CN105731463B - A kind of preparation method and application of molybdenum carbide micron ball - Google Patents
A kind of preparation method and application of molybdenum carbide micron ball Download PDFInfo
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- QIJNJJZPYXGIQM-UHFFFAOYSA-N 1lambda4,2lambda4-dimolybdacyclopropa-1,2,3-triene Chemical compound [Mo]=C=[Mo] QIJNJJZPYXGIQM-UHFFFAOYSA-N 0.000 title claims abstract description 67
- 229910039444 MoC Inorganic materials 0.000 title claims abstract description 67
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- 239000001257 hydrogen Substances 0.000 claims abstract description 32
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 32
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000003957 anion exchange resin Substances 0.000 claims abstract description 15
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims abstract description 11
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical compound [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052750 molybdenum Inorganic materials 0.000 claims abstract description 10
- 239000011733 molybdenum Substances 0.000 claims abstract description 10
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003456 ion exchange resin Substances 0.000 claims abstract description 7
- 229920003303 ion-exchange polymer Polymers 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims abstract description 7
- 239000011347 resin Substances 0.000 claims abstract description 5
- 229920005989 resin Polymers 0.000 claims abstract description 5
- 239000000919 ceramic Substances 0.000 claims abstract description 4
- 239000011261 inert gas Substances 0.000 claims abstract description 3
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 238000006555 catalytic reaction Methods 0.000 claims description 6
- 239000003792 electrolyte Substances 0.000 claims description 5
- 235000015393 sodium molybdate Nutrition 0.000 claims description 4
- 239000011684 sodium molybdate Substances 0.000 claims description 4
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 claims description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 3
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 claims description 3
- 235000018660 ammonium molybdate Nutrition 0.000 claims description 3
- 239000011609 ammonium molybdate Substances 0.000 claims description 3
- 229940010552 ammonium molybdate Drugs 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 229910052700 potassium Inorganic materials 0.000 claims description 3
- 239000011591 potassium Substances 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- 239000011324 bead Substances 0.000 claims 2
- 230000005611 electricity Effects 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- 239000004005 microsphere Substances 0.000 abstract description 39
- 230000003197 catalytic effect Effects 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000002131 composite material Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 239000010411 electrocatalyst Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 239000000843 powder Substances 0.000 description 8
- 238000005868 electrolysis reaction Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- QXYJCZRRLLQGCR-UHFFFAOYSA-N dioxomolybdenum Chemical compound O=[Mo]=O QXYJCZRRLLQGCR-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 230000010287 polarization Effects 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 238000000026 X-ray photoelectron spectrum Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- -1 molybdenum ions Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000000634 powder X-ray diffraction Methods 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 101000878457 Macrocallista nimbosa FMRFamide Proteins 0.000 description 1
- 238000001069 Raman spectroscopy Methods 0.000 description 1
- 238000001237 Raman spectrum Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005349 anion exchange Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000002003 electron diffraction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000001420 photoelectron spectroscopy Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000004832 voltammetry Methods 0.000 description 1
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- 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
- B01J27/20—Carbon compounds
- B01J27/22—Carbides
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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
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
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- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
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Abstract
本发明公开了一种碳化钼微米球的制备方法,包括以下步骤:(1)将强碱性阴离子交换树脂加入钼酸盐溶液中,常温下搅拌反应,通过水洗,抽滤获得钼离子‑树脂复合物,干燥后得到含钼元素的离子交换树脂微球;(2)将步骤(1)得到的含钼元素的离子交换树脂微球置于到陶瓷坩埚中,在惰性气体保护下,于700~1000℃焙烧1~4小时,自然冷却至室温,得碳化钼微球。本发明还公开了碳化钼微米球在电解水产氢中的应用。本发明的制备条件要求低,原料廉价易得,制备得到的碳化钼微米球具有催化低过电位和稳定性好的电化学活性。
The invention discloses a preparation method of molybdenum carbide microspheres, comprising the following steps: (1) adding a strong basic anion exchange resin into a molybdate solution, stirring and reacting at normal temperature, washing with water, and suction filtering to obtain molybdenum ion-resin The composite is dried to obtain ion-exchange resin microspheres containing molybdenum; (2) the ion-exchange resin microspheres containing molybdenum obtained in step (1) are placed in a ceramic crucible, under the protection of an inert gas, at 700 Roasting at ~1000°C for 1 to 4 hours, then cooling naturally to room temperature to obtain molybdenum carbide microspheres. The invention also discloses the application of the molybdenum carbide microspheres in electrolyzing water to produce hydrogen. The preparation condition of the present invention is low, the raw material is cheap and easy to obtain, and the prepared molybdenum carbide microsphere has electrochemical activity with low catalytic overpotential and good stability.
