CN110565113A - Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution - Google Patents
Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution Download PDFInfo
- Publication number
- CN110565113A CN110565113A CN201910773071.8A CN201910773071A CN110565113A CN 110565113 A CN110565113 A CN 110565113A CN 201910773071 A CN201910773071 A CN 201910773071A CN 110565113 A CN110565113 A CN 110565113A
- Authority
- CN
- China
- Prior art keywords
- composite
- electrocatalytic
- tio
- cfp
- hydrogen evolution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002131 composite material Substances 0.000 title claims abstract description 42
- 239000000463 material Substances 0.000 title claims abstract description 40
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 239000001257 hydrogen Substances 0.000 title claims abstract description 33
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 229910018661 Ni(OH) Inorganic materials 0.000 claims abstract description 56
- 229910010413 TiO 2 Inorganic materials 0.000 claims abstract description 39
- 238000000034 method Methods 0.000 claims abstract description 27
- 239000002135 nanosheet Substances 0.000 claims abstract description 22
- 238000000137 annealing Methods 0.000 claims abstract description 12
- 229920000049 Carbon (fiber) Polymers 0.000 claims abstract description 11
- 239000004917 carbon fiber Substances 0.000 claims abstract description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 11
- 230000003197 catalytic effect Effects 0.000 claims abstract description 10
- 230000000694 effects Effects 0.000 claims abstract description 9
- 238000000576 coating method Methods 0.000 claims abstract description 8
- 238000002425 crystallisation Methods 0.000 claims abstract description 8
- 230000008025 crystallization Effects 0.000 claims abstract description 8
- 239000011248 coating agent Substances 0.000 claims abstract description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000010936 titanium Substances 0.000 claims abstract description 4
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 4
- 238000009713 electroplating Methods 0.000 claims abstract 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 239000010411 electrocatalyst Substances 0.000 claims description 26
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 239000002243 precursor Substances 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 8
- 239000002060 nanoflake Substances 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- 239000004408 titanium dioxide Substances 0.000 claims description 7
- 229910017855 NH 4 F Inorganic materials 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 5
- 238000000859 sublimation Methods 0.000 claims description 5
- 230000008022 sublimation Effects 0.000 claims description 5
- 239000013078 crystal Substances 0.000 claims description 4
- 239000012153 distilled water Substances 0.000 claims description 4
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 claims description 4
- 238000007747 plating Methods 0.000 claims description 4
- 238000001771 vacuum deposition Methods 0.000 claims description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 3
- 229910018590 Ni(NO3)2-6H2O Inorganic materials 0.000 claims description 2
- 238000011049 filling Methods 0.000 claims description 2
- 239000006260 foam Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims description 2
- -1 polytetrafluoroethylene Polymers 0.000 claims 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims 1
- 239000004810 polytetrafluoroethylene Substances 0.000 claims 1
- 239000003054 catalyst Substances 0.000 abstract description 13
- 238000012546 transfer Methods 0.000 abstract description 3
- 230000006872 improvement Effects 0.000 abstract description 2
- 238000009827 uniform distribution Methods 0.000 abstract description 2
- 239000000758 substrate Substances 0.000 abstract 3
- 239000000523 sample Substances 0.000 description 14
- 238000005868 electrolysis reaction Methods 0.000 description 8
- 239000003792 electrolyte Substances 0.000 description 7
- 238000002149 energy-dispersive X-ray emission spectroscopy Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 229910021607 Silver chloride Inorganic materials 0.000 description 4
- 238000010494 dissociation reaction Methods 0.000 description 4
- 230000005593 dissociations Effects 0.000 description 4
- 238000000840 electrochemical analysis Methods 0.000 description 4
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000013112 stability test Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000002447 crystallographic data Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000013068 control sample Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 229910021508 nickel(II) hydroxide Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 229910052861 titanite Inorganic materials 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000002061 vacuum sublimation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/33—Electric or magnetic properties
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Electrochemistry (AREA)
- Metallurgy (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
Abstract
一种用于碱性电催化析氢的复合电催化材料的制备方法,所述方法在碳纤维纸上生长一层Ni(OH)2纳米片结构;在其表面真空电镀包覆钛的氧化物层;再置于空气气氛下360度温度的马弗炉中退火晶化得TiO2‑Ni(OH)2@CFP复合结构材料;所述TiO2‑Ni(OH)2@CFP在真空条件下,控制不同镀膜时间,空气气氛中退火晶化后得到不同时间镀膜后的复合电催化材料。本发明采用CFP为催化剂的基底材料,增大了复合电极的表面积,利于传质和提高了电极的电化学活性;同时水热在基底材料上生长的Ni(OH)2,降低了成本又使Ni(OH)2与基底材料结合更加牢固,分布均匀提高了催化剂的稳定性。本发明引入TiO2对于提高催化剂的催化性能和降低析氢过电位上起到了极大的作用;实现了电催化析氢活性的显著提高。
A preparation method of a composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution, the method grows one deck of Ni(OH) on carbon fiber paper 2 nanosheet structure; vacuum electroplating an oxide layer coated with titanium on its surface; Then placed in a muffle furnace at a temperature of 360 degrees under an air atmosphere to anneal and crystallize to obtain a TiO 2 ‑Ni(OH) 2 @CFP composite structure material; the TiO 2 ‑Ni(OH) 2 @CFP is controlled under vacuum conditions. Composite electrocatalytic materials after different coating times were obtained after annealing and crystallization in air atmosphere. The present invention uses CFP as the substrate material of the catalyst, which increases the surface area of the composite electrode, facilitates mass transfer and improves the electrochemical activity of the electrode; at the same time, Ni(OH) 2 grown on the substrate material by hydrothermal reduces the cost and enables Ni(OH) 2 is more firmly combined with the substrate material, and the uniform distribution improves the stability of the catalyst. The introduction of TiO 2 in the present invention plays a great role in improving the catalytic performance of the catalyst and reducing the hydrogen evolution overpotential; and realizes the remarkable improvement of the electrocatalytic hydrogen evolution activity.
