CN101338437A - Method for preparing graded multicomponent metal mixing oxide anode - Google Patents
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- 229910052751 metal Inorganic materials 0.000 title claims abstract description 15
- 239000002184 metal Substances 0.000 title claims abstract description 15
- 238000002156 mixing Methods 0.000 title claims description 7
- 238000000034 method Methods 0.000 title abstract description 24
- 239000010936 titanium Substances 0.000 claims abstract description 60
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 51
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000011159 matrix material Substances 0.000 claims abstract description 38
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 230000000873 masking effect Effects 0.000 claims abstract description 31
- 238000002360 preparation method Methods 0.000 claims abstract description 28
- 239000011248 coating agent Substances 0.000 claims abstract description 14
- 238000000576 coating method Methods 0.000 claims abstract description 14
- 238000005245 sintering Methods 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 8
- 238000002203 pretreatment Methods 0.000 claims description 8
- 230000001680 brushing effect Effects 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 claims description 6
- 229910052718 tin Inorganic materials 0.000 claims description 6
- 229910052741 iridium Inorganic materials 0.000 claims description 5
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical group CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 4
- 239000012153 distilled water Substances 0.000 claims description 4
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 claims description 3
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 239000002904 solvent Substances 0.000 claims description 3
- 206010013786 Dry skin Diseases 0.000 claims description 2
- 238000003618 dip coating Methods 0.000 claims description 2
- 238000007590 electrostatic spraying Methods 0.000 claims description 2
- 235000006408 oxalic acid Nutrition 0.000 claims description 2
- 238000005554 pickling Methods 0.000 claims description 2
- 239000004576 sand Substances 0.000 claims description 2
- 238000005488 sandblasting Methods 0.000 claims description 2
- 239000003923 scrap metal Substances 0.000 claims description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 2
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 2
- 238000005868 electrolysis reaction Methods 0.000 abstract description 6
- 239000002344 surface layer Substances 0.000 abstract description 4
- 239000010865 sewage Substances 0.000 abstract description 3
- 238000007747 plating Methods 0.000 abstract description 2
- 239000013535 sea water Substances 0.000 abstract description 2
- 230000005518 electrochemistry Effects 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 38
- 238000004519 manufacturing process Methods 0.000 description 11
- 229910010413 TiO 2 Inorganic materials 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000013461 design Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 229910044991 metal oxide Inorganic materials 0.000 description 5
- 150000004706 metal oxides Chemical class 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 238000002161 passivation Methods 0.000 description 5
- 229910052715 tantalum Inorganic materials 0.000 description 5
- 239000010955 niobium Substances 0.000 description 4
- 239000010970 precious metal Substances 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 229910052758 niobium Inorganic materials 0.000 description 3
- 230000003245 working effect Effects 0.000 description 3
- 230000003373 anti-fouling effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910006404 SnO 2 Inorganic materials 0.000 description 1
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000004590 computer program Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910003455 mixed metal oxide Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 238000011020 pilot scale process Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 238000001149 thermolysis Methods 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
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Abstract
The invention relates to a preparation method of a gradient multi-metal mixed oxide anode, which belongs to the field of electrochemistry. The oxide anode prepared by the invention can be widely used for electrochemical industry, such as sea water electrolysis, cathode protection, sewage disposal and plating, etc. The preparation method comprises the procedures as follows: titanium matrix that has been pre-processed is cut into a flaky test sample; the masking liquids of the surface layer of the oxide anode are prepared respectively and have five different weight percentage concentrations that are numbered; the surface of the titanium matrix is coated with the masking liquids of the surface layer in sequence twice; after being coated once, the surface of the titanium matrix is dried under 100 DEG C for 10 minutes and sintered under 400 DEG C for 10 minutes; with the completion of last coating and sintering, the titanium matrix is sintered under 400 DEG C for one hour to be made into the gradient multi-metal mixed oxide anode. The masking liquid of the surface layer of the invention has appropriate preparation, good stability and convenient coating. In addition, the anode is easy to be prepared and the product has long service life, low cost, wide application and good cost performance.
Description
Technical field:
The invention belongs to electrochemical field, relate to a kind of preparation method of graded multicomponent metal mixing oxide anode, the oxide anode of its preparation can be widely used in electrochemical industry occasions such as seawater electrolysis, galvanic protection, sewage disposal and plating.