Description
技术领域technical field
本发明涉及催化剂领域,特别涉及碳化钼微米球的制备方法及应用。The invention relates to the field of catalysts, in particular to a preparation method and application of molybdenum carbide microspheres.
背景技术Background technique
由于氢能资源丰富,来源广,氢的燃烧热值高,清洁无污染,越来越受到各国科学家的关注。电解水制氢是目前最为成熟,易于工业化,绿色环保的方法。传统的电解水产氢是将电解水催化剂粉体通过粘结剂负载在导电电极上进行电解水产氢。这种模式存在的问题是负载的催化剂容易脱落,而且粘结剂也会降低电催化剂活性,尤其是高负载量的情况下。碳化钼是一种高效的催化剂,广泛应用于电解水产氢和加氢脱硫等领域。传统的方法合成碳化钼需要复杂的工艺,尺寸和形貌不可控,获得无规则的碳化钼粉体,需要负载在各种载体上或者压制成型才能应用于催化反应。Due to the abundance of hydrogen energy resources, wide sources, high combustion calorific value of hydrogen, clean and pollution-free, it has attracted more and more attention from scientists from all over the world. Hydrogen production by electrolysis of water is currently the most mature, easy-to-industrialize, and environmentally friendly method. The traditional hydrogen production by electrolyzing water is to load the electrolytic water catalyst powder on the conductive electrode through the binder to electrolyze water to produce hydrogen. The problem with this mode is that the supported catalyst is easy to fall off, and the binder will also reduce the activity of the electrocatalyst, especially in the case of high loading. Molybdenum carbide is a highly efficient catalyst widely used in electrolysis of water to produce hydrogen and hydrodesulfurization and other fields. The traditional method of synthesizing molybdenum carbide requires a complex process, the size and shape of which are uncontrollable, and irregular molybdenum carbide powders are obtained, which need to be loaded on various carriers or pressed to form before they can be used in catalytic reactions.
发明内容Contents of the invention
为了克服现有技术的上述缺点与不足,本发明的目的在于提供一种碳化钼微米球的制备方法,原料便宜,工艺简单,获得高催化活性的多孔碳化钼微球,避免了粉体催化剂负载和后续成型等缺点,实现了悬浮电催化反应。In order to overcome the above-mentioned shortcomings and deficiencies of the prior art, the object of the present invention is to provide a preparation method of molybdenum carbide microspheres, the raw materials are cheap, the process is simple, porous molybdenum carbide microspheres with high catalytic activity are obtained, and powder catalyst loading is avoided. And subsequent molding and other shortcomings, to achieve the suspension electrocatalytic reaction.
本发明的目的通过以下技术方案实现:The object of the present invention is achieved through the following technical solutions:
一种碳化钼微米球的制备方法,包括以下步骤:A preparation method of molybdenum carbide microspheres, comprising the following steps:
(1)将强碱性阴离子交换树脂加入钼酸盐溶液中,常温下搅拌反应12~48小时,通过水洗,抽滤获得钼离子-树脂复合物,干燥后得到含钼元素的离子交换树脂微球;(1) Add the strong basic anion exchange resin into the molybdate solution, stir and react at room temperature for 12 to 48 hours, wash with water and filter with suction to obtain the molybdenum ion-resin complex, and obtain the ion exchange resin microparticles containing molybdenum after drying. ball;
(2)将步骤(1)得到的含钼元素的离子交换树脂微球置于到陶瓷坩埚中,在惰性气体保护下,于700~1000℃焙烧1~4小时,自然冷却至室温,得碳化钼微球。(2) Place the molybdenum-containing ion-exchange resin microspheres obtained in step (1) into a ceramic crucible, and under the protection of an inert gas, bake at 700-1000° C. for 1-4 hours, and cool naturally to room temperature to obtain carbonized Molybdenum microspheres.
步骤(1)所述的强碱性阴离子交换树脂与钼酸盐的质量比为1~10。The mass ratio of the strongly basic anion exchange resin to the molybdate in the step (1) is 1-10.
步骤(1)所述的强碱性阴离子交换树脂为201×4、201×7、202、213、D201、D202型阴离子交换树脂中的一种。The strongly basic anion exchange resin described in the step (1) is one of 201×4, 201×7, 202, 213, D201, and D202 type anion exchange resins.
步骤(1)所述钼酸盐溶液为钼酸铵、钼酸钾或钼酸钠。The molybdate solution in step (1) is ammonium molybdate, potassium molybdate or sodium molybdate.
步骤(2)于700~1000℃焙烧1~4小时,具体为:Step (2) roasting at 700-1000°C for 1-4 hours, specifically:
以1~10℃/分钟的升温速度升温至700~1000℃焙烧1~4小时。Raise the temperature to 700-1000° C. at a rate of 1-10° C./min and bake for 1-4 hours.
所述碳化钼微米球的应用,用于电解水产氢。The application of the molybdenum carbide microspheres is for electrolyzing water to produce hydrogen.
所述碳化钼微米球作为悬浮电解水产氢的催化剂,加入到电催化解水产氢装置的阴极室的电解液中。The molybdenum carbide microspheres are used as a catalyst for suspending electrolysis of water to generate hydrogen, and are added to the electrolyte in the cathode chamber of the electrocatalytic water splitting device for hydrogen generation.
所述悬浮电催化解水产氢装置包括电解池,所述电解池中设有将电解池分隔为阳极室和阴极室的质子交换膜;所述质子交换膜倾斜设置,下端贴于电解池的底部,上端贴于电解池的顶部;所述阳极室位于质子交换膜的上方,阳极室的侧壁设有阳极,阳极室的顶部设有氧气出口;所述阴极室位于质子交换膜的下方,阴极室的底部设有阴极,阴极室的顶部设有氢气出口。The suspended electrocatalytic water splitting hydrogen production device includes an electrolytic cell, the electrolytic cell is provided with a proton exchange membrane separating the electrolytic cell into an anode chamber and a cathode chamber; the proton exchange membrane is arranged obliquely, and the lower end is attached to the bottom of the electrolytic cell , the upper end is attached to the top of the electrolytic cell; the anode chamber is positioned above the proton exchange membrane, the side wall of the anode chamber is provided with an anode, and the top of the anode chamber is provided with an oxygen outlet; the cathode chamber is positioned below the proton exchange membrane, and the cathode A cathode is provided at the bottom of the chamber, and a hydrogen outlet is provided at the top of the cathode chamber.
所述的碳化钼微米球的应用,所述阴极贴于电解池的底部上。In the application of the molybdenum carbide microspheres, the cathode is pasted on the bottom of the electrolytic cell.
与现有技术相比,本发明具有以下优点和有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:
(1)本发明的碳化钼微米球的制备方法,制备条件要求低,原料廉价易得,既解决环境污染问题,又获得了高催化活性的电催化剂。(1) The preparation method of the molybdenum carbide microspheres of the present invention requires low preparation conditions, and the raw materials are cheap and easy to obtain, which not only solves the problem of environmental pollution, but also obtains an electrocatalyst with high catalytic activity.
(2)本发明的碳化钼微米球的制备方法制备得到的碳化钼微米球,具有催化低过电位和稳定性好的电化学活性。(2) The molybdenum carbide microspheres prepared by the method for preparing molybdenum carbide microspheres of the present invention have electrochemical activity with low catalytic overpotential and good stability.
(3)将本发明制备的碳化钼微米球应用到电解水产氢中,可悬浮电催化解水反应,解决了电催化剂无粘结剂负载和再利用的问题,实现电解水析氢反应过程中高电流密度,高稳定性和高催化效率的技术目标。(3) Apply the molybdenum carbide microspheres prepared by the present invention to electrolysis of water for hydrogen production, which can suspend electrocatalyzed water splitting reaction, solve the problem of electrocatalyst without binder loading and reuse, and realize high current in the process of electrolysis of water for hydrogen evolution reaction Technical goals of density, high stability and high catalytic efficiency.
附图说明Description of drawings
图1为本发明的实施例1的经过离子交换反应后900摄氏度焙烧得到的碳化钼的XRD图谱。Fig. 1 is the XRD spectrum of the molybdenum carbide obtained by roasting at 900 degrees Celsius after the ion exchange reaction in Example 1 of the present invention.
图2为本发明的实施例1的900摄氏度焙烧所得碳化钼微米球扫描电镜照片。2 is a scanning electron micrograph of molybdenum carbide microspheres obtained by roasting at 900 degrees Celsius in Example 1 of the present invention.
图3为本发明的实施例1的900摄氏度焙烧所得碳化钼微米球的局部放大扫描电镜照片。Fig. 3 is a partially enlarged scanning electron micrograph of molybdenum carbide microspheres obtained by roasting at 900 degrees Celsius in Example 1 of the present invention.
图4为本发明的实施例1的悬浮电催化解水装置的示意图。Fig. 4 is a schematic diagram of the suspended electrocatalytic water splitting device in Example 1 of the present invention.
图5为本发明的实施例1悬浮电解水产氢的原理图。Fig. 5 is a schematic diagram of hydrogen production by suspension electrolysis of water according to Embodiment 1 of the present invention.
图6为本发明的实施例1的碳化钼微米球为催化剂的极化曲线图。Fig. 6 is a polarization curve diagram of molybdenum carbide microspheres as a catalyst in Example 1 of the present invention.
图7为本发明的实施例1的碳化钼微米球的悬浮电催化产氢反应的时间电流曲线图。Fig. 7 is a time-current graph of the electrocatalytic hydrogen production reaction of molybdenum carbide microspheres in Example 1 of the present invention.
图8为本发明的实施例2的1000摄氏度合成的碳化钼的X射线衍射图。Fig. 8 is an X-ray diffraction diagram of molybdenum carbide synthesized at 1000 degrees Celsius in Example 2 of the present invention.
图9为本发明的实施例2的1000摄氏度合成的碳化钼的扫描电镜图。Fig. 9 is a scanning electron micrograph of molybdenum carbide synthesized at 1000 degrees Celsius in Example 2 of the present invention.
图10为本发明的实施例2的1000摄氏度合成的碳化钼的极化曲线结果。Fig. 10 is the polarization curve result of molybdenum carbide synthesized at 1000 degrees Celsius in Example 2 of the present invention.
图11为本发明的实施例4的800摄氏度合成的得碳化钼和二氧化钼混合物形貌图。Fig. 11 is a morphological diagram of the mixture of molybdenum carbide and molybdenum dioxide synthesized at 800 degrees Celsius in Example 4 of the present invention.
图12为本发明的实施例4的800摄氏度合成的碳化钼和二氧化钼混合物X射线粉末衍射结果。Fig. 12 is the X-ray powder diffraction result of the mixture of molybdenum carbide and molybdenum dioxide synthesized at 800 degrees Celsius in Example 4 of the present invention.
图13为本发明的实施例3的700摄氏度合成的二氧化钼通过氮气吸脱附测试获得的比表面积。Fig. 13 is the specific surface area of molybdenum dioxide synthesized at 700 degrees Celsius in Example 3 of the present invention obtained through nitrogen adsorption and desorption tests.
图14为本发明的实施例5的900摄氏度合成的碳化钼粉体的拉曼光谱图。Fig. 14 is a Raman spectrum of molybdenum carbide powder synthesized at 900 degrees Celsius in Example 5 of the present invention.
图15为本发明的实施例5的900摄氏度合成的碳化钼粉体X射线光电子能谱图C峰。Fig. 15 is peak C of the X-ray photoelectron spectrum of molybdenum carbide powder synthesized at 900 degrees Celsius in Example 5 of the present invention.
图16为本发明的实施例5的900摄氏度合成的碳化钼粉体X射线光电子能谱图Mo3d峰。Figure 16 is the Mo3d peak in the X-ray photoelectron spectrum of the molybdenum carbide powder synthesized at 900 degrees Celsius in Example 5 of the present invention.