Description
技术领域technical field
本发明涉及一种用于碱性电催化析氢的复合电催化材料的制备方法,属电催化技术领域。The invention relates to a preparation method of a composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution, belonging to the technical field of electrocatalysis.
背景技术Background technique
化石资源的过度消耗和随之带来的环境污染问题迫使我们急需开发和利用可替代化石燃料的可再生的清洁能源。作为一种清洁,高效,安全和可持续的新能源,氢能被视为21世纪最有前景的清洁能源。电解水制氢是解决目前这种困境的一种有效途径。但是电解水过程中过电位的存在使得电解水的能耗较高,因此我们需要开发高活性的析氢反应催化剂来降低水分解反应的过电位,从而提高能源转换效率。理想中的电解水应该以低成本和高产率来生产氢气,但由于目前高效产氢最有效的电催化剂仍然是以稀缺且昂贵的贵金属基材料(例如,Pt用于HER)为主,这不利于在工业上的大规模应用。因此,迫切需要开发过电位低、且地球上储量丰富的电解水催化剂来改善反应动力学和水电解效率。目前大多数HER电催化剂在酸性条件下比碱性条件更有效,由于电催化剂的HER过程在碱性介质中效率较低与电催化剂表面上水的缓慢解离过程有关,但电解水在碱性电解槽中进行时,碱性电解液具有容易获得且性能持久的优点,然而,目前致力于促进水在碱性电解液中解离的相关研究增多,但合成复合材料的性能仍不能令人满意,和基于贵金属的电催化剂相比仍具有较大差距,因此高性能电催化剂的开发仍然是一个巨大的挑战。The excessive consumption of fossil resources and the resulting environmental pollution force us to develop and utilize renewable clean energy that can replace fossil fuels. As a clean, efficient, safe and sustainable new energy, hydrogen energy is regarded as the most promising clean energy in the 21st century. Hydrogen production by electrolysis of water is an effective way to solve the current dilemma. However, the existence of overpotential in the process of water electrolysis leads to high energy consumption in electrolysis of water. Therefore, we need to develop highly active hydrogen evolution reaction catalysts to reduce the overpotential of water splitting reaction, thereby improving energy conversion efficiency. Ideal water electrolysis should produce hydrogen at low cost and high yield, but since the most effective electrocatalysts for efficient hydrogen production are still dominated by scarce and expensive noble metal-based materials (e.g., Pt for HER), this is not true. It is conducive to large-scale application in industry. Therefore, there is an urgent need to develop water electrolysis catalysts with low overpotential and earth-abundant reserves to improve the reaction kinetics and water electrolysis efficiency. Most of the current HER electrocatalysts are more efficient in acidic conditions than in alkaline conditions, because the HER process of electrocatalysts is less efficient in alkaline media, which is related to the slow dissociation process of water on the surface of the electrocatalyst, but the electrolysis of water in alkaline Alkaline electrolytes have the advantages of easy availability and long-lasting performance when carried out in electrolyzers. However, the current research on promoting water dissociation in alkaline electrolytes has increased, but the performance of synthesized composites is still unsatisfactory. , and there is still a large gap compared with noble metal-based electrocatalysts, so the development of high-performance electrocatalysts is still a great challenge.
镍基层状氢氧化物具有可控的组成和结构,不断地被研究人员证明复合其它材料后其电解水活性有一定提高,目前得到的镍基层状氢氧化物对电催化析氢性能较差,产品稳定性差,使用周期短,导电性差,不易回收,制备原材料成本较高,而且制备过程对环境污染较大等问题急需解决。性能优异的电催化剂应具有适中的氢离子吸附能力,TiO2可以促进水分子在其表面的吸附和解离,离解产生的氢中间体将从氧化钛表面通过溢流效应输送到电催化剂表面,从而提高负载体系的析氢催化活性。Nickel-based layered hydroxide has a controllable composition and structure. It has been continuously proved by researchers that its electrolytic water activity has been improved after being combined with other materials. The nickel-based layered hydroxide has poor electrocatalytic hydrogen evolution performance. Poor stability, short service life, poor conductivity, difficult recycling, high cost of raw materials for preparation, and relatively large environmental pollution during the preparation process need to be solved urgently. An electrocatalyst with excellent performance should have a moderate hydrogen ion adsorption capacity. TiO2 can promote the adsorption and dissociation of water molecules on its surface, and the hydrogen intermediate produced by the dissociation will be transported from the surface of titanium oxide to the surface of the electrocatalyst through the overflow effect, thereby Improve the hydrogen evolution catalytic activity of the loading system.
发明内容Contents of the invention
本发明的目的在于,为了制备适用于在碱性电解液中进行析氢反应的催化剂,提高催化剂的催化性能,保证电解水产氢快速、高效进行,本发明提供一种用于碱性电催化析氢的复合电催化材料的制备方法。The purpose of the present invention is to prepare a catalyst suitable for hydrogen evolution reaction in alkaline electrolyte, improve the catalytic performance of the catalyst, and ensure the rapid and efficient hydrogen production by electrolysis of water. The present invention provides a catalyst for alkaline electrocatalytic hydrogen evolution Preparation method of composite electrocatalytic material.
为解决上述技术问题,本发明采用如下技术方案:一种用于碱性电催化析氢的复合电催化材料的制备方法,所述方法制备的复合电催化材料为TiO2-Ni(OH)2@CFP复合结构材料。In order to solve the above technical problems, the present invention adopts the following technical scheme: a method for preparing a composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution, the composite electrocatalytic material prepared by the method is TiO 2 -Ni(OH) 2 @ CFP composite structural material.
所述复合结构材料制备方法为:在碳纤维纸上首先生长一层Ni(OH)2纳米片结构;然后在其表面真空电镀包覆钛的氧化物层,得到二氧化钛包覆的Ni(OH)2.nH2O纳米薄片电催化剂前驱体;再置于空气气氛一定温度下的马弗炉中退火晶化得TiO2-Ni(OH)2@CFP复合结构材料;所述TiO2-Ni(OH)2@CFP在真空条件下,控制不同镀膜时间,空气气氛中退火晶化后得到不同时间镀膜后的复合电催化材料为TiO2-Ni(OH)2@CFP-XXX,其中,XXX=20,40,80或120分钟。The preparation method of the composite structural material is as follows: first grow a layer of Ni(OH) 2 nanosheet structure on the carbon fiber paper; then vacuum electroplate an oxide layer coated with titanium on its surface to obtain titanium dioxide-coated Ni(OH) 2 .nH 2 O nanosheet electrocatalyst precursor; then placed in a muffle furnace at a certain temperature in the air atmosphere for annealing and crystallization to obtain a TiO 2 -Ni(OH) 2 @CFP composite structure material; the TiO 2 -Ni(OH) ) 2 @CFP Under vacuum conditions, control different coating times, and anneal and crystallize in air atmosphere to obtain composite electrocatalytic materials after coating at different times are TiO 2 -Ni(OH) 2 @CFP-XXX, where XXX=20 , 40, 80 or 120 minutes.
TiO2-Ni(OH)2@CFP-20,TiO2-Ni(OH)2@CFP-40,TiO2-Ni(OH)2@CFP-80,TiO2-Ni(OH)2@CFP-120分别为不同时间镀膜复合电催化剂。TiO 2 -Ni(OH) 2 @CFP-20, TiO 2 -Ni(OH) 2 @CFP-40, TiO 2 -Ni(OH) 2 @CFP-80, TiO 2 -Ni(OH) 2 @CFP- 120 are film-coated composite electrocatalysts at different times, respectively.
所述TiO2-Ni(OH)2@CFP复合结构材料为层状结构形貌,其初级结构Ni(OH)2纳米薄片,薄片厚度为20-40nm。The TiO 2 -Ni(OH) 2 @CFP composite structure material has a layered structure morphology, its primary structure is Ni(OH) 2 nano flakes, and the thickness of the flakes is 20-40nm.
所述TiO2-Ni(OH)2@CFP-XXX复合电催化材料的制备方法步骤如下:The preparation method steps of the TiO 2 -Ni(OH) 2 @CFP-XXX composite electrocatalytic material are as follows:
(1)在碳纤维纸上制备Ni(OH)2.nH2O纳米薄片(1) Preparation of Ni(OH) 2 .nH 2 O nanosheets on carbon fiber paper
将0.725克的Ni(NO3)2·6H2O,0.185克NH4F及0.625克CO(NH2)2加入到40毫升水中,快速搅拌至完全溶解,完毕后继续搅拌10分钟得混合溶液,然后将3×2cm2的碳纤维纸水平放置在反应釜底部,加入混合溶液,130℃反应12小时,反应结束后冷却至室温,用去离子水和无水乙醇洗涤,于80℃干燥6h,得淡绿色Ni(OH)2.nH2O纳米薄片均匀覆盖在泡沫镍表面;Add 0.725 g of Ni(NO 3 ) 2 ·6H 2 O, 0.185 g of NH 4 F and 0.625 g of CO(NH 2 ) 2 into 40 ml of water, stir rapidly until completely dissolved, then continue stirring for 10 minutes to obtain a mixed solution , then place 3×2cm 2 carbon fiber paper horizontally on the bottom of the reaction kettle, add the mixed solution, react at 130°C for 12 hours, cool to room temperature after the reaction, wash with deionized water and absolute ethanol, and dry at 80°C for 6h, Light green Ni(OH) 2 .nH 2 O nanosheets are uniformly covered on the surface of nickel foam;
(2)二氧化钛包覆Ni(OH)2.nH2O纳米薄片(2) TiO2-coated Ni(OH) 2 .nH 2 O nanoflakes
取步骤(1)合成的覆盖有淡绿色Ni(OH)2.nH2O纳米薄片放置到真空镀膜机中,喷升华镀液,调节喷涂时间分别为20、40、80、120分钟;反应结束后,在60℃真空干燥6h,得到二氧化钛包覆的Ni(OH)2.nH2O纳米薄片电催化剂前驱体;Take the light green Ni(OH) 2 .nH 2 O nanosheets synthesized in step (1) and place them in a vacuum coating machine, spray the sublimation plating solution, and adjust the spraying time to 20, 40, 80, and 120 minutes respectively; the reaction is over Afterwards, vacuum-dry at 60°C for 6 hours to obtain the Ni(OH) 2 .nH 2 O nanosheet electrocatalyst precursor coated with titania;
(3)取步骤(2)中的负载有二氧化钛包覆的Ni(OH)2.nH2O纳米薄片电催化剂前驱体碳纤维纸样品,将其放置于马弗炉中退火晶化,获得TiO2-Ni(OH)2@CFP-XXX复合催化材料。(3) Take the carbon fiber paper sample loaded with titanium dioxide-coated Ni(OH) 2 .nH 2 O nanosheet electrocatalyst precursor in step (2), place it in a muffle furnace for annealing and crystallization, and obtain TiO 2 -Ni(OH) 2 @CFP-XXX composite catalytic materials.
所述Ni(NO3)2·6H2O,NH4F及CO(NH2)2的摩尔比为1∶2∶5。The molar ratio of Ni(NO 3 ) 2 ·6H 2 O, NH 4 F and CO(NH 2 ) 2 is 1:2:5.
步骤(1)中,所述反应在容量为100毫升聚四氟乙烯内衬的反应釜中进行,填充度50-60%体积比。In step (1), the reaction is carried out in a polytetrafluoroethylene-lined reactor with a capacity of 100 milliliters, and the filling degree is 50-60% by volume.
步骤(2)中,所述升华镀液为钛酸丁酯及蒸馏水,真空度为30帕;所述钛酸丁酯及蒸馏水交替升华。In step (2), the sublimation plating solution is butyl titanate and distilled water, and the vacuum degree is 30 Pa; the butyl titanate and distilled water are alternately sublimated.
步骤(3)中,所述退火晶化过程中,退火温度为360℃,保温时间2h,加热速率5℃/min-1。In step (3), during the annealing and crystallization process, the annealing temperature is 360°C, the holding time is 2h, and the heating rate is 5°C/min -1 .
所述方法制备的复合结构电催化剂在20mA/cm-2的电流密度下的过电势为335mV,具有良好的电催化活性;电催化45小时后,仍维持90%以上的催化活性。The composite structure electrocatalyst prepared by the method has an overpotential of 335mV at a current density of 20mA/cm -2 , and has good electrocatalytic activity; after 45 hours of electrocatalysis, it still maintains more than 90% of the catalytic activity.
所述二氧化钛包覆的Ni(OH)2.nH2O纳米薄片电催化剂前驱体在空气氛下于360℃进行退火晶化;退火后无定型TiO2,晶化化为能提高催化性能的锐钛矿型,前驱体含结晶水的氢氧化镍失水转化为氢氧化镍。The titanium dioxide-coated Ni(OH) 2 .nH 2 O nanosheet electrocatalyst precursor is annealed and crystallized at 360°C in an air atmosphere; after annealing, the amorphous TiO 2 crystallizes into a sharp crystal that can improve catalytic performance. Titanite type, the precursor nickel hydroxide containing crystal water loses water and transforms into nickel hydroxide.
与现有技术相比,本发明的具有以下的优点:Compared with the prior art, the present invention has the following advantages:
(1)本发明电催化材料的制备方法,采用水热法和真空升华镀膜法制备TiO2-Ni(OH)2@CFP,不但制备条件易于控制,而且Ni(OH)2呈纳米薄片状负载于CFP上,提高了电极材料的表面积,促进了电极的电催化活性;真空镀膜方法的使用,镀膜均匀牢固,镀膜厚度可控;(1) The preparation method of the electrocatalytic material of the present invention adopts the hydrothermal method and the vacuum sublimation coating method to prepare TiO 2 -Ni(OH) 2 @CFP, not only the preparation conditions are easy to control, but also the Ni(OH)2 is loaded in the form of nano flakes On the CFP, the surface area of the electrode material is increased, and the electrocatalytic activity of the electrode is promoted; the use of the vacuum coating method, the coating is uniform and firm, and the thickness of the coating is controllable;
(2)本发明采用CFP为催化剂的基底材料,由于CFP呈网状的结构特点增大了复合电极的表面积,则有利于传质和提高了电极的电化学活性;同时水热在基底材料上生长的Ni(OH)2,降低了成本又使Ni(OH)2与基底材料结合更加牢固,分布均匀提高了催化剂的稳定性。(2) The present invention adopts CFP as the base material of catalyst, because the structure characteristic of CFP in network shape increases the surface area of composite electrode, then helps mass transfer and improves the electrochemical activity of electrode; The grown Ni(OH) 2 reduces the cost and makes the combination of Ni(OH) 2 and the base material stronger, and the uniform distribution improves the stability of the catalyst.