Background technology:
At present, characteristics such as the anode of working in the industrialization electrolytic cell should satisfy generally that electric conductivity is good, physics and stable, corrosion-resistant, the easy processing of chemical property, good electro catalytic activity and selectivity, dimensionally stable anode (DSA) can satisfy above requirement preferably, and this point is existing the introduction in U.S.Pat.No.3632498.After Overheating Treatment prepares, its advantage is the oxide anode that can prepare different qualities by the kind and the proportioning of change mixed noble metal salt to the DSA anode, as adopting titanium base RuO at titanium-based surface coating mixed noble metal salt
2-TiO
2Anode adopts titanium base IrO as analysing chlorine type oxide anode
2-Ta
2O
5Anode is as analysing oxygen type anode etc.
In the widely used electrolytic industry of Mixed Metal Oxide Coated Titanium Anodes, anode surface is generally understood the aerobic generation during electric tank working, and no matter whether this electrode is that selectivity is analysed oxygen anodes, and electrolytic bath is pressed and also can be raise gradually.After electrolytic process proceeded to a certain degree, too high groove pressure can cause anode passivation, and electrolyzer quits work.Be penetrated into the interface of titanium matrix and oxide on surface coating and the anode passivation most important reason is the oxygen of separating out in the electrolytic process, destroyed the semiconductor doping structure at interface, formed nonconducting TiO
2Oxide compound.This nonconducting TiO
2Oxide interface also might cause precious metal oxide coating to peel off, and makes anode unavailable fully.Therefore when the development metal oxides coating of anode, at first to solve the problem of passivation of titanium.
Existing technology shows, to the alligatoring on metal titanium surface and apply the middle layer can address this problem to some extent between metal oxide containing precious metals layer and titanium base.The alligatoring on titanium surface helps the cast setting raising bonding force between the two by coating and titanium, thus the passivation that slows down titanium; Applying the middle layer then is to prevent the passivation of titanium by forming fine and close blocking layer on the titanium surface, thereby makes the life-span of electrode system obtain prolonging.Middle layer kind and interpolation middle layer method are more at present, have introduced a kind of polymkeric substance among the United States Patent (USP) U.S.Pat.No.4435313 as the middle layer; The hybrid metal metal oxide of having introduced employing Pt+ (Ti or Sn)+(Ta or Nb) among the United States Patent (USP) U.S.Pat.No.4554176 is as the middle layer; Introduced employing Nb among the United States Patent (USP) U.S.Pat.No.5290415, Ti, Ta, oxide compound at least a among the Zr is as the middle layer.Another similar method of producing the middle layer is first at matrix surface galvanic deposit resistant metal, and then by thermal treatment, makes the middle layer be reflected at interfacial layer by high-temperature interface and form sosoloid or compound.Matsumotoetal also proposes a kind of middle layer reparation technology of novelty, promptly form one deck high resistance oxide film by anodic polarization on the titanium surface earlier, and then form porous oxide film on the surface by special processing (as making the oxide film spark discharge), and then the coating Catalytic Layer, in fact this played the coating middle layer and reached the cast setting effect by the alligatoring to the middle layer.
Though the work-ing life of adopting the method in interpolation middle layer can improve oxide anode, but middle layer component and upper layer are inequality, even differ greatly, need adopt more complicated technology when causing preparing oxide anode, the control difficulty increases during scale operation; Need to purchase a greater variety of raw materials for production simultaneously, production cost increases.Therefore be necessary to develop the production field that a kind of method with higher ratio of performance to price is applied to oxide anode.
It must be the valve metal with unidirectional current-carrying character that oxide anode (DSA) requires matrix, as titanium, tantalum, zirconium, niobium etc., the most suitable DSA matrix of doing of the stability of tantalum and electroconductibility, but it costs an arm and a leg, and thermolysis needs oxygen free condition, complex process, no practical value in the making processes; Zr, Nb and Ta are similar; And the Ti low price, density is little, and is easy to process, therefore, generally selects the matrix of Ti as DSA.In the concrete application of DSA,, add the 3rd constituent element in tradition and be necessary in order to improve some property of traditional Ru-Ti anode coating.Present widely used metal oxide anode mainly contain in the elements such as Ru, Ti, Ir, Ta, Pt, Sn, Pd, Rh, Sb, Co three kinds and more than, wherein the atom of Ir, Sn (ion) radius and Ru, Ti ten minutes are close, IrO
2, SnO
2, RuO
2And TiO
2Identical rutile crystal structure is arranged; The electronegativity of Sn (1.8) is less with the difference of Ru (2.2), Ir (2.2).
Summary of the invention:
The objective of the invention is to overcome the shortcoming that prior art exists, multivariant oxide anodic gradient design method (FGM) is studied and improved, design the FGM manufacture method that a kind of suitable multivariant oxide anode uses.Because the FGM manufacture method only need change the concentration of each layer or which floor masking liquid, therefore when small serial production or pilot scale, can prepare the masking liquid of different ratios, and in the production of extensive oxide anode, can control the add-on of various pioneer's liquid by computer program, therefore can not increase production cost, and the oxide anode life-span of preparation significantly improves, have higher performance, have application promise in clinical practice.
To achieve these goals, the FGM preparation method who the present invention relates to determines the substrate types of oxide anode and the component of surfactivity layer, designs then that the coating to the surfactivity layer applies scheme from matrix.The present invention under the situation that the upper layer composition is determined, prepares the different upper layer masking liquid of each component concentration respectively, wherein with TiO according to the principle of similar compatibility
2The element that structure is identical or close (as Ti, Sn) or oxygen resistance inert element (Ta) content is from high to low to identical with the surfactivity layer preferably, and higher element (as Pt, Ir, Ru, the Co etc.) content of catalytic activity is then from low to high to identical with upper layer; In the process of preparation oxide anode, at first on the titanium matrix of handling well, coat and TiO
25～10 layers of the most close masking liquids of structure are coated and TiO then
25～10 layers of the inferior close masking liquids of structure, by that analogy, until being coated with 5～20 layers of upper surface layers; Whenever be coated with one deck all oven dry, sintering under suitable temperature, brush one deck down fully after the cooling again; Use the oxide anode masking liquid proportioning of this method preparation should be not less than 5, the number of plies of coating is calculated according to design carrying capacity and every layer of average carrying capacity, being coated with the number of plies and should keeping identical as far as possible of each prescription.
The titanium matrix of being carried among the present invention is industrially pure titanium or titanium alloy, and base shape is the shape of tabular, netted, tubulose or other any needs; Coating brush system uses hairbrush to brush or matrix dip-coating or roller coat or electrostatic spraying or other method in masking liquid are uniformly applied on the matrix; The titanium matrix that oxide anode adopts is generally thick titanium plate of 1mm or titanium expansion web; Preparation oxide anode pre-treatment step is: be that 60～200 orders, air pressure are (1～6) * 10 in the silicon carbide granularity earlier
5After under the condition of Pa the titanium matrix surface being carried out sandblasting, water cleans, and removes the sand grains and the scrap metal of remained on surface; Be that 5～25% oxalic acid solution was 85～95 ℃ of following etches 60～240 minutes again with the titanium matrix weight percent concentration after the sandblast; Then, water cleans the titanium matrix after the pickling, cleans with distilled water after brushing away the titanous oxalate settling of matrix surface with scrub-brush simultaneously again, is placed in the distilled water and preserves, and dries during use to get final product; The preparation of oxide anode is that the titanium matrix through pre-treatment is tailored the slabbing sample, and the oxide anode upper layer masking liquid of preparing five kinds of Different Weight percentage concentrations more respectively is also respectively by 5,4,3,2,1 numbering; The upper layer masking liquid is respectively brushed on the titanium matrix surface two times respectively successively by 5,4,3,2, No. 1 orders respectively, 100 ℃ of dryings 10 minutes sintering 10 minutes under 400 ℃ of conditions again after every brushing one time, brush again after the cooling next time, after the brushing sintering is finished the last time, again titanium matrix sintering under 400 ℃ of conditions was made graded multicomponent metal blended oxide anode in 1 hour.Described upper layer masking liquid is by ruthenium trichloride, chloro-iridic acid, tetrabutyl titanate preparation, or by chloro-iridic acid, ruthenium chloride, dibutyl tin laurate preparation, its solvent is a propyl carbinol; The weight percent content of the Ru of upper layer masking liquid, Ir, Ti is Ru: Ir: Ti or Sn=0～25: 10～40: 40～80 or 45～85; Total concentration of metal ions is 0.25mol/L.
Fields such as the oxide anode of the present invention preparation can be antifouling at electrolysis antifouling, electrolytic brine, sewage disposal, swimming-pool water sterilization, galvanic protection and electrometallurgy industry are extensive use of; The oxide anode of similar face layer formula, by adopting the present invention mentioned design of FGM thought and manufacture method, improved more than 30% its work-ing life, and when this oxide anode is used for the flowing water electrolysis, improve more than 50% than the oxide anode life-span of ordinary method preparation work-ing life; Adopt this method to prepare oxide anode simultaneously, preparation technology remains unchanged substantially, therefore is easy to control, and manufacturing cost can not increase; Therefore manufacture method involved in the present invention has higher performance, has application promise in clinical practice.
Embodiment:
Further the present invention is described below by embodiment.
Embodiment 1:
Earlier the titanium matrix is carried out the oxide anode pre-treatment.To make 2 of 30mm * 60mm sheet sample through the titanium matrix of pre-treatment, take by weighing chloro-iridic acid 1.00 grams, ruthenium chloride 0.79 gram, measure 3.05 milliliters of dibutyl tin laurates, it is dissolved in the 20ml propyl carbinol stirs, as oxide anode upper layer masking liquid, this moment Ru: Ir: Sn=25: 30: 45 (wt.%), i.e. No. 1 masking liquid.Prepare Ru: Ir: Sn=25 then respectively: 30: 45 (wt.%); Ru: Ir: Sn=20: 25: 55 (wt.%); Ru: Ir: Sn=15: 20: 65 (wt.%); Ru: Ir: Sn=10: 15: 75 (wt.%); Ru: Ir: Sn=5: 10: 85 (wt.%) five kinds of masking liquids, and be numbered masking liquid respectively 1～No. 5.No. 1 upper layer masking liquid that at first will prepare evenly is painted on first titanium matrix surface, at 400 ℃ of following sintering 10min, repeats above process 10 times behind 100 ℃ of dry 10min, makes No. 1, oxide anode sample as a comparison at 400 ℃ of following sintering 1h at last; Brush No. 5, No. 4, No. 3, No. 2, No. 1 each masking liquid respectively successively and brush twice respectively on second titanium matrix, the drying and sintering step that every brushing one-time surface floor masking liquid repeats No. 1 sample is prepared into oxide anode No. 2, as the anode of present embodiment preparation; Oxide anode carrying capacity by above-mentioned two kinds of methods preparation is respectively 10.25g/m through calculating
2And 9.92g/m
2, the intensified electrolysis life-span is respectively 37.2h and 49h, and the life-span has improved 31.7%, and the precious metal usage quantity decreases relatively, therefore the oxide anode of preparation has higher performance in this way.
Embodiment 2:
Earlier the titanium matrix is carried out the oxide anode pre-treatment.To make 2 of 30mm * 60mm sheet sample through the titanium matrix of pre-treatment, the ruthenium trichloride of weighing suitable quantity, chloro-iridic acid and tetrabutyl titanate are mixed with Ru: Ir: Ti=20: 40: 40 (wt%), solvent is a propyl carbinol, total concentration of metal ions is the oxide anode masking liquid of 0.25mol/L, with this component masking liquid as the upper layer masking liquid; Prepare Ru: Ir: Ti=20 then respectively: 40: 40 (wt.%), Ru: Ir: Ti=15: 35: 50 (wt.%), Ru: Ir: Ti=10: 30: 60 (wt.%), Ru: Ir: Ti=5: 25: 70 (wt.%), Ru: Ir: Ti=0: 20: 80 (wt.%) five kinds of masking liquids are numbered masking liquid respectively 1～No. 5; Repeat the subsequent step of embodiment 1.Oxide anode carrying capacity by above-mentioned two kinds of methods preparation is respectively 9.85g/m2 and 10.08g/m2 through calculating, the intensified electrolysis life-span is respectively 123h and 180h, life-span has improved 46.3%, and the precious metal usage quantity decreases relatively, and therefore the oxide anode of preparation has higher performance in this way.
Claims (4)
1. the preparation method of a graded multicomponent metal mixing oxide anode is characterized in that the titanium matrix through pre-treatment is tailored the slabbing sample, prepares the oxide anode upper layer masking liquid of five kinds of Different Weight percentage concentrations more respectively and also numbers respectively; The upper layer masking liquid is respectively brushed on the titanium matrix surface two times respectively successively by the sequence number order respectively, 100 ℃ of dryings 10 minutes sintering 10 minutes under 400 ℃ of conditions again after every brushing one time, brush again after the cooling next time, after the brushing sintering is finished the last time, again titanium matrix sintering under 400 ℃ of conditions was made graded multicomponent metal blended oxide anode in 1 hour.
2. the preparation method of a kind of graded multicomponent metal mixing oxide anode according to claim 1, it is characterized in that described upper layer masking liquid is by ruthenium trichloride, chloro-iridic acid, tetrabutyl titanate preparation, or by chloro-iridic acid, ruthenium chloride, dibutyl tin laurate preparation, its solvent is a propyl carbinol; The weight percent content of the Ru of upper layer masking liquid, Ir, Ti is Ru: Ir: Ti or Sn=0～25: 10～40: 40～80 or 45～85; Total concentration of metal ions is 0.25mol/L.
