WO2021022988A1 - Co3o4/cumoo4 compound, preparation method therefor, and application thereof - Google Patents

Co3o4/cumoo4 compound, preparation method therefor, and application thereof Download PDF

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WO2021022988A1
WO2021022988A1 PCT/CN2020/102362 CN2020102362W WO2021022988A1 WO 2021022988 A1 WO2021022988 A1 WO 2021022988A1 CN 2020102362 W CN2020102362 W CN 2020102362W WO 2021022988 A1 WO2021022988 A1 WO 2021022988A1
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cumoo
water
composite according
urea
precipitate
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李�浩
卢东升
廖锦云
冯裕发
王慧泽
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惠州学院
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/885Molybdenum and copper
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/068Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents the hydrogen being generated from the water as a result of a cyclus of reactions, not covered by groups C01B3/063 or C01B3/105
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041Composition of the catalyst
    • C01B2203/1047Group VIII metal catalysts
    • C01B2203/1052Nickel or cobalt catalysts
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041Composition of the catalyst
    • C01B2203/1076Copper or zinc-based catalysts
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • the present invention relates to the technical field of catalyst synthesis, in particular to a Co 3 O 4 /CuMoO 4 composite, a preparation method thereof and its application in hydrogen production.
  • non-precious metal catalytic materials mainly includes sulfides, phosphides and oxides. Sulfides and phosphides, although a certain catalytic activity, there are security risks, such as Ashok K.Ganguli et al (Ashok K.Ganguli et al.Comparative Study of TiO 2 / CuS Core / Shell and Composite Nanostructures for Efficient in the manufacturing process Visible Light Photocatalysis, ACS Sustainable Chem. Eng.
  • Ni 2-x Co x P catalyst was prepared by solid-phase reaction.
  • nanowires are the most ideal morphology, such as Z.Ren (Z.Ren et al.Cu nanowires shelled with NiFe layered double hydroxide nanosheets as bifunctional electrocatalysts for overall water splitting, Energy Environ.Sci., 2017, 10, 1820-1827) reported core-shell nanowires, but the The method is based on copper foil, the use of the carrier makes the preparation process complicated; more interesting sea urchin-shaped has also been reported, such as J. Zhang et al. (J. Zhang et al. Morphological evolution of Fe doped sea urchin-shaped ZnO nanoparticles with Enhanced photocatalytic activity, J. Alloys Compound. 2017, 696, 639-647) Synthetic sea urchin-like Fe-doped ZnO catalyst, the use of surfactants and organic solvents in the preparation process are more expensive than pure aqueous solutions.
  • the present invention provides a Co 3 O 4 /CuMoO 4 composite and a preparation method thereof.
  • the method of the present invention is specifically adjusted by a two-step hydrothermal method.
  • the added amount of copper molybdate successfully prepared a sea urchin-like catalyst assembled with nanowires.
  • This method provides a simple and controllable technology for the synthesis of sea urchin-like materials, and at the same time, it is important to promote the low-cost mass production of materials. step.
  • the technical solution adopted by the present invention is:
  • the invention provides a Co 3 O 4 /CuMoO 4 composite, a sea urchin-like Co 3 O 4 /CuMoO 4 composite composed of nanorods.
  • the present invention also provides a method for preparing the aforementioned Co 3 O 4 /CuMoO 4 composite, which includes the following steps:
  • the amount of CuCl 2 and urea fed is 1:10.
  • the synthesis conditions of the cobalt precursor in step (2) are 95-110°C for 8-24 hours.
  • the temperature of the vacuum oven in step (3) is 40-60°C, and the drying time is 3-6h.
  • the synthesis condition of Co 3 O 4 /CuMoO 4 is 150-180° C. for 6-10 hours.
  • the muffle furnace temperature is 450-600°C for calcination for 2 to 4 hours, and the muffle furnace temperature rise rate is 2°C/min.
  • the stirring time in step (7) is 30 minutes.
  • the invention also discloses the application of the Co 3 O 4 /CuMoO 4 composite prepared by the above preparation method as a catalyst in the hydrolysis of ammonia borane.
  • the Co 3 O 4 /CuMoO 4 composite provided by the present invention successfully prepares a sea urchin-like catalyst assembled with nanowires by a two-step hydrothermal method by adjusting the doping amount of copper molybdate.
  • the method has a simple synthesis process.
  • the raw materials are cheap and easy to obtain, and the morphology is unique and controllable, and it shows excellent catalytic activity in the field of catalyzing the hydrolysis of ammonia borane.
