof
CN108026649A (en) * 2015-09-25 2018-05-11 阿克苏诺贝尔化学品国际有限公司 Electrode
CN109225195A (en) * 2018-10-15 2019-01-18 吉林大学 Nano transition metal boride catalyst and its application in terms of electro-catalysis water-splitting hydrogen manufacturing
WO2020215770A1 (en) * 2019-04-26 2020-10-29 无锡小天鹅电器有限公司 Electrolysis electrode and preparation method therefor, electrolysis apparatus, and clothing treatment device
CN112609206A (en) * 2020-11-26 2021-04-06 中氢能源科技(广东)有限公司 Anode barrier layer for PEM electrolytic hydrogen production device and preparation method thereof
CN113929188A (en) * 2020-06-29 2022-01-14 佛山市顺德区美的饮水机制造有限公司 Electrode structure, purification structure and electrode preparation method

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101490301B (en) * 2006-07-14 2012-05-30 丹佛斯公司 Method for treating titanium objects with a surface layer of mixed tantalum and titanium oxides
CN101528985B (en) * 2006-10-16 2011-06-22 德诺拉工业有限公司 Anode for electrolysis
CN101016632B (en) * 2006-12-22 2010-11-24 扬州大学 Process method for preparing metal oxide electrodes by thermal decomposition of polymeric precursors
CN101567269B (en) * 2009-06-05 2011-01-05 中南大学 Coating and thermal decomposition process for preparing RuO* electrode material of super-capacitor
CN103345958A (en) * 2013-06-07 2013-10-09 河北工业大学 Composite electrode material containing reactive plasma spraying nanometer TiN middle layer and preparation method thereof
CN104591342A (en) * 2014-11-10 2015-05-06 牛军峰 Preparation method of Ti/Ebonex/PbO2 electrode for sewage deep-treatment
CN104591342B (en) * 2014-11-10 2017-04-05 牛军峰 For the Ti/Ebonex/PbO of advanced treatment of wastewater2The preparation method of electrode
CN104988535A (en) * 2015-05-22 2015-10-21 东南大学 Mixed metal oxide coating electrode and preparation method thereof
CN104947143A (en) * 2015-05-29 2015-09-30 华北水利水电大学 A Titanium-Based TiNx/TiO2-RuO2 Coated Anode
CN104846399A (en) * 2015-05-29 2015-08-19 华北水利水电大学 A Titanium-Based TiNx/TiO2-RuO2 Nano-coated Anode
CN104846399B (en) * 2015-05-29 2018-05-29 华北水利水电大学 A kind of titanium-based TiNx/TiO2-RuO2Nano coating anode
CN108026649A (en) * 2015-09-25 2018-05-11 阿克苏诺贝尔化学品国际有限公司 Electrode
CN109225195A (en) * 2018-10-15 2019-01-18 吉林大学 Nano transition metal boride catalyst and its application in terms of electro-catalysis water-splitting hydrogen manufacturing
CN109225195B (en) * 2018-10-15 2021-09-28 吉林大学 Nano transition metal boride catalyst and application thereof in aspect of hydrogen production by electrocatalytic water cracking
WO2020215770A1 (en) * 2019-04-26 2020-10-29 无锡小天鹅电器有限公司 Electrolysis electrode and preparation method therefor, electrolysis apparatus, and clothing treatment device
US12180095B2 (en) 2019-04-26 2024-12-31 Wuxi Little Swan Electric Co., Ltd. Electrolysis electrode and preparation method therefor, electrolysis apparatus, and clothing treatment device
CN113929188A (en) * 2020-06-29 2022-01-14 佛山市顺德区美的饮水机制造有限公司 Electrode structure, purification structure and electrode preparation method
CN112609206A (en) * 2020-11-26 2021-04-06 中氢能源科技(广东)有限公司 Anode barrier layer for PEM electrolytic hydrogen production device and preparation method thereof

Similar Documents

Publication Publication Date Title
CN101343749B (en) Metallic oxide coating electrode and manufacture method thereof
CN102677092B (en) Preparation method of titanium anode
US8580091B2 (en) Multi-layer mixed metal oxide electrode and method for making same
CN101880891B (en) High-stability DSA anode for preparing chlorine by electrolysis and preparation method thereof
US20230107452A1 (en) A New Interlayer Can Withstand Polarity Reversal
CN108677221B (en) A kind of titanium-based β-MnO2 composite coating anode and preparation method thereof
CN1849414B (en) electrode
MXPA05003643A (en) Coatings for the inhibition of undesirable oxidation in an electrochemical cell.
CN102766882A (en) Manufacture method for chlorine-evolution dimensionally stable anode (DSA) electro-catalytic electrode with three dimensional structure
CN1772955A (en) A kind of mixed metal oxide electrode and preparation method thereof
CN110820030A (en) A preparation method of titanium-based PbO2 anode based on in-situ thermal reaction to prepare conductive ceramic film intermediate layer
WO2013038928A1 (en) Positive electrode for electrolytic plating and electrolytic plating method using positive electrode
CN106048690B (en) A kind of titanium-based titanium dioxide nanotube composite anode and preparation method thereof
CN113800606A (en) Coated titanium anode for circulating cooling water treatment, preparation method and application
CN101338437A (en) A kind of preparation method of gradient multi-element metal mixed oxide anode
CN109778100B (en) A kind of arc thermal spraying preparation method of life-extending and energy-saving form-stable PbO2 anode intermediate layer
CN106086989B (en) A kind of titania modified by Argentine nanotube composite anode and preparation method thereof
CN112195482B (en) Composite titanium anode plate and preparation method thereof
CN100359046C (en) A method for manufacturing a coated anode for electrolysis
JP3653296B2 (en) Electrode for electrolysis and method for producing the same
CN118932445A (en) Iridium composite-coated titanium anode and preparation method thereof
CN116764917A (en) Coating pyrolysis preparation method of oxide coated anode
CN110257814A (en) A kind of metal oxide anode preparation method based on mechanical ball mill paint-on technique
CN117779002A (en) Corrosion-resistant coating, modified titanium material, preparation method and application thereof
CN118480807B (en) Tantalum-permeation gradient interlayer titanium-based metal oxide electrode and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication