CN115074792B - Preparation method of cobalt-based alloy film with special structure and product - Google Patents
Preparation method of cobalt-based alloy film with special structure and product Download PDFInfo
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- 229910000531 Co alloy Inorganic materials 0.000 title claims abstract description 54
- 238000002360 preparation method Methods 0.000 title claims abstract description 26
- 239000002131 composite material Substances 0.000 claims abstract description 89
- 239000000243 solution Substances 0.000 claims abstract description 68
- 230000002378 acidificating effect Effects 0.000 claims abstract description 45
- 238000004070 electrodeposition Methods 0.000 claims abstract description 45
- 238000007747 plating Methods 0.000 claims abstract description 43
- 239000002245 particle Substances 0.000 claims abstract description 40
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 31
- 239000001257 hydrogen Substances 0.000 claims abstract description 31
- 239000000463 material Substances 0.000 claims abstract description 26
- 238000005260 corrosion Methods 0.000 claims abstract description 12
- 230000007797 corrosion Effects 0.000 claims abstract description 12
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims abstract description 10
- 239000002904 solvent Substances 0.000 claims abstract description 10
- 229910052751 metal Inorganic materials 0.000 claims abstract description 9
- 239000002184 metal Substances 0.000 claims abstract description 9
- 150000003657 tungsten Chemical class 0.000 claims abstract description 8
- 150000001868 cobalt Chemical class 0.000 claims abstract description 7
- 239000012670 alkaline solution Substances 0.000 claims abstract description 5
- 238000007654 immersion Methods 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 45
- 239000008139 complexing agent Substances 0.000 claims description 20
- 229940044175 cobalt sulfate Drugs 0.000 claims description 15
- 229910000361 cobalt sulfate Inorganic materials 0.000 claims description 15
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical group [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 14
- XMVONEAAOPAGAO-UHFFFAOYSA-N sodium tungstate Chemical group [Na+].[Na+].[O-][W]([O-])(=O)=O XMVONEAAOPAGAO-UHFFFAOYSA-N 0.000 claims description 14
- 239000007772 electrode material Substances 0.000 claims description 6
- 229910045601 alloy Inorganic materials 0.000 claims description 5
- 239000000956 alloy Substances 0.000 claims description 5
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
- 229910017052 cobalt Inorganic materials 0.000 claims description 3
- 239000010941 cobalt Substances 0.000 claims description 3
- 244000248349 Citrus limon Species 0.000 claims 1
- 235000005979 Citrus limon Nutrition 0.000 claims 1
- 239000002253 acid Substances 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 28
- 230000003197 catalytic effect Effects 0.000 abstract description 12
- 239000007769 metal material Substances 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 23
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 22
- 238000003756 stirring Methods 0.000 description 18
- 229910020515 Co—W Inorganic materials 0.000 description 14
- KLOIYEQEVSIOOO-UHFFFAOYSA-N carbocromen Chemical group CC1=C(CCN(CC)CC)C(=O)OC2=CC(OCC(=O)OCC)=CC=C21 KLOIYEQEVSIOOO-UHFFFAOYSA-N 0.000 description 14
- 238000000576 coating method Methods 0.000 description 13
- 239000011248 coating agent Substances 0.000 description 12
- 238000010586 diagram Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- 238000005868 electrolysis reaction Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 229910000510 noble metal Inorganic materials 0.000 description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 3
- 238000000151 deposition Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920000557 Nafion® Polymers 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/56—Electroplating: Baths therefor from solutions of alloys
- C25D3/562—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of iron or nickel or cobalt
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/073—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
- C25B11/075—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound
- C25B11/089—Alloys
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/48—After-treatment of electroplated surfaces
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/60—Electroplating characterised by the structure or texture of the layers
- C25D5/623—Porosity of the layers
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- Electroplating And Plating Baths Therefor (AREA)
Abstract
本发明公开了一种特殊结构钴基合金膜层的制备方法及产品,属于金属材料技术领域。钴基合金膜层的制备方法,包括以下步骤:将金属基底材料浸入酸性复合镀液中进行复合电沉积,然后再浸入碱性溶液中浸泡腐蚀,得到所述钴基合金膜层;所述酸性复合镀液的制备包括:将钴盐、钨盐和Al2O3颗粒加入溶剂中混合后调节pH值至酸性得到所述酸性复合镀液。该钴基合金膜层耐磨性能提高,析氢过电位减小,析氢性能提高,具有优良的催化性能。
The invention discloses a preparation method and product of a cobalt-based alloy film layer with a special structure, and belongs to the technical field of metal materials. The preparation method of the cobalt-based alloy film layer includes the following steps: immersing the metal base material in an acidic composite plating solution for composite electrodeposition, and then immersing it in an alkaline solution for immersion corrosion to obtain the cobalt-based alloy film layer; the acidic The preparation of the composite plating solution includes: adding cobalt salt, tungsten salt and Al 2 O 3 particles into a solvent, mixing, and then adjusting the pH value to acidic to obtain the acidic composite plating solution. The cobalt-based alloy film layer has improved wear resistance, reduced hydrogen evolution overpotential, improved hydrogen evolution performance, and has excellent catalytic performance.
Description
技术领域Technical field
本发明涉及金属材料技术领域,特别是涉及一种特殊结构钴基合金膜层的制备方法及产品。The invention relates to the technical field of metal materials, and in particular to a preparation method and product of a special structure cobalt-based alloy film layer.