  • the unique sea urchin-like catalyst prepared by the present invention has a novel method and only regulates the morphology by adjusting the doping amount of CuMoO 4 ;
  • the synthesized Co 3 O 4 /CuMoO 4 composite has the characteristics of sea urchin-like microstructure and is expected to be a highly active catalyst, such as showing superior catalytic activity in catalyzing the hydrolysis of ammonia borane to produce hydrogen.
  • Figure 1 is an SEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • Figure 2 is a TEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • Example 3 is a BET test curve of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • FIG. 4 is an XRD test curve of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • Example 5 is a test curve of the catalytic hydrogen production of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • the invention provides a method for preparing a Co3O4/CuMoO4 composite, which specifically includes the following methods:
  • Figure 1 is an SEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention. It can be seen from the scan that the Co 3 O 4 /CuMoO 4 synthesized by hydrothermal method has a sea urchin-like appearance.
  • Figure 2 is a TEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • the projection image can further confirm the sea urchin-like catalyst.
  • FIG. 3 is a nitrogen adsorption and desorption isotherm curve of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
  • Fig. 4 is an XRD test of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention. Marked in the figure are the characteristic peaks of CuMoO 4 and Co 3 O 4 corresponding crystal planes.
  • Fig. 5 is a performance test of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention as a catalyst to catalyze the hydrolysis of ammonia borane to produce hydrogen.
  • the amount of NH 3 BH 3 is 3 mmol, NaOH 20 mmol, and the catalyst 10 mg. It is measured that Co 3 O 4 /CuMoO 4 is used as a catalyst to produce 121.5 mL of hydrogen per minute at 25°C.

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Abstract

Disclosed in the present invention is a Co3O4/CuMoO4 compound. The compound is an urchin-like Co3O4/CuMoO4 compound formed by nanorods. Also disclosed in the present invention a preparation method for the compound, comprising: (1) weighing cobalt nitrate, hexamethylene tetramine, and trisodium citrate and dissolving same in deionized water, and continuously stirring until complete dissolution; (2) transferring the solution to a reaction kettle; (3) performing suction filtration and water washing, and drying in a vacuum oven; (4) weighing a precipitate obtained in step (3) and dispersing same in water; (5) adding CuCl2, stirring until complete dissolution, and then adding H2MoO4; (6) dissolving urea in water; (7) dropwise adding a urea solution to the solution and stirring; (8) transferring to the reaction kettle, cooling to room temperature after reaction is completed, collecting a precipitate, and vacuum-drying after washing several times; and (9) calcining the collected sample in a muffle furnace to obtain a product. According to the method, an urchin-like catalyst formed by assembling nanowires is successfully prepared by adjusting the doping amount of copper molybdate. The method is simple in synthetic process and cheap and easy-to-access in raw material, and the catalyst is unique and controllable in appearance and shows excellent catalytic activity in the field of catalysis of ammonia borane hydrolysis.

Description

一种Co 3O 4/CuMoO 4复合物及其制备方法和应用 A Co 3O 4/CuMoO 4 Complex and its preparation method and application 技术领域Technical field
本发明涉及催化剂合成技术领域,尤其涉及一种Co 3O 4/CuMoO 4复合物及其制备方法和其在制氢上的应用。 The present invention relates to the technical field of catalyst synthesis, in particular to a Co 3 O 4 /CuMoO 4 composite, a preparation method thereof and its application in hydrogen production.
背景技术Background technique
应对当下能源危机及生态环保,一系列研究应运而生,比如光电催化析氢,二氧化碳电还原,氧还原,化学氢化物析氢等。发展均具有较广阔的前景。而在这些研究中,往往需要催化剂以达到更理想的状况,为此催化剂的设计、合成显得尤为重要。在各个领域,贵重金属均表现出优异的活性,但因其较高成本、地壳含量较低等客观因素使得商业化得不偿失,从而限制其广泛的使用,所以大力发展过渡金属中非贵金属催化剂成为主流。In response to the current energy crisis and ecological environmental protection, a series of studies have emerged, such as photoelectric catalytic hydrogen evolution, carbon dioxide electroreduction, oxygen reduction, and hydrogen evolution from chemical hydrides. Development has broad prospects. In these studies, catalysts are often needed to achieve a more ideal situation. For this reason, the design and synthesis of catalysts are particularly important. In various fields, precious metals show excellent activity, but due to objective factors such as higher cost and lower crust content, commercialization is not worth the loss, which limits its wide use. Therefore, the development of non-precious metal catalysts in transition metals has become the mainstream .