图17为本发明的实施例5的900摄氏度合成的碳化钼的时间电流曲线。Fig. 17 is the time-current curve of molybdenum carbide synthesized at 900 degrees Celsius in Example 5 of the present invention.
图18为本发明的实施例5的900摄氏度合成的碳化钼阻抗结果。Fig. 18 is the impedance result of molybdenum carbide synthesized at 900 degrees Celsius in Example 5 of the present invention.
具体实施方式detailed description
下面结合实施例,对本发明作进一步地详细说明,但本发明的实施方式不限于此。The present invention will be described in further detail below in conjunction with the examples, but the embodiments of the present invention are not limited thereto.
实施例1Example 1
称取5克D201型阴离子交换树脂加入到盛有20毫升,0.5摩尔每升的钼酸钠溶液,加入搅拌子常温下搅拌反应24小时。将溶液缓慢加入到抽滤瓶中抽滤,将所得固体100℃干燥24小时,获得吸附钼离子的离子交换树脂。将所得粉体加入到陶瓷坩埚中,置于气氛管式炉中,氮气气体保护下,管式炉中5℃每分钟升温速度升温至900℃高温焙烧2小时,自然冷却至室温,获得碳化钼微米球。通过X射线电子衍射表征微球为碳化钼组分,如图1;通过扫描电子显微镜观察到微米球状形貌,直径为200-500微米(如图2),微球表面有颗粒状组成,具有多孔结构(如图3)。Weigh 5 grams of D201 type anion exchange resin and add to 20 milliliters, 0.5 mole per liter of sodium molybdate solution, add a stirring bar and stir for 24 hours at room temperature. Slowly add the solution into a suction filter bottle for suction filtration, and dry the obtained solid at 100° C. for 24 hours to obtain an ion exchange resin adsorbing molybdenum ions. Put the obtained powder into a ceramic crucible, place it in an atmosphere tube furnace, and under the protection of nitrogen gas, heat up to 900 °C at a heating rate of 5 °C per minute in the tube type furnace for 2 hours, and cool naturally to room temperature to obtain molybdenum carbide Microspheres. The microspheres are characterized by X-ray electron diffraction as a molybdenum carbide component, as shown in Figure 1; the microsphere shape is observed by a scanning electron microscope, with a diameter of 200-500 microns (as Figure 2), and the surface of the microspheres has a granular composition, with Porous structure (Figure 3).
如图4所示,本实施例的电催化解水装置包括电解池,为圆柱体结构,体壁为玻璃材质,底部密封,顶部为塑料套帽,设有氧气出口1和氢气出口2;所述电解池中设有将电解池分隔为阳极室3和阴极室4的质子交换膜5;所述质子交换膜倾斜设置,与水平面的夹角为45度,下端贴于电解池的底部,上端贴于塑料套帽上;所述阳极室3位于质子交换膜5的上方,阳极6采用方片型碳布,设于阳极室3的侧壁,氢气出口1设于阳极室3的顶部;所述阴极室4位于质子交换膜5的下方,阴极7采用圆片型钛片,形状与电解池的底部相同,贴于电解池的底部,氢气出口2设于阴极室4的顶部。电催化剂碳化钼微球8分散在电解液中。As shown in Figure 4, the electrocatalytic water splitting device of this embodiment includes an electrolytic cell, which is a cylindrical structure, the body wall is made of glass, the bottom is sealed, the top is a plastic sleeve cap, and an oxygen outlet 1 and a hydrogen outlet 2 are provided; The electrolytic cell is provided with a proton exchange membrane 5 that separates the electrolytic cell into an anode chamber 3 and a cathode chamber 4; Pasted on the plastic cover cap; the anode chamber 3 is located above the proton exchange membrane 5, the anode 6 adopts square sheet carbon cloth, is arranged on the side wall of the anode chamber 3, and the hydrogen outlet 1 is located on the top of the anode chamber 3; The cathode chamber 4 is located below the proton exchange membrane 5, and the cathode 7 adopts a disc-type titanium sheet, which is identical in shape to the bottom of the electrolytic cell and attached to the bottom of the electrolytic cell. The hydrogen outlet 2 is located on the top of the cathode chamber 4. The electrocatalyst molybdenum carbide microspheres 8 are dispersed in the electrolyte solution.