背景技术Background technique
在众多清洁能源中,氢能作为一种经济、高效、可持续的绿色能源,是最为理想的能源载体之一,其受到了越来越广泛的关注。在多种制氢技术中,水电解离制氢被认为是通往“氢经济”的最有效途径之一。然而在实际应用中,水电解离制氢往往需要克服较高的析氢过电位,从而造成较高的能源损耗,为有效解决水电解离析氢过电位过高的技术瓶颈,高效催化材料的应用是突破此瓶颈的技术关键。目前贵金属铂及其合金是最为有效的析氢催化剂,但价格高昂、资源稀少以及电化学稳定性较差等不足限制了其规模化应用,粉末状催化剂受限于粘合剂和电化学稳定性。因此,亟需开发一种机械强度高、催化活性良好的非贵金属电极材料。Among many clean energy sources, hydrogen energy, as an economical, efficient and sustainable green energy, is one of the most ideal energy carriers and has received more and more widespread attention. Among various hydrogen production technologies, water electrolysis to produce hydrogen is considered to be one of the most effective ways to lead to the "hydrogen economy". However, in practical applications, water electrolysis to produce hydrogen often needs to overcome a high hydrogen evolution overpotential, resulting in high energy losses. In order to effectively solve the technical bottleneck of water electrolysis and hydrogen evolution overpotential being too high, the application of high-efficiency catalytic materials is The technical key to breaking through this bottleneck. At present, the precious metal platinum and its alloys are the most effective hydrogen evolution catalysts, but shortcomings such as high price, scarce resources, and poor electrochemical stability limit their large-scale application. Powdered catalysts are limited by binders and electrochemical stability. Therefore, there is an urgent need to develop a non-noble metal electrode material with high mechanical strength and good catalytic activity.
在众多非贵金属电催化材料中,过渡金属磷化物由于其独特的电子结构以及类金属特性,是催化反应活性高、稳定性好和成本效能佳的析氢电催化材料之一,其具有代替Pt基电催化材料的潜质。当前,水电解离析氢所用磷化物催化材料大多采用溶液水热合成工序和高温固相还原工序制备,其形态多为粉体,需在溶剂中充分分散,之后再利用Nafion溶液和聚偏氟乙烯有机溶液等粘结剂将其固定在导电载体上,这样催化电极的催化剂负载量有限,且粘结剂会降低电极材料的电传导性能,同时还存在粘结剂会包覆和遮蔽催化剂的部分活性点位,降低其催化性能;此外,长时间电解过程中,活性催化材料易从电极表面脱落,致使水电解离析氢催化电极稳定性差。而如何制备得到一种催化活性及耐磨性良好的非贵金属电极材料,成为本领域技术人员亟待解决的技术难题。Among many non-noble metal electrocatalytic materials, transition metal phosphide is one of the hydrogen evolution electrocatalytic materials with high catalytic activity, good stability and good cost-effectiveness due to its unique electronic structure and metal-like properties. It has the ability to replace Pt-based potential of electrocatalytic materials. At present, most of the phosphide catalytic materials used for hydrogen separation in water electrolysis are prepared by solution hydrothermal synthesis process and high-temperature solid-phase reduction process. Most of them are in the form of powder, which needs to be fully dispersed in the solvent, and then Nafion solution and polyvinylidene fluoride are used. Binders such as organic solutions are used to fix it on the conductive carrier, so that the catalyst loading capacity of the catalytic electrode is limited, and the binder will reduce the electrical conductivity of the electrode material, and there are also parts where the binder will coat and shield the catalyst. The active sites reduce its catalytic performance; in addition, during the long-term electrolysis process, the active catalytic material easily falls off the electrode surface, resulting in poor stability of the catalytic electrode for hydrogen separation in water electrolysis. How to prepare a non-noble metal electrode material with good catalytic activity and wear resistance has become an urgent technical problem for those skilled in the art to be solved.
发明内容Contents of the invention
本发明的目的是提供一种特殊结构钴基合金膜层的制备方法及产品,以解决现有技术中存在的问题,本发明在基底材料表面制备由钴、钨和Al2O3颗粒复合电沉积,再由NaOH溶液腐蚀去除Al2O3颗粒而成的具有特殊结构(将图1~2和图8进行对比,可以看出来特殊结构和原有结构,氧化铝颗粒去除后表面留下多孔)的钴基合金膜层,该膜层兼具耐磨性能及较高的析氢性能。The purpose of the present invention is to provide a method and product for preparing a cobalt-based alloy film layer with a special structure to solve the problems existing in the prior art. The present invention prepares a composite electrode composed of cobalt, tungsten and Al 2 O 3 particles on the surface of the base material. Deposition, and then etching the Al 2 O 3 particles with NaOH solution to form a special structure (comparing Figures 1 to 2 and Figure 8, you can see the special structure and the original structure. After the aluminum oxide particles are removed, the surface remains porous ) cobalt-based alloy film layer, which has both wear resistance and high hydrogen evolution performance.
为实现上述目的,本发明提供了如下方案In order to achieve the above objects, the present invention provides the following solutions
本发明的技术方案之一:One of the technical solutions of the present invention:
将金属基底材料浸入酸性复合镀液中进行复合电沉积,然后再浸入碱性溶液中浸泡腐蚀,得到所述钴基合金膜层;The metal base material is immersed in an acidic composite plating solution for composite electrodeposition, and then immersed in an alkaline solution for immersion corrosion to obtain the cobalt-based alloy film layer;
所述酸性复合镀液的制备包括:将钴盐、钨盐和Al2O3颗粒加入溶剂中混合后调节pH值至酸性得到所述酸性复合镀液。The preparation of the acidic composite plating solution includes: adding cobalt salt, tungsten salt and Al 2 O 3 particles into a solvent, mixing, and then adjusting the pH value to acidity to obtain the acidic composite plating solution.
Co-W合金膜层结构致密、硬度高、耐热性好、耐磨耐蚀性能优良。The Co-W alloy film layer has a dense structure, high hardness, good heat resistance, and excellent wear and corrosion resistance.
将氧化铝颗粒通过腐蚀的方法去除,可以在表面形成多孔结构,有效增大表面积,提高其电催化性能。Removing alumina particles through corrosion can form a porous structure on the surface, effectively increasing the surface area and improving its electrocatalytic performance.