3. the preparation method of a kind of graded multicomponent metal mixing oxide anode according to claim 1 is characterized in that titanium matrix pre-treatment step is is that 60～200 orders, air pressure are 1～6 * 10 in the silicon carbide granularity earlier
5After under the condition of Pa the titanium matrix surface being carried out sandblasting, water cleans, and removes the sand grains and the scrap metal of remained on surface; Be that 5～25% oxalic acid solution was 85～95 ℃ of following etches 60～240 minutes again with the titanium matrix weight percent concentration after the sandblast; Then, water cleans the titanium matrix after the pickling, cleans with distilled water after brushing away the titanous oxalate settling of matrix surface with scrub-brush simultaneously again, is placed in the distilled water and preserves.
4. the preparation method of a kind of graded multicomponent metal mixing oxide anode according to claim 1 is characterized in that coating uses hairbrush to brush or matrix dip-coating or roller coat or electrostatic spraying in masking liquid are uniformly applied on the matrix.
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102251252A (en) * | 2011-07-20 | 2011-11-23 | 南京师范大学 | Preparation method of seawater electrolysis reaction anode IrO2-RuO2-SnO2-TiO2 nanoparticle coating |
| CN102517603A (en) * | 2011-11-30 | 2012-06-27 | 浙江大学 | Preparation method for titanium-based low-precious-metal-content oxide coating anode |
| CN103121737A (en) * | 2013-02-21 | 2013-05-29 | 福建工程学院 | Method for electrochemically treating printing and dyeing wastewater |
| CN106011918A (en) * | 2016-07-11 | 2016-10-12 | 青岛双瑞海洋环境工程股份有限公司 | Seawater-electrolysis chlorine producing electrolytic bath used for resisting manganese pollution |
| CN106975894A (en) * | 2017-03-01 | 2017-07-25 | 东莞市佳乾新材料科技有限公司 | A kind of composite titan-based inert anode plate and preparation method thereof |
| CN108046380A (en) * | 2017-12-13 | 2018-05-18 | 东华大学 | A kind of titanium-based Sn-Sb-Ce oxide electrodes and its preparation method and application |
| CN109518221A (en) * | 2019-01-08 | 2019-03-26 | 福州大学 | A kind of surface is rich in the gradient distribution Ni―Ti anode and preparation method thereof of iridium dioxide |
| CN111137953A (en) * | 2020-01-09 | 2020-05-12 | 江苏安凯特科技股份有限公司 | Preparation process of titanium-based tin iridium oxide coating electrode |
-
2008
- 2008-08-07 CN CN 200810140104 patent/CN101338437A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102251252A (en) * | 2011-07-20 | 2011-11-23 | 南京师范大学 | Preparation method of seawater electrolysis reaction anode IrO2-RuO2-SnO2-TiO2 nanoparticle coating |
| CN102517603A (en) * | 2011-11-30 | 2012-06-27 | 浙江大学 | Preparation method for titanium-based low-precious-metal-content oxide coating anode |
| CN103121737A (en) * | 2013-02-21 | 2013-05-29 | 福建工程学院 | Method for electrochemically treating printing and dyeing wastewater |
| CN103121737B (en) * | 2013-02-21 | 2014-05-07 | 福建工程学院 | Method for electrochemically treating printing and dyeing wastewater |
| CN106011918A (en) * | 2016-07-11 | 2016-10-12 | 青岛双瑞海洋环境工程股份有限公司 | Seawater-electrolysis chlorine producing electrolytic bath used for resisting manganese pollution |
| CN106975894A (en) * | 2017-03-01 | 2017-07-25 | 东莞市佳乾新材料科技有限公司 | A kind of composite titan-based inert anode plate and preparation method thereof |
| CN108046380A (en) * | 2017-12-13 | 2018-05-18 | 东华大学 | A kind of titanium-based Sn-Sb-Ce oxide electrodes and its preparation method and application |
| CN109518221A (en) * | 2019-01-08 | 2019-03-26 | 福州大学 | A kind of surface is rich in the gradient distribution Ni―Ti anode and preparation method thereof of iridium dioxide |
| CN111137953A (en) * | 2020-01-09 | 2020-05-12 | 江苏安凯特科技股份有限公司 | Preparation process of titanium-based tin iridium oxide coating electrode |
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