(3)本发明引入TiO2对于提高催化剂的催化性能和降低析氢过电位上起到了极大的作用,归功于TiO2与Ni之间的d电子相互作用改变了Ni电子结构,同时增强了催化剂对水分子的吸收而实现电催化析氢活性的显著提高。(3) The introduction of TiO 2 in the present invention has played a great role in improving the catalytic performance of the catalyst and reducing the hydrogen evolution overpotential, due to the d electron interaction between TiO 2 and Ni has changed the electronic structure of Ni, and at the same time strengthened the catalyst Significant improvement in electrocatalytic hydrogen evolution activity can be achieved by absorbing water molecules.
附图说明Description of drawings
图1是按照实施例的方法制备的复合电催化剂样品的X射线衍射图谱;Fig. 1 is the X-ray diffraction spectrum of the composite electrocatalyst sample prepared according to the method for embodiment;
图2是按照对比例和实施例的方法制备的样品的SEM图及EDS元素映射图;Fig. 2 is the SEM figure and the EDS element map of the sample prepared according to the method for comparative example and embodiment;
其中,图2(a)为低倍扫描电镜,图2(b-c)为高倍扫描电镜,图2(d-g)为SEM图像及EDX元素映射图,图2(e)为氧元素,图2(f)为镍元素,图2(g)为钛元素,图2(h)为EDS元素分析图;Among them, Figure 2(a) is a low-magnification scanning electron microscope, Figure 2(b-c) is a high-power scanning electron microscope, Figure 2(d-g) is a SEM image and an EDX element map, Figure 2(e) is an oxygen element, and Figure 2(f ) is a nickel element, Fig. 2 (g) is a titanium element, and Fig. 2 (h) is an EDS elemental analysis diagram;
图3是按照对比例和实施例的方法制备的样品的过电位曲线图;Fig. 3 is the overpotential curve figure of the sample prepared according to the method for comparative example and embodiment;
图4是按照对比例和实施例的方法制备的样品的Nyquist曲线;Fig. 4 is the Nyquist curve of the sample prepared according to the method of comparative example and embodiment;
图5是按照对比例和实施例的方法制备的样品的稳定性测试;Fig. 5 is the stability test of the sample prepared according to the method for comparative example and embodiment;
图6是用于碱性电催化析氢的复合电催化剂的制备流程。Figure 6 is the preparation process of the composite electrocatalyst for alkaline electrocatalytic hydrogen evolution.
具体实施方式Detailed ways
本发明的具体实施步骤如图6所示。The specific implementation steps of the present invention are shown in FIG. 6 .
本实施例采用的原料为Ni(NO3)2,NH4F,CO(NH2)2。The raw materials used in this example are Ni(NO 3 ) 2 , NH 4 F, CO(NH 2 ) 2 .
称取0.725克的Ni(NO3)2·6H2O,0.185克NH4F及0.625克CO(NH2)2快速搅拌至完全溶解,完毕后继续搅拌10min得混合溶液,混合并溶于40毫升水中;Weigh 0.725 g of Ni(NO 3 ) 2 6H 2 O, 0.185 g of NH 4 F and 0.625 g of CO(NH 2 ) 2 and stir quickly until completely dissolved, then continue stirring for 10 min to obtain a mixed solution, mix and dissolve in 40 ml of water;
然后取一张碳纤维纸(CFP)切成面积成2×3cm2的块状,分别依次在丙酮、乙醇和水中超声清洗15min,取出干燥称量;Then take a piece of carbon fiber paper (CFP) and cut it into a block with an area of 2×3cm 2 , ultrasonically clean it in acetone, ethanol and water for 15 minutes respectively, take it out and weigh it dry;
再在容积为50mL反应釜内胆中倒入上述溶液,并加入一片洗净的2×3cm2CFP,密封反应釜保持温度130℃下反应12h,用去离子水和无水乙醇洗涤,于80℃干燥6h,称量负载在碳纤维纸上前驱体的质量;Then pour the above solution into the inner tank of a 50mL reaction kettle, and add a piece of washed 2×3cm 2 CFP, seal the reaction kettle and keep the temperature at 130°C for 12 hours, wash with deionized water and absolute ethanol, and place at 80 Dry at ℃ for 6 hours, and weigh the mass of the precursor loaded on the carbon fiber paper;
取上述步骤合成的覆盖有淡绿色Ni(OH)2.nH2O纳米薄片放置到真空镀膜机中,升华镀液为钛酸丁酯,调节喷镀时间分别为20,40,80,120分钟;反应结束后,在60℃下真空干燥6h,得到二氧化钛包覆的Ni(OH)2.nH2O纳米薄片电催化剂前驱体;Take the light green Ni(OH) 2 .nH 2 O nanosheets synthesized in the above steps and place them in a vacuum coating machine. The sublimation plating solution is butyl titanate, and the spraying time is adjusted to 20, 40, 80, and 120 minutes respectively. ; after the reaction, vacuum drying at 60° C. for 6 hours to obtain a Ni(OH) 2 .nH 2 O nanosheet electrocatalyst precursor coated with titanium dioxide;
取上述合成的负载有二氧化钛包覆的Ni(OH)2.nH2O纳米薄片的碳纤维纸样品,将其放置于马弗炉中360℃下退火晶化,退火时间为2小时,并称重测负载量。Take the carbon fiber paper sample synthesized above loaded with titanium dioxide-coated Ni(OH) 2 .nH 2 O nanoflakes, place it in a muffle furnace for annealing and crystallization at 360°C for 2 hours, and weigh Measure the load.
对实施例获得的样品,用X射线衍射方法测得衍射数据,如图1所示。其中图1的曲线为测试制备的复合电催化剂样品得到的衍射数据。图1中的竖线为标准卡片数据。For the sample obtained in the embodiment, the diffraction data were measured by X-ray diffraction method, as shown in FIG. 1 . The curve in Figure 1 is the diffraction data obtained by testing the prepared composite electrocatalyst samples. The vertical lines in Figure 1 are standard card data.
从图1中可以看出,对样品进行指标化,其空间群为P-3m1,晶格常数为a=b=3.126,α=β=90°,γ=120°。晶格常数没有发生变化以及没有杂相,说明TiO2掺入到了化合物中量少未体现其晶体相。It can be seen from Figure 1 that the sample is indexed, its space group is P-3m1, and its lattice constant is a=b=3.126, α=β=90°, γ=120°. There is no change in the lattice constant and no impurity phase, indicating that TiO 2 is incorporated into the compound in a small amount and does not reflect its crystal phase.
对实施例获得的样品,用SEM扫描测定样品新貌,能量弥散X射线光谱(EDS)测得元素组成数据,如图2所示。For the sample obtained in the embodiment, the new appearance of the sample was measured by SEM scanning, and the elemental composition data was measured by energy dispersive X-ray spectroscopy (EDS), as shown in FIG. 2 .
图2显示TiO2-Ni(OH)2@CFP纳米薄片均质地沉积在CFP的表面,在CFP表面的单片纳米片的厚度大约为20-30nm。能量弥散X射线光谱(EDS)确认了在TiO2-Ni(OH)2@CFP中存在着Ni,Ti,和O。Figure 2 shows that TiO 2 -Ni(OH) 2 @CFP nanoflakes are homogeneously deposited on the surface of CFP, and the thickness of a single nanosheet on the surface of CFP is about 20-30nm. Energy dispersive X-ray spectroscopy (EDS) confirmed the presence of Ni, Ti, and O in TiO 2 -Ni(OH) 2 @CFP.
对比例和实施例样品的过电位曲线如图3所示。The overpotential curves of the samples of the comparative examples and the examples are shown in FIG. 3 .
通常采用-20mA/cm2时的过电位进行对比。显然,镀了TiO2层的样品的过电位绝对值比未镀TiO2层对比样品的过电位绝对值小了许多。未镀TiO2层样品在碱性条件下析氢的过电位超过500mV,镀上TiO2层80分钟后的电催化剂样品的过电位绝对值最低值降低到335mV,具有最优的电催化析氢性能。The overpotential at -20mA/cm 2 is usually used for comparison. Obviously, the absolute value of the overpotential of the sample coated with TiO 2 layer is much smaller than that of the control sample without TiO 2 layer. The hydrogen evolution overpotential of the uncoated TiO 2 layer sample exceeds 500mV under alkaline conditions, and the absolute value of the overpotential of the electrocatalyst sample coated with the TiO 2 layer for 80 minutes decreases to 335mV, which has the best electrocatalytic hydrogen evolution performance.
对比例和实施例样品的Nyquist曲线如图4所示。The Nyquist curves of the samples of the comparative example and the example are shown in FIG. 4 .
在低频范围的半圆与发生在电催化剂表面的法拉第过程(HER)有关。其对应的电阻成分是电荷转移电阻(Rct)。The semicircle in the low-frequency range is related to the Faradaic process (HER) occurring on the surface of the electrocatalyst. Its corresponding resistive component is the charge transfer resistance (R ct ).
Rct常被用来评估HER的动力学过程,一般Rct越小,HER过程越快。显然,在Ni(OH)2纳米薄片镀上TiO2之后Rct随之降低,这说明TiO2-Ni(OH)2@CFP纳米片在析氢反应中具有最快的电子传递能力。R ct is often used to evaluate the kinetic process of HER. Generally, the smaller the R ct is, the faster the HER process is. Obviously, R ct decreases after Ni(OH) 2 nanosheets are coated with TiO 2 , which indicates that TiO 2 -Ni(OH) 2 @CFP nanosheets have the fastest electron transfer ability in hydrogen evolution reaction.
材料的电催化性能测试:Electrocatalytic performance test of materials:
电化学测试采用三电极体系,通过CHI-614D电化学分析仪工作站测试,负载有催化剂的CFP为工作电极,碳棒电极作为对电极,银/氯化银电极(Ag/AgCl)作为参比电极。电化学测试电解液为1mol/L的KOH溶液,测试前在溶液中通氩气10min以除去电解液中的空气。The electrochemical test adopts a three-electrode system, which is tested by the CHI-614D electrochemical analyzer workstation. The CFP loaded with catalyst is used as the working electrode, the carbon rod electrode is used as the counter electrode, and the silver/silver chloride electrode (Ag/AgCl) is used as the reference electrode. . Electrochemical test electrolyte is 1mol/L KOH solution, and argon gas is passed through the solution for 10 minutes before the test to remove the air in the electrolyte.
实验结果表明:电催化析氢过电位为335mV时电流密度就能达到20mA/cm-2。The experimental results show that the current density can reach 20mA/cm -2 when the overpotential of electrocatalytic hydrogen evolution is 335mV.