进一步地,所述酸性复合镀液中钴盐的浓度为0.05~0.1mol/L,钨盐的浓度为0.05~0.1mol/L,Al2O3颗粒的浓度为10~30g/L;所述酸性复合镀液的pH值为4.5~6.0。Further, the concentration of cobalt salt in the acidic composite plating solution is 0.05-0.1 mol/L, the concentration of tungsten salt is 0.05-0.1 mol/L, and the concentration of Al 2 O 3 particles is 10-30 g/L; The pH value of the acidic composite plating solution is 4.5 to 6.0.
复合高浓度氧化铝颗粒的镀层厚度低于低浓度镀层。络合剂可以起到亮化、平整化和缓冲作用。The coating thickness of composite high-concentration alumina particles is lower than that of low-concentration coatings. Complexing agents can brighten, smooth and buffer.
进一步地,所述钴盐为硫酸钴;所述钨盐为钨酸钠。Further, the cobalt salt is cobalt sulfate; the tungsten salt is sodium tungstate.
进一步地,所述酸性复合镀液中还含有络合剂。Further, the acidic composite plating solution also contains a complexing agent.
进一步地,所述络合剂在酸性复合镀液中的浓度为0.2~0.4mol/L;所述络合剂为柠檬酸氢二铵。Further, the concentration of the complexing agent in the acidic composite plating solution is 0.2-0.4 mol/L; the complexing agent is diammonium hydrogen citrate.
进一步地,所述复合电沉积的条件为:恒电流密度,电流密度为10~50mA/cm2,电沉积时间为30~60min,电沉积温度为40~70℃。Further, the conditions of the composite electrodeposition are: constant current density, current density is 10~50mA/cm 2 , electrodeposition time is 30~60min, and electrodeposition temperature is 40~70°C.
进一步地,所述碱性溶液包括NaOH溶液;所述NaOH溶液的浓度为5~7mol/L。Further, the alkaline solution includes NaOH solution; the concentration of the NaOH solution is 5-7 mol/L.
进一步地,所述浸泡腐蚀的温度为60~80℃。Further, the temperature of the immersion corrosion is 60-80°C.
本发明的技术方案之二:一种上述制备方法制备的钴基合金膜层。The second technical solution of the present invention: a cobalt-based alloy film layer prepared by the above preparation method.
本发明的技术方案之三:一种上述钴基合金膜层在制备电极材料中的应用。The third technical solution of the present invention: the application of the above-mentioned cobalt-based alloy film layer in the preparation of electrode materials.
本发明公开了以下技术效果:The invention discloses the following technical effects:
(1)采用本发明的酸性复合镀液对基底材料进行复合电沉积,可以形成机械优异性能的Co-W合金膜层,进一步将其浸入NaOH溶液中进行腐蚀,最终在基底表面形成了厚度为10~13μm的特殊结构钴基合金膜层,该复合膜表面平整、特殊结构均匀,摩擦系数为0.5~0.8,在10-100mA/cm2的电流密度下腐蚀,其析氢过电位减小(与Co-W镀层的572mV相比),催化性能提高。(1) Using the acidic composite plating solution of the present invention to conduct composite electrodeposition on the base material, a Co-W alloy film layer with excellent mechanical properties can be formed, which is further immersed in a NaOH solution for corrosion, and finally a Co-W alloy film layer with a thickness of A 10-13μm special structure cobalt-based alloy film. The composite film has a smooth surface, a uniform special structure, and a friction coefficient of 0.5-0.8. When corroded at a current density of 10-100mA/ cm2 , its hydrogen evolution overpotential decreases (with Compared with 572mV of Co-W coating), the catalytic performance is improved.
(2)本发明制备得到的特殊结构的钴基合金膜层兼具耐磨性能及较高的析氢性能。(2) The specially structured cobalt-based alloy film prepared by the present invention has both wear resistance and high hydrogen evolution performance.
(3)本发明在现有的钴盐、钨盐复合共沉积的基础上,加入了Al2O3颗粒,三种物质在络合剂柠檬酸氢二铵的作用下复合共沉积,可以制得Co-W-Al2O3复合膜层,可以提高膜层的耐磨性。然后在NaOH溶液中腐蚀去除Al2O3颗粒,得到具有特殊结构的钴基合金膜层。钴基膜层本身具有优异的性能,而本发明使用的脱颗粒法制备特殊结构的钴基合金膜层,使膜层具有较大的孔隙率、比表面积和化学活性,进一步提高了膜层的力学性能和催化性能。另外,本发明采用复合电沉积和腐蚀脱颗粒的方式,得到的膜层具有耐磨、比表面积大(具有多孔结构,比表面积变大)及析氢性能高等优点。(3) On the basis of the existing composite co-deposition of cobalt salt and tungsten salt, the present invention adds Al 2 O 3 particles. The three substances are composite and co-deposited under the action of the complexing agent diammonium hydrogen citrate, which can be produced. The Co-W-Al 2 O 3 composite film layer is obtained, which can improve the wear resistance of the film layer. The Al 2 O 3 particles are then etched away in NaOH solution to obtain a cobalt-based alloy film with a special structure. The cobalt-based film layer itself has excellent performance, and the degranulation method used in the present invention prepares a cobalt-based alloy film layer with a special structure, so that the film layer has larger porosity, specific surface area and chemical activity, further improving the performance of the film layer. mechanical properties and catalytic properties. In addition, the present invention adopts composite electrodeposition and corrosion degranulation, and the obtained film layer has the advantages of wear resistance, large specific surface area (having a porous structure, the specific surface area becomes larger), and high hydrogen evolution performance.
(4)本发明的方法适合于制备电催化中(需要具有优异析氢性能、耐磨要求)的各种电极材料。(4) The method of the present invention is suitable for preparing various electrode materials in electrocatalysis (requiring excellent hydrogen evolution performance and wear resistance).
(5)本发明采用复合电沉积和腐蚀脱颗粒技术,提高了其析氢性能及力学性能。(5) The present invention adopts composite electrodeposition and corrosion degranulation technology to improve its hydrogen evolution performance and mechanical properties.
(6)本发明的制备方法操作简单、清洁环保、适用于复杂形状及有盲孔的金属材料,易于工业化。(6) The preparation method of the present invention is simple to operate, clean and environmentally friendly, suitable for metal materials with complex shapes and blind holes, and is easy to be industrialized.
附图说明Description of the drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the drawings needed to be used in the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some of the drawings of the present invention. Embodiments, for those of ordinary skill in the art, other drawings can also be obtained based on these drawings without exerting creative efforts.
图1为本发明实施例1制备的特殊结构钴基合金膜层的表面形貌图;Figure 1 is a surface morphology diagram of the special structure cobalt-based alloy film layer prepared in Example 1 of the present invention;
图2为本发明实施例2制备的特殊结构钴基合金膜层的表面形貌图;Figure 2 is a surface morphology diagram of the special structure cobalt-based alloy film layer prepared in Example 2 of the present invention;
图3为本发明实施例3制备的特殊结构钴基合金膜层的表面形貌图;Figure 3 is a surface morphology diagram of the special structure cobalt-based alloy film prepared in Example 3 of the present invention;
图4为本发明实施例4制备的特殊结构钴基合金膜层的表面形貌图;Figure 4 is a surface morphology diagram of the special structure cobalt-based alloy film prepared in Example 4 of the present invention;
图5为本发明实施例5制备的特殊结构钴基合金膜层的表面形貌图;Figure 5 is a surface morphology diagram of the special structure cobalt-based alloy film layer prepared in Example 5 of the present invention;
图6为本发明实施例6制备的特殊结构钴基合金膜层的表面形貌图;Figure 6 is a surface morphology diagram of the special structure cobalt-based alloy film layer prepared in Example 6 of the present invention;
图7为本发明对比例1制备的膜层的表面形貌图;Figure 7 is a surface morphology diagram of the film layer prepared in Comparative Example 1 of the present invention;
图8为本发明对比例2制备的膜层的表面形貌图;Figure 8 is a surface morphology diagram of the film layer prepared in Comparative Example 2 of the present invention;
图9为本发明对比例3制备的膜层的表面形貌图;Figure 9 is a surface morphology diagram of the film layer prepared in Comparative Example 3 of the present invention;
图10为本发明对比例4制备的膜层的表面形貌图;Figure 10 is a surface morphology diagram of the film layer prepared in Comparative Example 4 of the present invention;
图11为本发明对比例5制备的膜层的表面形貌图。Figure 11 is a surface morphology diagram of the film layer prepared in Comparative Example 5 of the present invention.
具体实施方式Detailed ways
现详细说明本发明的多种示例性实施方式,该详细说明不应认为是对本发明的限制,而应理解为是对本发明的某些方面、特性和实施方案的更详细的描述。Various exemplary embodiments of the invention will now be described in detail. This detailed description should not be construed as limitations of the invention, but rather as a more detailed description of certain aspects, features and embodiments of the invention.
应理解本发明中所述的术语仅仅是为描述特别的实施方式,并非用于限制本发明。另外,对于本发明中的数值范围,应理解为还具体公开了该范围的上限和下限之间的每个中间值。在任何陈述值或陈述范围内的中间值以及任何其他陈述值或在所述范围内的中间值之间的每个较小的范围也包括在本发明内。这些较小范围的上限和下限可独立地包括或排除在范围内。It should be understood that the terms used in the present invention are only used to describe particular embodiments and are not intended to limit the present invention. In addition, for numerical ranges in the present invention, it should be understood that every intermediate value between the upper and lower limits of the range is also specifically disclosed. Every smaller range between any stated value or value intermediate within a stated range and any other stated value or value intermediate within a stated range is also included within the invention. The upper and lower limits of these smaller ranges may independently be included or excluded from the range.
除非另有说明,否则本文使用的所有技术和科学术语具有本发明所述领域的常规技术人员通常理解的相同含义。虽然本发明仅描述了优选的方法和材料,但是在本发明的实施或测试中也可以使用与本文所述相似或等同的任何方法和材料。本说明书中提到的所有文献通过引用并入,用以公开和描述与所述文献相关的方法和材料。在与任何并入的文献冲突时,以本说明书的内容为准。Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Although only the preferred methods and materials are described herein, any methods and materials similar or equivalent to those described herein can be used in the practice or testing of the invention. All documents mentioned in this specification are incorporated by reference to disclose and describe the methods and materials in connection with which they were cited. In the event of conflict with any incorporated document, the contents of this specification shall prevail.
在不背离本发明的范围或精神的情况下,可对本发明说明书的具体实施方式做多种改进和变化,这对本领域技术人员而言是显而易见的。由本发明的说明书得到的其他实施方式对技术人员而言是显而易见的。本申请说明书和实施例仅是示例性的。It will be apparent to those skilled in the art that various modifications and changes can be made to the specific embodiments described herein without departing from the scope or spirit of the invention. Other embodiments will be apparent to the skilled person from the description of the invention. The specification and examples are intended to be illustrative only.
关于本文中所使用的“包含”、“包括”、“具有”、“含有”等等,均为开放性的用语,即意指包含但不限于。The words "includes", "includes", "has", "contains", etc. used in this article are all open terms, which mean including but not limited to.
实施例1Example 1
一种特殊结构钴基合金膜层的制备方法:Preparation method of a special structure cobalt-based alloy film layer:
(1)酸性复合镀液的制备:将硫酸钴、钨酸钠、络合剂(柠檬酸氢二铵)、氧化铝颗粒(粒径1μm)依次加入溶剂水中混合,溶解,搅拌均匀,得到酸性复合镀液。(1) Preparation of acidic composite plating solution: Add cobalt sulfate, sodium tungstate, complexing agent (diammonium hydrogen citrate), and alumina particles (particle size 1 μm) into the solvent water in sequence, mix, dissolve, and stir evenly to obtain acidic Composite plating solution.
其中各组分的浓度分别为:硫酸钴0.1mol/L,钨酸钠0.1mol/L,络合剂(柠檬酸氢二铵)0.2mol/L,氧化铝颗粒20g/L。酸性复合镀液的温度为60℃恒定温度,pH值为5.0。The concentrations of each component are: cobalt sulfate 0.1 mol/L, sodium tungstate 0.1 mol/L, complexing agent (diammonium hydrogen citrate) 0.2 mol/L, and alumina particles 20 g/L. The temperature of the acidic composite plating solution is a constant temperature of 60°C, and the pH value is 5.0.
(2)将金属基底材料浸入酸性复合镀液中进行复合电沉积(复合电沉积在空气搅拌的条件下进行,采用恒电流密度,电流密度为20mA/cm2,电沉积时间为60min,电沉积的温度为60℃),电沉积结束后取出、水洗、冷风吹干;然后浸入含有NaOH溶液(浓度为5mol/L)的恒温(80℃)反应器中,空气搅拌下腐蚀60min脱去氧化铝颗粒,取出、水洗、冷风吹干,得到特殊结构钴基合金膜层(具有复合膜层的基底材料)。(2) Immerse the metal base material into the acidic composite plating solution for composite electrodeposition (composite electrodeposition is carried out under air stirring conditions, using a constant current density, the current density is 20mA/cm 2 , the electrodeposition time is 60min, and the electrodeposition The temperature is 60℃), after the electrodeposition is completed, take it out, wash with water, and blow dry with cold air; then immerse it in a constant temperature (80℃) reactor containing NaOH solution (concentration: 5mol/L), and corrode for 60 minutes under air stirring to remove alumina. The particles are taken out, washed with water, and dried with cold air to obtain a special structure cobalt-based alloy film layer (base material with a composite film layer).
将制备得到的特殊结构钴基合金膜层置于扫描电镜下观察其表面形貌,结果如图1所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得特殊结构钴基合金膜层的厚度为13μm,摩擦系数为0.54,在10mA/cm2的电流密度下腐蚀,其析氢过电位为532mV,与Co-W镀层的572mV相比减小了40mV。The prepared special structure cobalt-based alloy film layer was placed under a scanning electron microscope to observe its surface morphology. The results are shown in Figure 1. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained special structure cobalt-based alloy film is 13μm, the friction coefficient is 0.54, and when corroded at a current density of 10mA/ cm2 , its hydrogen evolution overpotential is 532mV, which is reduced compared with the 572mV of the Co-W coating. 40mV.
实施例2Example 2
一种特殊结构钴基合金膜层的制备方法:Preparation method of a special structure cobalt-based alloy film layer:
(1)酸性复合镀液的制备:将硫酸钴、钨酸钠、络合剂(柠檬酸氢二铵)、氧化铝颗粒(粒径1μm)依次加入溶剂水中混合,溶解,搅拌均匀,得到酸性复合镀液。(1) Preparation of acidic composite plating solution: Add cobalt sulfate, sodium tungstate, complexing agent (diammonium hydrogen citrate), and alumina particles (particle size 1 μm) into the solvent water in sequence, mix, dissolve, and stir evenly to obtain acidic Composite plating solution.
其中各组分的浓度分别为:硫酸钴0.1mol/L,钨酸钠0.1mol/L,络合剂(柠檬酸氢二铵)0.2mol/L,氧化铝颗粒10g/L。酸性复合镀液的温度为60℃恒定温度,pH值为5.0。The concentrations of each component are: cobalt sulfate 0.1 mol/L, sodium tungstate 0.1 mol/L, complexing agent (diammonium hydrogen citrate) 0.2 mol/L, and alumina particles 10 g/L. The temperature of the acidic composite plating solution is a constant temperature of 60°C, and the pH value is 5.0.
(2)将金属基底材料浸入酸性复合镀液中进行复合电沉积(复合电沉积在空气搅拌的条件下进行,采用恒电流密度,电流密度为20mA/cm2,电沉积时间为60min,电沉积的温度为60℃),电沉积结束后取出、水洗、冷风吹干;然后浸入含有NaOH溶液(浓度为5mol/L)的恒温(80℃)反应器中,空气搅拌下腐蚀60min脱去氧化铝颗粒,取出、水洗、冷风吹干,得到特殊结构钴基合金膜层(具有复合膜层的基底材料)。(2) Immerse the metal base material into the acidic composite plating solution for composite electrodeposition (composite electrodeposition is carried out under air stirring conditions, using a constant current density, the current density is 20mA/cm 2 , the electrodeposition time is 60min, and the electrodeposition The temperature is 60℃), after the electrodeposition is completed, take it out, wash with water, and blow dry with cold air; then immerse it in a constant temperature (80℃) reactor containing NaOH solution (concentration: 5mol/L), and corrode for 60 minutes under air stirring to remove alumina. The particles are taken out, washed with water, and dried with cold air to obtain a special structure cobalt-based alloy film layer (base material with a composite film layer).
将制备得到的特殊结构钴基合金膜层置于扫描电镜下观察其表面形貌,结果如图2所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得特殊结构钴基合金膜层的厚度为11μm,摩擦系数为0.53,在10mA/cm2的电流密度下腐蚀,其析氢过电位为567mV,与Co-W镀层的572mV相比减小了5mV。The surface morphology of the prepared special structure cobalt-based alloy film layer was observed under a scanning electron microscope. The results are shown in Figure 2. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained special structure cobalt-based alloy film is 11μm, the friction coefficient is 0.53, and when corroded at a current density of 10mA/ cm2 , its hydrogen evolution overpotential is 567mV, which is reduced compared with the 572mV of the Co-W coating. 5mV.
实施例3Example 3
一种特殊结构钴基合金膜层的制备方法:Preparation method of a special structure cobalt-based alloy film layer:
(1)酸性复合镀液的制备:将硫酸钴、钨酸钠、络合剂(柠檬酸氢二铵)、氧化铝颗粒(粒径1μm)依次加入溶剂水中混合,溶解,搅拌均匀,得到酸性复合镀液。(1) Preparation of acidic composite plating solution: Add cobalt sulfate, sodium tungstate, complexing agent (diammonium hydrogen citrate), and alumina particles (particle size 1 μm) into the solvent water in sequence, mix, dissolve, and stir evenly to obtain acidic Composite plating solution.
其中各组分的浓度分别为:硫酸钴0.1mol/L,钨酸钠0.1mol/L,络合剂(柠檬酸氢二铵)0.2mol/L,氧化铝颗粒30g/L。酸性复合镀液的温度为60℃恒定温度,pH值为5.0。The concentrations of each component are: cobalt sulfate 0.1 mol/L, sodium tungstate 0.1 mol/L, complexing agent (diammonium hydrogen citrate) 0.2 mol/L, and alumina particles 30 g/L. The temperature of the acidic composite plating solution is a constant temperature of 60°C, and the pH value is 5.0.
(2)将金属基底材料浸入酸性复合镀液中进行复合电沉积(复合电沉积在空气搅拌的条件下进行,采用恒电流密度,电流密度为20mA/cm2,电沉积时间为60min,电沉积的温度为60℃),电沉积结束后取出、水洗、冷风吹干;然后浸入含有NaOH溶液(浓度为5mol/L)的恒温(80℃)反应器中,空气搅拌下腐蚀60min脱去氧化铝颗粒,取出、水洗、冷风吹干,得到特殊结构钴基合金膜层(具有复合膜层的基底材料)。(2) Immerse the metal base material into the acidic composite plating solution for composite electrodeposition (composite electrodeposition is carried out under air stirring conditions, using a constant current density, the current density is 20mA/cm 2 , the electrodeposition time is 60min, and the electrodeposition The temperature is 60℃), after the electrodeposition is completed, take it out, wash with water, and blow dry with cold air; then immerse it in a constant temperature (80℃) reactor containing NaOH solution (concentration: 5mol/L), and corrode for 60 minutes under air stirring to remove alumina. The particles are taken out, washed with water, and dried with cold air to obtain a special structure cobalt-based alloy film layer (base material with a composite film layer).
将制备得到的特殊结构钴基合金膜层置于扫描电镜下观察其表面形貌,结果如图3所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得特殊结构钴基合金膜层的厚度为10μm,摩擦系数为0.68,在10mA/cm2的电流密度下腐蚀,其析氢过电位为543mV,与Co-W镀层的572mV相比减小了29mV。The prepared special structure cobalt-based alloy film layer was placed under a scanning electron microscope to observe its surface morphology. The results are shown in Figure 3. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained special structure cobalt-based alloy film is 10μm, the friction coefficient is 0.68, and when corroded at a current density of 10mA/ cm2 , its hydrogen evolution overpotential is 543mV, which is reduced compared with the 572mV of the Co-W coating. 29mV.
实施例4Example 4
一种特殊结构钴基合金膜层的制备方法:Preparation method of a special structure cobalt-based alloy film layer:
(1)酸性复合镀液的制备:将硫酸钴、钨酸钠、络合剂(柠檬酸氢二铵)、氧化铝颗粒(粒径80nm)依次加入溶剂水中混合,溶解,搅拌均匀,得到酸性复合镀液。(1) Preparation of acidic composite plating solution: Add cobalt sulfate, sodium tungstate, complexing agent (diammonium hydrogen citrate), and alumina particles (particle size 80nm) into the solvent water in sequence, mix, dissolve, and stir evenly to obtain acidic Composite plating solution.
其中各组分的浓度分别为:硫酸钴0.1mol/L,钨酸钠0.1mol/L,络合剂(柠檬酸氢二铵)0.2mol/L,氧化铝颗粒10g/L。酸性复合镀液的温度为60℃恒定温度,pH值为5.0。The concentrations of each component are: cobalt sulfate 0.1 mol/L, sodium tungstate 0.1 mol/L, complexing agent (diammonium hydrogen citrate) 0.2 mol/L, and alumina particles 10 g/L. The temperature of the acidic composite plating solution is a constant temperature of 60°C, and the pH value is 5.0.
(2)将金属基底材料浸入酸性复合镀液中进行复合电沉积(复合电沉积在空气搅拌的条件下进行,采用恒电流密度,电流密度为20mA/cm2,电沉积时间为60min,电沉积的温度为60℃),电沉积结束后取出、水洗、冷风吹干;然后浸入含有NaOH溶液(浓度为5mol/L)的恒温(80℃)反应器中,空气搅拌下腐蚀60min脱去氧化铝颗粒,取出、水洗、冷风吹干,得到特殊结构钴基合金膜层(具有复合膜层的基底材料)。(2) Immerse the metal base material into the acidic composite plating solution for composite electrodeposition (composite electrodeposition is carried out under air stirring conditions, using a constant current density, the current density is 20mA/cm 2 , the electrodeposition time is 60min, and the electrodeposition The temperature is 60℃), after the electrodeposition is completed, take it out, wash with water, and blow dry with cold air; then immerse it in a constant temperature (80℃) reactor containing NaOH solution (concentration: 5mol/L), and corrode for 60 minutes under air stirring to remove alumina. The particles are taken out, washed with water, and dried with cold air to obtain a special structure cobalt-based alloy film layer (base material with a composite film layer).
将制备得到的特殊结构钴基合金膜层置于扫描电镜下观察其表面形貌,结果如图4所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得特殊结构钴基合金膜层的厚度为12μm,摩擦系数为0.69,在10mA/cm2的电流密度下腐蚀,其析氢过电位为561mV,与Co-W镀层的572mV相比减小了11mV。The prepared special structure cobalt-based alloy film layer was placed under a scanning electron microscope to observe its surface morphology. The results are shown in Figure 4. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained special structure cobalt-based alloy film is 12μm, the friction coefficient is 0.69, and when corroded at a current density of 10mA/ cm2 , its hydrogen evolution overpotential is 561mV, which is reduced compared with the 572mV of the Co-W coating. 11mV.