目前为止,非贵金属催化材料的研究主要包括硫化物、磷化物及氧化物。硫化物与磷化物虽具备一定催化活性,但在制备过程中存在安全隐患,如Ashok K.Ganguli等人(Ashok K.Ganguli et al.Comparative Study of TiO 2/CuS Core/Shell and Composite Nanostructures for Efficient Visible Light Photocatalysis,ACS Sustainable Chem.Eng.2016,4,1487-1499)水热合成制备硫化物,但硫化钠或者硫脲作为硫源,反应中伴随硫的有毒气体产生,不能绿色生产;如Y.Chen等人(Y.Chen et al.Ternary Ni-Co-P nanoparticles and their hybrids with graphene as noble-metal-free catalysts to boost the hydrolytic dehydrogenation of ammonia-borane,Energy Environ.Sci.,2017,10,1770-1776)用固相反应制备Ni 2-xCo xP催化剂,虽取得了较好的催化活性,但在制备过程中,将次磷酸钠与氢氧化物前驱体研磨后直接加热反应,而次磷酸钠加热超过200℃时则迅速分解,放出可自燃的有毒的磷化氢,遇强热时会爆炸,制备工艺存在危险;故氧化物催化剂的研究更为安全可靠。氧化物各种形貌均有报道,但从催化角度而言,拥有好的分散性以及小尺寸的特定形貌更有助于催化的进行,无疑纳米线是最理想形貌,如Z.Ren等人(Z.Ren et al.Cu nanowires shelled with NiFe layered double hydroxide nanosheets as bifunctional electrocatalysts for overall water splitting,Energy Environ.Sci.,2017,10,1820-1827)报道的核壳型纳米线,但该方法是以铜箔作为基底,载体的使用使得制备工艺复杂;更为有趣的海胆状也有报道,如J.Zhang等人(J.Zhang et al.Morphological evolution of Fe doped sea urchin-shaped ZnO nanoparticles with enhanced photocatalytic activity,J.Alloys Compound.2017,696,639-647)合成海胆状Fe掺杂的 ZnO催化剂,其制备过程中表面活性剂的使用及有机溶剂的使用,相比单纯水溶液成本更高。 So far, the research on non-precious metal catalytic materials mainly includes sulfides, phosphides and oxides. Sulfides and phosphides, although a certain catalytic activity, there are security risks, such as Ashok K.Ganguli et al (Ashok K.Ganguli et al.Comparative Study of TiO 2 / CuS Core / Shell and Composite Nanostructures for Efficient in the manufacturing process Visible Light Photocatalysis, ACS Sustainable Chem. Eng. 2016, 4, 1487-1499) Hydrothermal synthesis to prepare sulfide, but sodium sulfide or thiourea is used as a sulfur source, the reaction is accompanied by the production of toxic gases of sulfur, which cannot be green production; .Chen et al.(Y.Chen et al.Ternary Ni-Co-P nanoparticles and their hybrids with graphene as noble-metal-free catalysts to boost the hydrolytic dehydrogenation of ammonia-borane, Energy Environ.Sci., 2017, 10, 1770-1776) Ni 2-x Co x P catalyst was prepared by solid-phase reaction. Although good catalytic activity was achieved, in the preparation process, the sodium hypophosphite and hydroxide precursor were ground and directly heated to react. Sodium hypophosphite decomposes rapidly when heated above 200°C and emits spontaneously combustible toxic phosphine, which will explode when exposed to strong heat, and the preparation process is dangerous; therefore, the research on oxide catalysts is safer and more reliable. Various morphologies of oxides have been reported, but from the perspective of catalysis, a specific morphology with good dispersion and small size is more helpful to the progress of catalysis. No doubt nanowires are the most ideal morphology, such as Z.Ren (Z.Ren et al.Cu nanowires shelled with NiFe layered double hydroxide nanosheets as bifunctional electrocatalysts for overall water splitting, Energy Environ.Sci., 2017, 10, 1820-1827) reported core-shell nanowires, but the The method is based on copper foil, the use of the carrier makes the preparation process complicated; more interesting sea urchin-shaped has also been reported, such as J. Zhang et al. (J. Zhang et al. Morphological evolution of Fe doped sea urchin-shaped ZnO nanoparticles with Enhanced photocatalytic activity, J. Alloys Compound. 2017, 696, 639-647) Synthetic sea urchin-like Fe-doped ZnO catalyst, the use of surfactants and organic solvents in the preparation process are more expensive than pure aqueous solutions.