稳定性实验:Stability test:
电化学测试采用三电极体系,通过CHI-614D电化学分析仪工作站测试,负载有催化剂的CFP为工作电极,碳棒电极作为对电极,银/氯化银电极(Ag/AgCl)作为参比电极。电化学测试电解液为1mol/L的KOH溶液,测试前在溶液中通氩气10min以除去电解液中的空气,稳定性测试保持恒电压为750mV。产品稳定性好,在750mV的恒电压下,电流密度40小时内降低不超过5%,且结构稳定,没有坍塌。The electrochemical test adopts a three-electrode system, which is tested by the CHI-614D electrochemical analyzer workstation. The CFP loaded with catalyst is used as the working electrode, the carbon rod electrode is used as the counter electrode, and the silver/silver chloride electrode (Ag/AgCl) is used as the reference electrode. . Electrochemical test electrolyte is 1mol/L KOH solution, argon gas is passed through the solution for 10 minutes before the test to remove the air in the electrolyte, and the stability test maintains a constant voltage of 750mV. The product has good stability. Under a constant voltage of 750mV, the current density does not decrease by more than 5% within 40 hours, and the structure is stable without collapse.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910773071.8A CN110565113B (en) | 2019-08-21 | 2019-08-21 | Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910773071.8A CN110565113B (en) | 2019-08-21 | 2019-08-21 | Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110565113A true CN110565113A (en) | 2019-12-13 |
CN110565113B CN110565113B (en) | 2021-03-26 |
Family
ID=68775798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910773071.8A Active CN110565113B (en) | 2019-08-21 | 2019-08-21 | Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110565113B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112058275A (en) * | 2020-08-19 | 2020-12-11 | 天津大学 | Alkaline photoelectrolysis water catalyst for thin film electrode and preparation method and application thereof |
CN112921337A (en) * | 2021-01-21 | 2021-06-08 | 三峡大学 | Ni/NiO/TiO2Preparation method of heterojunction material and application of heterojunction material in bifunctional catalytic electrolysis of water |
CN114308136A (en) * | 2021-07-30 | 2022-04-12 | 台湾塑胶工业股份有限公司 | Carbon fiber composite material and method for producing same |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106391027A (en) * | 2016-09-30 | 2017-02-15 | 浙江工业大学 | TiO2-Ni(OH)2 bilayer molecular film photocatalyst and its preparation method and application |
CN107326392A (en) * | 2017-05-24 | 2017-11-07 | 广西大学 | A kind of preparation method of bifunctional catalyst |
CN108716007A (en) * | 2018-05-30 | 2018-10-30 | 天津大学 | The method for improving hydroxide electrocatalytic hydrogen evolution reactivity worth by Lacking oxygen engineering |
CN109161921A (en) * | 2018-09-29 | 2019-01-08 | 陕西科技大学 | The preparation method of network structure zinc-nickel double-metal hydroxide bifunctional electrocatalyst |
CN109201103A (en) * | 2018-10-17 | 2019-01-15 | 大连理工大学 | A kind of full electrolysis water catalyst of monolithic porous economic benefits and social benefits base metal and synthetic method |
CN109647447A (en) * | 2019-01-14 | 2019-04-19 | 济南大学 | A kind of Ni (OH)2-NiTe2The preparation method of combined electrolysis water catalyst |
CN110038577A (en) * | 2019-05-20 | 2019-07-23 | 南昌航空大学 | Synthetic method of the one step growth in situ in the class alpha-phase nickel hydroxide nanometer sheet of carbon cloth substrate |
-
2019
- 2019-08-21 CN CN201910773071.8A patent/CN110565113B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106391027A (en) * | 2016-09-30 | 2017-02-15 | 浙江工业大学 | TiO2-Ni(OH)2 bilayer molecular film photocatalyst and its preparation method and application |
CN107326392A (en) * | 2017-05-24 | 2017-11-07 | 广西大学 | A kind of preparation method of bifunctional catalyst |
CN108716007A (en) * | 2018-05-30 | 2018-10-30 | 天津大学 | The method for improving hydroxide electrocatalytic hydrogen evolution reactivity worth by Lacking oxygen engineering |
CN109161921A (en) * | 2018-09-29 | 2019-01-08 | 陕西科技大学 | The preparation method of network structure zinc-nickel double-metal hydroxide bifunctional electrocatalyst |
CN109201103A (en) * | 2018-10-17 | 2019-01-15 | 大连理工大学 | A kind of full electrolysis water catalyst of monolithic porous economic benefits and social benefits base metal and synthetic method |
CN109647447A (en) * | 2019-01-14 | 2019-04-19 | 济南大学 | A kind of Ni (OH)2-NiTe2The preparation method of combined electrolysis water catalyst |
CN110038577A (en) * | 2019-05-20 | 2019-07-23 | 南昌航空大学 | Synthetic method of the one step growth in situ in the class alpha-phase nickel hydroxide nanometer sheet of carbon cloth substrate |
Non-Patent Citations (2)
Title |
---|
JINDOU HU 等: "Simple solid-state synthesis and improved performance of Ni(OH)2-TiO2 nanocomposites for photocatalytic H2 production", 《CERAMICS INTERNATIONAL》 * |
WEI ZHANG 等: "3D flower-like heterostructured TiO2@Ni(OH)2 microspheres for solar photocatalytic hydrogen production", 《CHINESE JOURNAL OF CATALYSIS》 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112058275A (en) * | 2020-08-19 | 2020-12-11 | 天津大学 | Alkaline photoelectrolysis water catalyst for thin film electrode and preparation method and application thereof |
CN112058275B (en) * | 2020-08-19 | 2022-11-01 | 天津大学 | Thin-film electrode alkaline photoelectrolysis water catalyst and its preparation method and application |