实施例5Example 5
一种特殊结构钴基合金膜层的制备方法:Preparation method of a special structure cobalt-based alloy film layer:
(1)酸性复合镀液的制备:将硫酸钴、钨酸钠、络合剂(柠檬酸氢二铵)、氧化铝颗粒(粒径5μm)依次加入溶剂水中混合,溶解,搅拌均匀,得到酸性复合镀液。(1) Preparation of acidic composite plating solution: Add cobalt sulfate, sodium tungstate, complexing agent (diammonium hydrogen citrate), and alumina particles (particle size 5 μm) into the solvent water in sequence, mix, dissolve, and stir evenly to obtain acidic Composite plating solution.
其中各组分的浓度分别为:硫酸钴0.1mol/L,钨酸钠0.1mol/L,络合剂(柠檬酸氢二铵)0.2mol/L,氧化铝颗粒20g/L。酸性复合镀液的温度为60℃恒定温度,pH值为5.0。The concentrations of each component are: cobalt sulfate 0.1 mol/L, sodium tungstate 0.1 mol/L, complexing agent (diammonium hydrogen citrate) 0.2 mol/L, and alumina particles 20 g/L. The temperature of the acidic composite plating solution is a constant temperature of 60°C, and the pH value is 5.0.
(2)将金属基底材料浸入酸性复合镀液中进行复合电沉积(复合电沉积在空气搅拌的条件下进行,采用恒电流密度,电流密度为20mA/cm2,电沉积时间为60min,电沉积的温度为60℃),电沉积结束后取出、水洗、冷风吹干;然后浸入含有NaOH溶液(浓度为5mol/L)的恒温(80℃)反应器中,空气搅拌下腐蚀60min脱去氧化铝颗粒,取出、水洗、冷风吹干,得到特殊结构钴基合金膜层(具有复合膜层的基底材料)。(2) Immerse the metal base material into the acidic composite plating solution for composite electrodeposition (composite electrodeposition is carried out under air stirring conditions, using a constant current density, the current density is 20mA/cm 2 , the electrodeposition time is 60min, and the electrodeposition The temperature is 60℃), after the electrodeposition is completed, take it out, wash with water, and blow dry with cold air; then immerse it in a constant temperature (80℃) reactor containing NaOH solution (concentration: 5mol/L), and corrode for 60 minutes under air stirring to remove alumina. The particles are taken out, washed with water, and dried with cold air to obtain a special structure cobalt-based alloy film layer (base material with a composite film layer).
将制备得到的特殊结构钴基合金膜层置于扫描电镜下观察其表面形貌,结果如图5所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得特殊结构钴基合金膜层的厚度为12μm,摩擦系数为0.78,在10mA/cm2的电流密度下腐蚀,其析氢过电位为559mV,与Co-W镀层的572mV相比减小了13mV。The prepared special structure cobalt-based alloy film layer was placed under a scanning electron microscope to observe its surface morphology. The results are shown in Figure 5. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained special structure cobalt-based alloy film is 12μm, the friction coefficient is 0.78, and when corroded at a current density of 10mA/ cm2 , its hydrogen evolution overpotential is 559mV, which is reduced compared with the 572mV of the Co-W coating. 13mV.
实施例6Example 6
一种特殊结构钴基合金膜层的制备方法:Preparation method of a special structure cobalt-based alloy film layer:
(1)酸性复合镀液的制备:将硫酸钴、钨酸钠、络合剂(柠檬酸氢二铵)、氧化铝颗粒(粒径5μm)依次加入溶剂水中混合,溶解,搅拌均匀,得到酸性复合镀液。(1) Preparation of acidic composite plating solution: Add cobalt sulfate, sodium tungstate, complexing agent (diammonium hydrogen citrate), and alumina particles (particle size 5 μm) into the solvent water in sequence, mix, dissolve, and stir evenly to obtain acidic Composite plating solution.
其中各组分的浓度分别为:硫酸钴0.1mol/L,钨酸钠0.1mol/L,络合剂(柠檬酸氢二铵)0.2mol/L,氧化铝颗粒30g/L。酸性复合镀液的温度为60℃恒定温度,pH值为5.0。The concentrations of each component are: cobalt sulfate 0.1 mol/L, sodium tungstate 0.1 mol/L, complexing agent (diammonium hydrogen citrate) 0.2 mol/L, and alumina particles 30 g/L. The temperature of the acidic composite plating solution is a constant temperature of 60°C, and the pH value is 5.0.
(2)将金属基底材料浸入酸性复合镀液中进行复合电沉积(复合电沉积在空气搅拌的条件下进行,采用恒电流密度,电流密度为20mA/cm2,电沉积时间为60min,电沉积的温度为60℃),电沉积结束后取出、水洗、冷风吹干;然后浸入含有NaOH溶液(浓度为5mol/L)的恒温(80℃)反应器中,空气搅拌下腐蚀60min脱去氧化铝颗粒,取出、水洗、冷风吹干,得到特殊结构钴基合金膜层(具有复合膜层的基底材料)。(2) Immerse the metal base material into the acidic composite plating solution for composite electrodeposition (composite electrodeposition is carried out under air stirring conditions, using a constant current density, the current density is 20mA/cm 2 , the electrodeposition time is 60min, and the electrodeposition The temperature is 60℃), after the electrodeposition is completed, take it out, wash with water, and blow dry with cold air; then immerse it in a constant temperature (80℃) reactor containing NaOH solution (concentration: 5mol/L), and corrode for 60 minutes under air stirring to remove alumina. The particles are taken out, washed with water, and dried with cold air to obtain a special structure cobalt-based alloy film layer (base material with a composite film layer).
