CN111282588A - Catalyst for hydrogen evolution by electrolyzing water and preparation method and application thereof - Google Patents
Catalyst for hydrogen evolution by electrolyzing water and preparation method and application thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 37
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 239000001257 hydrogen Substances 0.000 title claims abstract description 25
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 37
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 13
- 239000002243 precursor Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 12
- QIJNJJZPYXGIQM-UHFFFAOYSA-N 1lambda4,2lambda4-dimolybdacyclopropa-1,2,3-triene Chemical group [Mo]=C=[Mo] QIJNJJZPYXGIQM-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910039444 MoC Inorganic materials 0.000 claims abstract description 10
- 229920000767 polyaniline Polymers 0.000 claims abstract description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 8
- 230000003647 oxidation Effects 0.000 claims abstract description 7
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 7
- 239000002131 composite material Substances 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 16
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 claims description 12
- 239000008367 deionised water Substances 0.000 claims description 11
- 229910021641 deionized water Inorganic materials 0.000 claims description 11
- 229910021389 graphene Inorganic materials 0.000 claims description 9
- 238000001291 vacuum drying Methods 0.000 claims description 9
- 239000002041 carbon nanotube Substances 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 239000011609 ammonium molybdate Substances 0.000 claims description 7
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 claims description 7
- 229940010552 ammonium molybdate Drugs 0.000 claims description 7
- 235000018660 ammonium molybdate Nutrition 0.000 claims description 7
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 7
- 230000001681 protective effect Effects 0.000 claims description 7
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 6
- 239000003575 carbonaceous material Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 5
- 229910002804 graphite Inorganic materials 0.000 claims description 5
- 239000010439 graphite Substances 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 3
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- 229910017604 nitric acid Inorganic materials 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 1
- 238000000227 grinding Methods 0.000 claims 1
- 238000010992 reflux Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 2
- 239000003153 chemical reaction reagent Substances 0.000 abstract 1
- 238000000840 electrochemical analysis Methods 0.000 abstract 1
- 238000011065 in-situ storage Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000002441 X-ray diffraction Methods 0.000 description 3
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 3
- 102000011759 adducin Human genes 0.000 description 3
- 108010076723 adducin Proteins 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000001000 micrograph Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052573 porcelain Inorganic materials 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 239000011865 Pt-based catalyst Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 229910021397 glassy carbon Inorganic materials 0.000 description 2
- 238000004502 linear sweep voltammetry Methods 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 229920000557 Nafion® Polymers 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229940075397 calomel Drugs 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical compound Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- JAGQSESDQXCFCH-UHFFFAOYSA-N methane;molybdenum Chemical compound C.[Mo].[Mo] JAGQSESDQXCFCH-UHFFFAOYSA-N 0.000 description 1
- -1 molybdate ions Chemical class 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 239000002048 multi walled nanotube Substances 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 238000010301 surface-oxidation reaction Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000001075 voltammogram Methods 0.000 description 1
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- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/24—Nitrogen compounds
-
- 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
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- 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
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- 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
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- Inorganic Chemistry (AREA)
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Abstract
本发明公布了一种电解水析氢催化剂及其制备方法。所述析氢催化剂为担载于碳‑氮掺杂碳复合载体的碳化钼,其制备方法包括以下步骤:首先在碳载体上通过化学氧化法原位生长钼掺杂聚苯胺得到前驱体,将前驱体洗涤干燥后,然后在氮气保护下进行高温处理得到催化剂。本发明采用的试剂价格较低,生产流程短,电化学测试表明得到的催化剂催化析氢效果较好。The invention discloses a hydrogen evolution catalyst for electrolysis water and a preparation method thereof. The hydrogen evolution catalyst is molybdenum carbide supported on a carbon-nitrogen-doped carbon composite carrier, and the preparation method includes the following steps: firstly, a precursor is obtained by in-situ growth of molybdenum-doped polyaniline on the carbon carrier by a chemical oxidation method, and the precursor is After being washed and dried, the catalyst was obtained by high temperature treatment under nitrogen protection. The reagents used in the invention have low price and short production process, and electrochemical tests show that the obtained catalyst has a good effect of catalyzing hydrogen evolution.
Description
技术领域technical field
本发明属于电催化领域,具体涉及一种碳-氮掺杂碳(NC)基碳化钼(Mo2C)复合材料及其制备方法。The invention belongs to the field of electrocatalysis, and in particular relates to a carbon-nitrogen- doped carbon (NC)-based molybdenum carbide (Mo2C) composite material and a preparation method thereof.