CN112921337A (en) * | 2021-01-21 | 2021-06-08 | 三峡大学 | Ni/NiO/TiO2Preparation method of heterojunction material and application of heterojunction material in bifunctional catalytic electrolysis of water |
CN112921337B (en) * | 2021-01-21 | 2022-02-01 | 三峡大学 | Ni/NiO/TiO2Preparation method of heterojunction material and application of heterojunction material in bifunctional catalytic electrolysis of water |
CN114308136A (en) * | 2021-07-30 | 2022-04-12 | 台湾塑胶工业股份有限公司 | Carbon fiber composite material and method for producing same |
US20230044426A1 (en) * | 2021-07-30 | 2023-02-09 | Formosa Plastics Corporation | Carbon fiber composites and method for producing the same |
US12048916B2 (en) * | 2021-07-30 | 2024-07-30 | Formosa Plastics Corporation | Carbon fiber composites and method for producing the same |
Also Published As
Publication number | Publication date |
---|---|
CN110565113B (en) | 2021-03-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109847778B (en) | Cobalt disulfide/carbon nitrogen composite material for oxygen evolution by electrolyzing water and synthetic method thereof | |
CN111282582A (en) | Preparation method of foam nickel-based catalyst for hydrogen production by water electrolysis | |
CN109518216B (en) | Cobalt phosphide nano-framework and preparation and application thereof | |
CN113430553B (en) | Double-function catalytic electrode based on transition metal heterogeneous layered structure and preparation method thereof | |
CN108447703B (en) | A kind of nickel-iron double metal hydroxide@ceria heterostructure nanosheet material, preparation method and application thereof | |
CN109012749A (en) | Nonmetallic difunctional VPO catalysts and its preparation method and application based on ZIF-8 phosphorus sulphur codope | |
CN108374179A (en) | A kind of preparation method and application of the compound nitrogen-doped carbon material of two cobaltous selenide of Fe2O3 doping | |
Li et al. | A three-dimensional flower-like NiCo-layered double hydroxide grown on nickel foam with an MXene coating for enhanced oxygen evolution reaction electrocatalysis | |
CN113005469A (en) | Ruthenium-loaded amorphous nickel hydroxide/nickel phosphide composite electrode and preparation method and application thereof | |
CN110565113A (en) | Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution | |
CN113512738A (en) | Ternary iron-nickel-molybdenum-based composite catalyst for water electrolysis, preparation method and application thereof | |
CN108315758A (en) | A kind of electrolysis aquatic products hydrogen catalyst and preparation method thereof | |
CN110292939A (en) | A kind of iridium nanocluster and its preparation method and application of double carbon confinements | |
CN113529122B (en) | Nickel-organic framework nano-sheet array material and preparation method and application thereof | |
CN115896848A (en) | Nitrogen/sulfur co-doped porous carbon loaded zinc monoatomic/metallic copper series catalyst and preparation method and application thereof | |
CN110743594A (en) | Nitrogen-doped carbon-supported tin and tin oxide nanocomposites and their preparation and applications | |
CN112023922B (en) | Pt-MnO2Material, preparation method and application thereof | |
US20230203675A1 (en) | Hydrogen evolution electrode and preparation method thereof | |
CN114214636B (en) | A method and application of a cobalt-based nanosheet self-supporting electrode prepared by a selenium-containing ligand | |
CN113174611B (en) | A self-supporting Al3Ni2/Ni catalytic hydrogen evolution electrode and its preparation method | |
CN108855139A (en) | A kind of titanium sheet, the preparation method and applications of surface modification sulfur doping titanium dioxide nanometer sheet | |
CN116426961A (en) | A kind of cobalt-based oxide electrocatalyst supported by foamed nickel and its preparation and application | |
CN110479286B (en) | A kind of preparation method of titanium-iron-nickel high hydrogen evolution active electrocatalyst | |
Li et al. | Electrochemical-leaching route for the size-controllable synthesis of copper-based oxygen reduction reaction catalysts: From nanoparticles to atomic clusters and single atoms | |
CN113930800A (en) | Heterostructure electrocatalytic hydrogen evolution material and preparation method and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
EE01 | Entry into force of recordation of patent licensing contract | ||
EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20191213 Assignee: JIANGXI GUANGYUAN CHEMICAL Co.,Ltd. Assignor: JINGGANGSHAN University Contract record no.: X2023980053575 Denomination of invention: Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution Granted publication date: 20210326 License type: Common License Record date: 20231221 |
|
EE01 | Entry into force of recordation of patent licensing contract | ||
EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20191213 Assignee: JIANGXI BAIXIN ELECTRIC PORCELAIN ELECTRIC CO.,LTD. Assignor: JINGGANGSHAN University Contract record no.: X2024980002577 Denomination of invention: Preparation method of composite electrocatalytic material for alkaline electrocatalytic hydrogen evolution Granted publication date: 20210326 License type: Common License Record date: 20240311 |