将制备得到的特殊结构钴基合金膜层置于扫描电镜下观察其表面形貌,结果如图6所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得特殊结构钴基合金膜层的厚度为11μm,摩擦系数为0.80,在10mA/cm2的电流密度下腐蚀,其析氢过电位为562mV,与Co-W镀层的572mV相比减小了10mV。The surface morphology of the prepared special structure cobalt-based alloy film layer was observed under a scanning electron microscope. The results are shown in Figure 6. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained special structure cobalt-based alloy film is 11μm, the friction coefficient is 0.80, and when corroded at a current density of 10mA/ cm2 , its hydrogen evolution overpotential is 562mV, which is reduced compared with the 572mV of the Co-W coating. 10mV.
对比例1Comparative example 1
同实施例1,区别在于,复合电沉积后未浸入NaOH溶液中进行腐蚀。Same as Example 1, except that the composite electrodeposition was not immersed in NaOH solution for corrosion.
将制备得到的膜层置于扫描电镜下观察其表面形貌,结果如图7所示,由图中可以看出,所得膜层表面平整,可见复合氧化铝颗粒。经检测,所得膜层的厚度为13μm,摩擦系数为0.58,其析氢过电位为568mV。The surface morphology of the prepared film was observed under a scanning electron microscope. The results are shown in Figure 7. It can be seen from the figure that the surface of the film is smooth and composite alumina particles can be seen. After testing, the thickness of the obtained film layer was 13 μm, the friction coefficient was 0.58, and its hydrogen evolution overpotential was 568 mV.
对比例2Comparative example 2
同实施例1,区别在于,步骤(1)中的酸性复合镀液中不含有氧化铝颗粒,复合电沉积后未浸入NaOH溶液中进行腐蚀。The same as Example 1, but the difference is that the acidic composite plating solution in step (1) does not contain aluminum oxide particles, and the composite electroplating solution is not immersed in NaOH solution for corrosion after composite electrodeposition.
将所得膜层(Co-W镀层)置于扫描电镜下观察其表面形貌,结果如图8所示,由图中可以看出,所得膜层表面平整,连续致密,无须状形貌。经检测,所得膜层的厚度为8μm,摩擦系数为0.63,其析氢过电位为572mV。The surface morphology of the obtained film layer (Co-W coating) was observed under a scanning electron microscope. The results are shown in Figure 8. It can be seen from the figure that the surface of the obtained film layer is smooth, continuous and dense, and has no whisker morphology. After testing, the thickness of the obtained film layer was 8 μm, the friction coefficient was 0.63, and its hydrogen evolution overpotential was 572 mV.
对比例3Comparative example 3
同实施例1,区别在于,氧化铝颗粒的粒径为30nm。Same as Example 1, except that the particle size of the alumina particles is 30 nm.
将所得膜层置于扫描电镜下观察其表面形貌,结果如图9所示,由图中可以看出,所得膜层表面平整、连续均匀、特殊结构不明显。经检测,所得膜层的厚度为11μm,摩擦系数为0.71,在10mA/cm2的电流密度下腐蚀,其析氢过电位为560mV,与Co-W镀层的572mV相比减小了12mV。The surface morphology of the obtained film layer was observed under a scanning electron microscope. The results are shown in Figure 9. It can be seen from the figure that the surface of the obtained film layer is smooth, continuous and uniform, and the special structure is not obvious. After testing, the thickness of the obtained film layer is 11 μm, the friction coefficient is 0.71, and the hydrogen evolution overpotential is 560 mV when corroded at a current density of 10 mA/ cm2 , which is 12 mV lower than the 572 mV of the Co-W coating.
对比例4Comparative example 4
同实施例1,区别在于,复合电沉积的电流密度为100mA/cm2。The same as Example 1, except that the current density of composite electrodeposition is 100 mA/cm 2 .
将所得复合膜层置于扫描电镜下观察其表面形貌,结果如图10所示,由图中可以看出,所得复合膜层表面平整、特殊结构均匀。经检测,所得复合膜层的厚度为10μm,摩擦系数为0.59,在100mA/cm2的电流密度下腐蚀,其析氢过电位为550mV,与Co-W镀层的572mV相比减小了22mV。The surface morphology of the obtained composite film layer was observed under a scanning electron microscope. The results are shown in Figure 10. It can be seen from the figure that the surface of the obtained composite film layer is smooth and the special structure is uniform. After testing, the thickness of the obtained composite film layer is 10 μm, the friction coefficient is 0.59, and the hydrogen evolution overpotential is 550 mV when corroded at a current density of 100 mA/ cm2 , which is 22 mV lower than the 572 mV of the Co-W coating.
对比例5Comparative example 5
同实施例1,区别在于,硫酸钴的浓度为0.15mol/L。Same as Example 1, except that the concentration of cobalt sulfate is 0.15 mol/L.
将所得膜层置于扫描电镜下观察其表面形貌,结果如图11所示,由图中可以看出,所得膜层表面平整、连续均匀、特殊结构不明显。经检测,所得膜层的厚度为5μm,摩擦系数为0.78,在10mA/cm2的电流密度下腐蚀,其析氢过电位为575mV,与Co-W镀层的572mV相比增加了3mV。The surface morphology of the obtained film layer was observed under a scanning electron microscope. The results are shown in Figure 11. It can be seen from the figure that the surface of the obtained film layer is smooth, continuous and uniform, and the special structure is not obvious. After testing, the thickness of the obtained film layer is 5 μm, the friction coefficient is 0.78, and the hydrogen evolution overpotential is 575 mV when corroded at a current density of 10 mA/ cm2 , which is an increase of 3 mV compared with the 572 mV of the Co-W coating.
以上所述的实施例仅是对本发明的优选方式进行描述,并非对本发明的范围进行限定,在不脱离本发明设计精神的前提下,本领域普通技术人员对本发明的技术方案做出的各种变形和改进,均应落入本发明权利要求书确定的保护范围内。The above-described embodiments only describe the preferred modes of the present invention and do not limit the scope of the present invention. Without departing from the design spirit of the present invention, those of ordinary skill in the art can make various modifications to the technical solutions of the present invention. All deformations and improvements shall fall within the protection scope determined by the claims of the present invention.
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