发明内容Summary of the invention
针对上述制备过程中存在的制备成本高、操作繁琐的关键问题,本发明提供一种Co 3O 4/CuMoO 4复合物及其制备方法,本发明的方法具体是由两步水热法通过调节钼酸铜的加入量成功制备具有纳米线组装而成的海胆状催化剂,该方法为合成海胆状材料提供一种简易可控的技术,同时也为推动材料的低成本规模化生产迈出了重要一步。 In view of the key problems of high preparation cost and cumbersome operation in the above preparation process, the present invention provides a Co 3 O 4 /CuMoO 4 composite and a preparation method thereof. The method of the present invention is specifically adjusted by a two-step hydrothermal method. The added amount of copper molybdate successfully prepared a sea urchin-like catalyst assembled with nanowires. This method provides a simple and controllable technology for the synthesis of sea urchin-like materials, and at the same time, it is important to promote the low-cost mass production of materials. step.
为解决以上技术问题,本发明采用的技术方案是:To solve the above technical problems, the technical solution adopted by the present invention is:
本发明提供了一种Co 3O 4/CuMoO 4复合物,由纳米棒组成的海胆状Co 3O 4/CuMoO 4复合物。 The invention provides a Co 3 O 4 /CuMoO 4 composite, a sea urchin-like Co 3 O 4 /CuMoO 4 composite composed of nanorods.
本发明还提供了上述Co 3O 4/CuMoO 4复合物的制备方法,包括以下步骤: The present invention also provides a method for preparing the aforementioned Co 3 O 4 /CuMoO 4 composite, which includes the following steps:
(1)、取硝酸钴、六次甲基四胺、柠檬酸三钠溶于去离子水中,持续搅拌直至溶解,其中,硝酸钴、六次甲基四胺、柠檬酸三钠三者投料的物质的量比为6∶3∶2;(1). Dissolve cobalt nitrate, hexamethylenetetramine, and trisodium citrate in deionized water and continue stirring until dissolved. Among them, cobalt nitrate, hexamethylenetetramine, and trisodium citrate are charged The quantity ratio of the substances is 6:3:2;
(2)、将上述溶液转移至反应釜,在一定温度下反应一段时间;(2) Transfer the above solution to the reaction kettle and react for a period of time at a certain temperature;
(3)、然后,抽滤水洗,真空烘箱干燥;(3) Then, it is filtered and washed with water and dried in a vacuum oven;
(4)、取步骤(3)中的沉淀物分散于水中;(4) Disperse the precipitate in step (3) in water;
(5)、加CuCl 2搅拌溶解,再对应加入相同物质的量的H 2MoO 4(5) Add CuCl 2 and stir to dissolve, and then add H 2 MoO 4 corresponding to the same substance;
(6)、将尿素溶于水中;(6) Dissolve urea in water;
(7)、将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌;(7) Add the urea solution dropwise to the above solution through the sealing funnel, and stir;
(8)、转移至反应釜,在一定温度下反应一段时间,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;(8) Transfer to the reactor, react for a period of time at a certain temperature, cool to room temperature after the reaction, collect the precipitate, wash it several times and then vacuum dry;
(9)、将收集样品在马弗炉中煅烧一段时间后,得到最终催化剂Co 3O 4/CuMoO 4(9) After calcining the collected samples in a muffle furnace for a period of time, the final catalyst Co 3 O 4 /CuMoO 4 is obtained .
进一步的,CuCl 2与尿素投料的物质的量为1∶10。 Further, the amount of CuCl 2 and urea fed is 1:10.
优选的,步骤(2)中钴前驱体的合成条件为95~110℃反应8~24h。Preferably, the synthesis conditions of the cobalt precursor in step (2) are 95-110°C for 8-24 hours.
优选的,步骤(3)中真空烘箱的温度为40~60℃,干燥时间为3~6h。Preferably, the temperature of the vacuum oven in step (3) is 40-60°C, and the drying time is 3-6h.
优选的,步骤(8)中,Co 3O 4/CuMoO 4的合成条件为150~180℃反应6~10h。 Preferably, in step (8), the synthesis condition of Co 3 O 4 /CuMoO 4 is 150-180° C. for 6-10 hours.
