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 PDFInfo
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- 229910003455 mixed metal oxide Inorganic materials 0.000 title claims abstract description 22
- 238000002360 preparation method Methods 0.000 title claims description 11
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 32
- 229910052751 metal Inorganic materials 0.000 claims abstract description 27
- 239000002184 metal Substances 0.000 claims abstract description 27
- 239000000758 substrate Substances 0.000 claims abstract description 26
- 238000000576 coating method Methods 0.000 claims abstract description 21
- 239000011248 coating agent Substances 0.000 claims abstract description 19
- 229910052715 tantalum Inorganic materials 0.000 claims abstract description 15
- 229910052758 niobium Inorganic materials 0.000 claims abstract description 13
- 238000005245 sintering Methods 0.000 claims abstract description 12
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 7
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 7
- 239000010935 stainless steel Substances 0.000 claims abstract description 7
- 229910052721 tungsten Inorganic materials 0.000 claims abstract description 7
- 229910052726 zirconium Inorganic materials 0.000 claims abstract description 7
- 238000005979 thermal decomposition reaction Methods 0.000 claims abstract description 6
- 238000010422 painting Methods 0.000 claims abstract 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 30
- 239000010936 titanium Substances 0.000 claims description 30
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 12
- 239000010955 niobium Substances 0.000 claims description 11
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 claims description 9
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 6
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 6
- 239000010937 tungsten Substances 0.000 claims description 6
- 150000001247 metal acetylides Chemical class 0.000 claims description 5
- -1 niobium nitrides Chemical class 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 4
- 238000005238 degreasing Methods 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 2
- 230000001680 brushing effect Effects 0.000 claims description 2
- 238000005229 chemical vapour deposition Methods 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
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- 239000000203 mixture Substances 0.000 claims description 2
- 238000005121 nitriding Methods 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims description 2
- 238000005240 physical vapour deposition Methods 0.000 claims description 2
- 238000000623 plasma-assisted chemical vapour deposition Methods 0.000 claims description 2
- 239000002243 precursor Substances 0.000 claims description 2
- 238000007751 thermal spraying Methods 0.000 claims description 2
- CFJRGWXELQQLSA-UHFFFAOYSA-N azanylidyneniobium Chemical compound [Nb]#N CFJRGWXELQQLSA-UHFFFAOYSA-N 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 7
- 230000003647 oxidation Effects 0.000 abstract description 6
- 238000007254 oxidation reaction Methods 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 150000004767 nitrides Chemical class 0.000 abstract description 4
- 238000001311 chemical methods and process Methods 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 31
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 11
- 239000011229 interlayer Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical compound [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000002161 passivation Methods 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 239000007772 electrode material Substances 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
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- 238000011156 evaluation Methods 0.000 description 2
- ULFQGKXWKFZMLH-UHFFFAOYSA-N iridium tantalum Chemical compound [Ta].[Ir] ULFQGKXWKFZMLH-UHFFFAOYSA-N 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 229910001925 ruthenium oxide Inorganic materials 0.000 description 2
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 description 2
- 229910003456 titanium-based mixed metal oxide Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 239000010407 anodic oxide Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
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- 238000010586 diagram Methods 0.000 description 1
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
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Abstract
Description
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.
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| 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 |
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| 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 |
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| 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 |
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