背景技术Background technique
在当今社会,能源危机和环境污染已日益严峻,威胁着人类的生存和发展。氢能是一种十分重要的能源,由于氢气的高能量密度以及环境友好的特点,它被认为是可持续的能源存储的理想能源载体和化石燃料的替代物。而目前,氢气的生产依赖于化石燃料行业,因此也面临许多难题,如氢气纯度低和成本较高;而利用电流使水分解产生氢气和氧气是非常有效的产氢方法,而且生产成本相对较低,制备的氢气纯度高。In today's society, the energy crisis and environmental pollution have become increasingly severe, threatening the survival and development of human beings. Hydrogen energy is a very important energy source, which is considered as an ideal energy carrier for sustainable energy storage and an alternative to fossil fuels due to its high energy density and environmental friendliness. At present, the production of hydrogen depends on the fossil fuel industry, so it also faces many problems, such as low hydrogen purity and high cost; using electric current to split water to generate hydrogen and oxygen is a very effective hydrogen production method, and the production cost is relatively high. low, the hydrogen produced has high purity.
电解水产氢反应被认为是大规模工业产氢的一种高效的途径。其中贵金属展现了极其优异的催化活性,例如Pt基催化剂是目前公认的性质最佳的电解水产氢催化剂,但是贵金属由于储量有限且价格昂贵因而无法大规模推广应用。碳化钼是一种被认为可用来替代Pt基催化剂的高效析氢催化剂,为了提高导电性和改善传质,析氢催化剂常和各种碳载体进行复合以提高催化性能。Hydrogen production by electrolysis of water is considered to be an efficient route for large-scale industrial hydrogen production. Among them, noble metals show extremely excellent catalytic activity. For example, Pt-based catalysts are currently recognized as the best catalysts for water electrolysis and hydrogen production. However, due to their limited reserves and high prices, noble metals cannot be widely used in large-scale applications. Molybdenum carbide is an efficient hydrogen evolution catalyst that is considered to be a substitute for Pt-based catalysts. In order to improve electrical conductivity and improve mass transfer, hydrogen evolution catalysts are often compounded with various carbon supports to improve catalytic performance.
发明内容SUMMARY OF THE INVENTION
本发明提供了一种新的制备碳-氮掺杂碳基碳化钼材料的制备方法,同时制备的方法简单,并且在电解水析氢中有很好的催化效果。The invention provides a new preparation method for preparing carbon-nitrogen doped carbon-based molybdenum carbide material, and the preparation method is simple and has good catalytic effect in the hydrogen evolution of water electrolysis.
为实现上述目的,本发明提供了如下技术方案:For achieving the above object, the present invention provides the following technical solutions:
本发明一方面提供一种电解水用析氢催化剂的制备方法,所述方法包括如下步骤:One aspect of the present invention provides a method for preparing a hydrogen evolution catalyst for electrolysis of water, the method comprising the steps of:
步骤一:将碳载体进行氧化处理,并洗涤,在真空干燥箱中干燥;Step 1: The carbon carrier is oxidized, washed, and dried in a vacuum drying oven;
步骤二:将经步骤一处理的碳载体和钼酸铵溶于去离子水中,并加入一定量的苯胺,在冰浴中搅拌至钼酸铵溶解并恒温;Step 2: Dissolve the carbon carrier and ammonium molybdate treated in
步骤三:配置一定浓度过硫酸铵(NH4)2S2O8的HCl溶液,加入步骤二溶液中持续搅拌;Step 3: configure the HCl solution of ammonium persulfate (NH 4 ) 2 S 2 O 8 with a certain concentration, add it to the solution of
步骤四:混合溶液变为墨绿色,离心取下层沉淀并洗涤数次,在真空干燥箱中干燥得到钼掺杂的碳-聚苯胺前驱体;Step 4: the mixed solution becomes dark green, the lower layer is centrifuged to remove the precipitate and washed several times, and dried in a vacuum drying oven to obtain a molybdenum-doped carbon-polyaniline precursor;
步骤五:将步骤四中前驱体研磨成粉末,放入管式炉内,在保护气氛下热处理并自然冷却,得到碳-氮掺杂碳基碳化钼材料。Step 5: Grind the precursor in Step 4 into powder, put it into a tube furnace, heat treatment in a protective atmosphere and naturally cool to obtain a carbon-nitrogen doped carbon-based molybdenum carbide material.
基于以上技术方案,优选的,步骤一所述碳材料为石墨、碳纳米管中的任意一种。石墨烯的氧化处理,使用的是Hummers氧化法通过石墨制备氧化石墨烯。碳纳米管的氧化处理,为将碳纳米管在60~70℃浓硝酸中回流3~4h、洗涤至中性。Based on the above technical solutions, preferably, the carbon material in
基于以上技术方案,优选的,步骤一、步骤四的干燥是指在真空干燥箱中60~80℃干燥12~14h。Based on the above technical solutions, preferably, the drying in
基于以上技术方案,优选的,步骤五中所述保护气体为氮气、氩气中的任意一种。Based on the above technical solutions, preferably, the protective gas in step 5 is any one of nitrogen and argon.
基于以上技术方案,优选的,步骤五中所述热处理为以3~5℃/min速度升温至750~800℃处理3~4h。Based on the above technical solutions, preferably, the heat treatment in step 5 is to heat up to 750-800° C. at a rate of 3-5° C./min for 3-4 hours.
本发明另一方面提供一种上述方法制备的电解水用析氢催化剂,其特征在于,所述催化剂负载型催化剂,载体为碳-氮掺杂碳复合载体,被担载物为碳化钼。。Another aspect of the present invention provides a hydrogen evolution catalyst for water electrolysis prepared by the above method, characterized in that the catalyst-supported catalyst is a carbon-nitrogen doped carbon composite support, and the supported material is molybdenum carbide. .
本发明再一方面提供一种上述的电解水用析氢催化剂的应用,所述催化剂用于电解水析氢反应。Another aspect of the present invention provides an application of the above-mentioned hydrogen evolution catalyst for electrolysis of water, wherein the catalyst is used for the hydrogen evolution reaction of electrolyzed water.
本发明的优势在于:The advantages of the present invention are:
1.本发明利用苯胺和钼酸根离子的配位,并使之均匀聚合在碳载体上,有利于钼元素的分散,避免了后续高温过程中的团聚,暴露更多活性位点,提高电催化活性;1. The present invention utilizes the coordination of aniline and molybdate ions, and makes them uniformly polymerized on the carbon carrier, which is beneficial to the dispersion of molybdenum elements, avoids the agglomeration in the subsequent high temperature process, exposes more active sites, and improves electrocatalysis. active;
2.本发明制备过程简单,操作可控,催化性能较好,有在工业上应用的潜力。2. The preparation process of the invention is simple, the operation is controllable, the catalytic performance is good, and the invention has the potential of industrial application.
附图说明Description of drawings
图1为实施例1制备的Mo2C/rGO-NC的X射线衍射分析图;Fig. 1 is the X-ray diffraction analysis diagram of Mo 2 C/rGO-NC prepared in Example 1;
图2为实施例3制备的Mo2C/NC的X射线衍射分析图;Fig. 2 is the X-ray diffraction analysis diagram of Mo 2 C/NC prepared in Example 3;
图3为实施例2制备的Mo2C/CNTs-NC的X射线衍射分析图;3 is an X-ray diffraction analysis diagram of Mo 2 C/CNTs-NC prepared in Example 2;
图4为实施例1制备的Mo2C/rGO-NC的扫描电镜图;4 is a scanning electron microscope image of Mo 2 C/rGO-NC prepared in Example 1;
图5为实施例3制备的Mo2C/NC的扫描电镜图;5 is a scanning electron microscope image of Mo 2 C/NC prepared in Example 3;
图6为实施例2制备的Mo2C/CNTs-NC的扫描电镜图;6 is a scanning electron microscope image of Mo 2 C/CNTs-NC prepared in Example 2;
图7为实施例1制备的Mo2C/rGO-NC的EDX元素分布图;Fig. 7 is the EDX element distribution diagram of Mo 2 C/rGO-NC prepared in Example 1;
图8为实施例3制备的Mo2C/NC的EDX元素分布图;Fig. 8 is the EDX element distribution map of Mo 2 C/NC prepared in Example 3;
图9为实施例2制备的Mo2C/CNTs-NC的EDX元素分布图;Fig. 9 is the EDX element distribution diagram of Mo 2 C/CNTs-NC prepared in Example 2;
图10为实施例1、2、实施例3的线性扫描伏安曲线图;Fig. 10 is the linear sweep voltammogram of
图11为实施例1、2、3的塔菲尔斜率图。FIG. 11 is a Tafel slope diagram of Examples 1, 2, and 3. FIG.