以5克上述的碳化钼微球为电催化剂加入上述电催化解水装置的阴极室中,以浓度为0.5摩尔每升的硫酸水溶液为电解液,直径5厘米的圆形钛片为阴极,直径为5厘米圆形碳布为阳极,中间为酸性质子交换膜,电解池为玻璃材质。Add 5 grams of the above-mentioned molybdenum carbide microspheres as the electrocatalyst into the cathode chamber of the above-mentioned electrocatalytic water splitting device, use the sulfuric acid aqueous solution with a concentration of 0.5 moles per liter as the electrolyte, and a circular titanium sheet with a diameter of 5 cm as the cathode. The 5 cm circular carbon cloth is the anode, the middle is the acidic proton exchange membrane, and the electrolytic cell is made of glass.
如图5所示,本实施例的碳化钼微球悬浮电催化解水的原理如下:As shown in Figure 5, the principle of molybdenum carbide microsphere suspension electrocatalytic water splitting in this embodiment is as follows:
强碱性阴离子交换树脂本身含有的强碱性官能团,能在水中离解出氢氧根,钼酸根阴离子与氢氧根阴离子发生交换,与树脂中正电基团吸附结合,从而产生阴离子交换作用。将离子交换反应后得到的树脂在高温下焙烧碳化,就能得到保持球形结构的碳化钼微米球。再将这种碳化钼微米球转移到以0.5摩尔每升的硫酸为电解液的悬浮式电解水析氢装置,其中产氢工作电极处于电解池底部。通过施加适当大小的电压,碳化钼微米球由于吸附有催化反应所产生的氢气从而有向上的浮力,当重力Fg与浮力Fb大小相等时,便会产生悬浮;同时,碳化钼微球彼此之间碰撞,使氢气泡脱落而沉到底部电极。碳化钼微球与电极之间没有固定负载关系,可以实现简单的电催化剂的更换。碳化钼微米球在电解液中漂浮与沉降两个过程不断转换,实现高效地悬浮电解水产氢。Strongly basic anion exchange resin itself contains strong basic functional groups, which can dissociate hydroxides in water, molybdate anions exchange with hydroxide anions, and adsorb and combine with positively charged groups in the resin to produce anion exchange. The resin obtained after the ion exchange reaction is calcined and carbonized at a high temperature to obtain molybdenum carbide microspheres maintaining a spherical structure. Then transfer the molybdenum carbide microspheres to a suspension type electrolysis water hydrogen evolution device using 0.5 mol per liter of sulfuric acid as the electrolyte, wherein the hydrogen production working electrode is at the bottom of the electrolytic cell. By applying an appropriate voltage, the molybdenum carbide microspheres have an upward buoyancy due to the adsorption of hydrogen generated by the catalytic reaction. When the gravity Fg and the buoyancy Fb are equal in magnitude, they will be suspended; at the same time, the molybdenum carbide microspheres are in contact with each other Collisions between the electrodes make the hydrogen bubbles fall off and sink to the bottom electrode. There is no fixed load relationship between the molybdenum carbide microspheres and the electrode, which can realize simple electrocatalyst replacement. The two processes of molybdenum carbide microspheres floating and settling in the electrolyte are continuously converted to achieve efficient hydrogen production by suspending electrolyzed water.
采用线性伏安扫描测试其极化曲线如图6,具有低的电解水产氢过电势,其值为75毫伏;采用时间-电流方法测试其催化电流密度随着反应时间的变化,催化反应10小时未见催化电流密度降低,展现了良好的循环稳定性(图7)。Using linear voltammetry scanning to test its polarization curve as shown in Figure 6, it has a low electrolyzed water hydrogen production overpotential, and its value is 75 millivolts; using time-current method to test its catalytic current density with the change of reaction time, catalytic reaction 10 There is no decrease in the catalytic current density after 4 hours, showing good cycle stability (Figure 7).