具体实施方式Detailed ways
实施例1Example 1
使用Hummers法制备氧化石墨烯(GO):1g石墨鳞片、1g硝酸钠放入50mL浓硫酸并在冰浴下搅拌2h,缓慢加入4g高锰酸钾粉末并在冰浴下持续搅拌,转移至35℃油浴内进行中温反应2h,滴加150mL去离子水并升温至95℃,滴加完毕将产物分散在去离子水中,加入10mL过氧化氢和100mL10%wt盐酸搅拌离心,将沉淀放入透析袋中用去离子水透析至不含硫酸根离子,最后将产物用液氮冷冻并放入冷冻干燥机中干燥得到氧化石墨烯。取30mg氧化石墨烯,60mg钼酸铵溶于20mL去离子水中,滴加95mg苯胺并在冰浴中搅拌分散均匀,滴加配好的含0.4g过硫酸铵的0.5MHCl溶液10mL,在冰浴中反应4h。溶液变为墨绿色,离心并用去离子水洗涤数次,放入真空干燥箱中60℃干燥12h得到钼掺杂的氧化石墨烯-聚苯胺前驱体。将该前驱体放入瓷舟内,在管式炉中以氮气为保护气,5℃/min升温至800℃保持3h,再自然冷却,获得Mo2C/rGO-NC催化剂。Graphene oxide (GO) was prepared by Hummers method: 1 g of graphite flakes and 1 g of sodium nitrate were put into 50 mL of concentrated sulfuric acid and stirred for 2 h in an ice bath, and 4 g of potassium permanganate powder was slowly added and continuously stirred in an ice bath, and then transferred to 35 The reaction was carried out at a medium temperature in an oil bath for 2 hours, 150 mL of deionized water was added dropwise and the temperature was raised to 95 °C. After the dropwise addition, the product was dispersed in deionized water, and 10 mL of hydrogen peroxide and 100 mL of 10% wt hydrochloric acid were added to stir and centrifuge, and the precipitate was put into dialysis. The bag is dialyzed with deionized water until it does not contain sulfate ions, and finally the product is frozen with liquid nitrogen and dried in a freeze dryer to obtain graphene oxide. Take 30 mg of graphene oxide and 60 mg of ammonium molybdate and dissolve it in 20 mL of deionized water, add 95 mg of aniline dropwise and stir and disperse evenly in an ice bath. The reaction was carried out for 4 hours. The solution turned dark green, centrifuged and washed with deionized water for several times, and dried in a vacuum drying oven at 60°C for 12 h to obtain the molybdenum-doped graphene oxide-polyaniline precursor. The precursor was placed in a porcelain boat, and nitrogen was used as a protective gas in a tube furnace, heated to 800°C at 5°C/min for 3 hours, and then cooled naturally to obtain a Mo 2 C/rGO-NC catalyst.
实施例2Example 2
对碳纳米管(CNTs)进行表面氧化处理:1g多壁碳纳米管加入30mL浓硝酸中搅拌,并在60℃油浴下回流3h,产物经抽滤并用去离子水洗涤至中性,在真空干燥箱中60℃干燥12h得到。取30mg表面氧化碳纳米管,60mg钼酸铵溶于20mL去离子水中,滴加95mg苯胺并在冰浴中搅拌分散均匀,滴加配好的含0.4g过硫酸铵的0.5MHCl溶液10mL,在冰浴中反应4h。溶液变为墨绿色,离心并用去离子水洗涤数次,放入真空干燥箱中60℃干燥12h得到钼掺杂的碳纳米管-聚苯胺前驱体。将该前驱体放入瓷舟内,在管式炉中以氮气为保护气,5℃/min升温至800℃保持3h,再自然冷却,获得Mo2C/CNTs-NC催化剂。Surface oxidation treatment of carbon nanotubes (CNTs): 1 g of multi-walled carbon nanotubes was added to 30 mL of concentrated nitric acid and stirred, and refluxed in an oil bath at 60 °C for 3 h. Obtained by drying at 60°C for 12h in a drying oven. Dissolve 30 mg of surface oxidized carbon nanotubes and 60 mg of ammonium molybdate in 20 mL of deionized water, add 95 mg of aniline dropwise and stir to disperse evenly in an ice bath. The reaction in the bath was 4h. The solution turned dark green, centrifuged and washed with deionized water for several times, put into a vacuum drying oven at 60 °C for 12 h to obtain molybdenum-doped carbon nanotube-polyaniline precursor. The precursor was placed in a porcelain boat, and nitrogen was used as a protective gas in a tube furnace. The temperature was raised to 800°C at 5°C/min for 3 hours, and then cooled naturally to obtain a Mo 2 C/CNTs-NC catalyst.