实施例2Example 2
称取2g的201×4型阴离子交换树脂加入到盛有40毫升,2摩尔每升的钼酸钠溶液,加入搅拌子常温下搅拌反应12小时。将所得溶液抽滤,将所得固体100℃干燥48小时。所得固体在氩气气体保护下,以5℃/min升温速度升温至1000℃高温焙烧2小时,自然冷却至室温,得碳化钼微米球,X射线衍射结果如图8;通过研磨粉碎获得碳化钼形貌如图9。Weigh 2g of 201×4 type anion exchange resin and add it into 40 ml of sodium molybdate solution with 2 moles per liter, add a stirring bar and stir for 12 hours at normal temperature. The obtained solution was filtered with suction, and the obtained solid was dried at 100° C. for 48 hours. Under the protection of argon gas, the obtained solid was heated up to 1000°C at a heating rate of 5°C/min and roasted at a high temperature for 2 hours, and then cooled naturally to room temperature to obtain molybdenum carbide microspheres. The X-ray diffraction results are shown in Figure 8; molybdenum carbide was obtained by grinding and pulverizing The morphology is shown in Figure 9.
以本实施例制备的碳化钼为电催化剂,其极化曲线结果图10,产氢过电势为0.22伏。Using the molybdenum carbide prepared in this example as the electrocatalyst, the result of its polarization curve is shown in Figure 10, and the hydrogen production overpotential is 0.22 volts.
实施例3Example 3
制备步骤同实施例1,不同之处是:阴离子交换树脂采用D202型,管式炉中5℃每分钟升温速度升温至800℃高温焙烧2小时。获得的碳化钼微球形貌如图11,X射线粉末衍射结果如图12。通过氮气吸脱附测试获得其比表面积为42.8平方米每克(图13),说明碳化钼微球为多孔结构。The preparation steps are the same as in Example 1, except that the anion exchange resin is D202 type, and the temperature is raised to 800° C. for 2 hours in a tube furnace at a heating rate of 5° C. per minute. The morphology of the obtained molybdenum carbide microspheres is shown in Figure 11, and the X-ray powder diffraction results are shown in Figure 12. The specific surface area obtained by the nitrogen adsorption and desorption test is 42.8 square meters per gram (Figure 13), indicating that the molybdenum carbide microspheres are porous structures.
实施例4Example 4
制备步骤同实施例1,不同之处是:煅烧温度改为900℃。通过拉曼表征证实电催化剂由碳化钼和结晶碳两种组分,如图14。The preparation steps are the same as in Example 1, except that the calcination temperature is changed to 900°C. It was confirmed by Raman characterization that the electrocatalyst consists of molybdenum carbide and crystalline carbon, as shown in Figure 14.
本实施例制备的粉体,通过光电子能谱表征,如图15和图16,可以看到电催化剂是由四价钼元素和碳元素组成,证实成功合成了碳化钼。The powder prepared in this example is characterized by photoelectron spectroscopy, as shown in Figure 15 and Figure 16, it can be seen that the electrocatalyst is composed of tetravalent molybdenum and carbon, which confirms the successful synthesis of molybdenum carbide.
以本实施例制备的碳化钼为电催化剂,通过时间电流曲线(如图17)测试表征碳化钼具有良好的产氢稳定性。The molybdenum carbide prepared in this example was used as the electrocatalyst, and the time-current curve (as shown in Figure 17) was used to test and show that the molybdenum carbide had good hydrogen production stability.
以本实施例制备的碳化钼为电催化剂,制备所得碳化钼电化学阻抗结果如图18,结果表明碳化钼具有小的阻抗值,随着电压增加,阻抗逐渐变小。Using the molybdenum carbide prepared in this example as the electrocatalyst, the electrochemical impedance results of the prepared molybdenum carbide are shown in Figure 18. The results show that the molybdenum carbide has a small impedance value, and the impedance gradually decreases as the voltage increases.
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受所述实施例的限制,如本发明的强碱性阴离子交换树脂还可为201×7、202、213型或其他阴离子交换树脂;钼酸盐还可以钼酸钾或钼酸铵其他钼酸盐;其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。Above-mentioned embodiment is preferred embodiment of the present invention, but embodiment of the present invention is not limited by described embodiment, also can be 201 * 7, 202, 213 type as strong basic anion exchange resin of the present invention or Other anion exchange resins; Molybdate can also be other molybdates of potassium molybdate or ammonium molybdate; Any other changes, modifications, substitutions, combinations, and simplifications that do not deviate from the spirit and principles of the present invention should be Equivalent replacement methods are all included in the protection scope of the present invention.
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