实施例3Example 3
取60mg钼酸铵溶于20mL去离子水中,滴加95mg苯胺并在冰浴中搅拌分散均匀,滴加配好的含0.4g过硫酸铵的0.5MHCl溶液10mL,在冰浴中反应4h。溶液变为墨绿色,离心并用去离子水洗涤数次,放入真空干燥箱中60℃干燥12h得到钼掺杂聚苯胺前驱体。将该前驱体放入瓷舟内,在管式炉中以氮气为保护气,5℃/min升温至800℃保持3h,再自然冷却,获得Mo2C/NC催化剂。实施例3采用与实施例1和实施例2相同的步骤,但是不加入碳载体。Dissolve 60 mg of ammonium molybdate in 20 mL of deionized water, add 95 mg of aniline dropwise, stir and disperse evenly in an ice bath, add 10 mL of a prepared 0.5 M HCl solution containing 0.4 g of ammonium persulfate dropwise, and react in an ice bath for 4 h. The solution turned dark green, centrifuged and washed several times with deionized water, and then put it into a vacuum drying oven for drying at 60°C for 12 hours to obtain the molybdenum-doped polyaniline precursor. The precursor was put into a porcelain boat, and nitrogen was used as a protective gas in a tube furnace, and the temperature was raised to 800°C at 5°C/min for 3 hours, and then cooled naturally to obtain a Mo 2 C/NC catalyst. Example 3 followed the same procedure as Example 1 and Example 2, but without adding a carbon support.
从图1、图2和图3可知,催化剂衍射峰较不明显,说明碳化钼催化剂结晶度较低,有利于暴露更多的活性位点。在38.0°、39.6°、52.3°、61.9°、69.8°处能显示出碳化钼的特征峰,分别归属于六方β-Mo2C(JCPDS 65-8766)的(002)、(101)、(102)、(110)、(103)晶面。以上结果说明本发明的制备方法有利于形成较多氧空位。It can be seen from Figure 1, Figure 2 and Figure 3 that the diffraction peaks of the catalyst are less obvious, indicating that the molybdenum carbide catalyst has a lower crystallinity, which is beneficial to expose more active sites. The characteristic peaks of molybdenum carbide can be displayed at 38.0°, 39.6°, 52.3°, 61.9°, and 69.8°, which are assigned to (002), (101), ( 102), (110), (103) crystal planes. The above results show that the preparation method of the present invention is favorable for the formation of more oxygen vacancies.
从图4可知,催化剂基本保持了原本碳载体氧化石墨烯的形貌,为二维片状结构,孔洞较多有利于物质的传输。It can be seen from Figure 4 that the catalyst basically maintains the original morphology of carbon-supported graphene oxide, which is a two-dimensional sheet-like structure, and more holes are conducive to the transport of substances.
从图5可知,本发明采用的用聚苯胺作为前驱体合成的碳化钼催化剂粒径较小,有利于催化剂暴露更多活性位点。It can be seen from FIG. 5 that the molybdenum carbide catalyst synthesized by using polyaniline as a precursor in the present invention has a smaller particle size, which is beneficial for the catalyst to expose more active sites.
从图7、图8、图9可知,Mo、C、N元素为均匀分布,表明聚苯胺的热解产物为氮掺杂碳。It can be seen from Fig. 7, Fig. 8 and Fig. 9 that Mo, C, and N elements are uniformly distributed, indicating that the pyrolysis product of polyaniline is nitrogen-doped carbon.
电催化测试:将5mg催化剂和80μL5%Nafion溶液分散在异丙醇溶液中超声30min得到催化剂浆料。移取10μL催化剂浆料于5mm直径玻碳电极上,在红外烤灯下烘干成薄膜催化层。在三电极体系(玻碳电极为工作电极,碳棒为对电极,甘汞电极为参比电极,0.5M硫酸溶液为电解质溶液),测量线性扫描伏安曲线,测试结果如图10,并在10mAcm-2下测试催化剂的过电位。由线性扫描伏安曲线可得各试样的塔菲尔曲线,如图11。测试结果如下表:Electrocatalytic test: 5 mg of catalyst and 80 μL of 5% Nafion solution were dispersed in isopropanol solution and ultrasonicated for 30 min to obtain catalyst slurry.
由结果可知,本发明制备方法得到的催化剂中碳化钼的粒径小、结晶度低,有利于形成更多氧空位,利于反应;添加碳纳米管和氧化石墨烯作为碳源载体后制备的催化剂Mo2C/CNTs-NC和催化剂Mo2C/rGO-NC表现出更为优异的催化析氢性能,具有较低的过电位。It can be seen from the results that in the catalyst obtained by the preparation method of the present invention, the molybdenum carbide has small particle size and low crystallinity, which is conducive to the formation of more oxygen vacancies and is conducive to the reaction; the catalyst prepared by adding carbon nanotubes and graphene oxide as a carbon source carrier Mo 2 C/CNTs-NC and catalyst Mo 2 C/rGO-NC exhibited better catalytic hydrogen evolution performance with lower overpotential.
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