优选的,步骤(9)中,马弗炉温度为450~600℃煅烧2~4h,马弗炉升温速率为2℃/min。Preferably, in step (9), the muffle furnace temperature is 450-600°C for calcination for 2 to 4 hours, and the muffle furnace temperature rise rate is 2°C/min.
优选的,步骤(7)中的搅拌时间为30min。Preferably, the stirring time in step (7) is 30 minutes.
本发明还公开了上述制备方法所制得的Co 3O 4/CuMoO 4复合物作为催化剂在催化氨硼烷水解中的应用。 The invention also discloses the application of the Co 3 O 4 /CuMoO 4 composite prepared by the above preparation method as a catalyst in the hydrolysis of ammonia borane.
本发明提供的一种Co 3O 4/CuMoO 4复合物,由两步水热法通过调节钼酸铜的掺杂量成功制备具有纳米线组装而成的海胆状催化剂,该方法合成工艺简易,原料价廉易得,且形貌独特可控,并且在催化氨硼烷水解领域表现出卓越的催化活性。 The Co 3 O 4 /CuMoO 4 composite provided by the present invention successfully prepares a sea urchin-like catalyst assembled with nanowires by a two-step hydrothermal method by adjusting the doping amount of copper molybdate. The method has a simple synthesis process. The raw materials are cheap and easy to obtain, and the morphology is unique and controllable, and it shows excellent catalytic activity in the field of catalyzing the hydrolysis of ammonia borane.
综上所述,运用本发明的技术方案,具有如下有益效果:In summary, using the technical solution of the present invention has the following beneficial effects:
1.工艺简单,原料价廉易得;1. The process is simple, and the raw materials are cheap and easy to obtain;
2.本发明制备的独特海胆状催化剂,方法新颖,仅仅通过调控CuMoO 4的掺杂量而调控形貌; 2. The unique sea urchin-like catalyst prepared by the present invention has a novel method and only regulates the morphology by adjusting the doping amount of CuMoO 4 ;
3.合成的Co 3O 4/CuMoO 4复合物因获得海胆状微观结构的特点,有望作为高活性催化剂,如在催化氨硼烷水解产氢方面表现出优越的催化活性。 3. The synthesized Co 3 O 4 /CuMoO 4 composite has the characteristics of sea urchin-like microstructure and is expected to be a highly active catalyst, such as showing superior catalytic activity in catalyzing the hydrolysis of ammonia borane to produce hydrogen.
附图说明Description of the drawings
图1为本发明实施例1制备的Co 3O 4/CuMoO 4的SEM图。 Figure 1 is an SEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
图2为本发明实施例1制备的Co 3O 4/CuMoO 4的TEM图。 Figure 2 is a TEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
图3为本发明实施例1制备的Co 3O 4/CuMoO 4的BET测试曲线。 3 is a BET test curve of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
图4为本发明实施例1制备的Co 3O 4/CuMoO 4的XRD测试曲线。 FIG. 4 is an XRD test curve of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
图5为本发明实施例1制备的Co 3O 4/CuMoO 4的催化产氢测试曲线。 5 is a test curve of the catalytic hydrogen production of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
具体实施方式detailed description
本发明提供了一种Co3O4/CuMoO4复合物的制备方法,具体包括以下方法:The invention provides a method for preparing a Co3O4/CuMoO4 composite, which specifically includes the following methods:
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ;
2、将上述溶液转移至100mL反应釜,95~110℃反应8~24h;2. Transfer the above solution to a 100mL reactor and react at 95~110℃ for 8~24h;
3、抽滤水洗,真空烘箱40~60℃干燥3~6h;3. Suction, filter and wash, dry in a vacuum oven at 40~60℃ for 3~6h;
4、将上述沉淀称取90mg分散在40mL的H 2O中; 4. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O;
5、加CuCl 2(0.5~2mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 45. Add CuCl 2 (0.5-2mmol) and stir to dissolve, and then add H 2 MoO 4 of the same amount respectively;
6、将尿素(5~20mmol)溶于40mL水;6. Dissolve urea (5-20mmol) in 40mL water;
7、将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;7. Add the urea solution dropwise to the above solution through the sealing funnel, and stir for 30 min;
8、转移至反应釜,150~180℃反应6~10h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;8. Transfer to a reaction kettle, react at 150-180°C for 6-10 hours, cool to room temperature after the reaction, collect the precipitate, wash it several times and then vacuum dry;
9、将收集样品在马弗炉中450~600℃煅烧2~4h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 49. Calcining the collected samples in a muffle furnace at 450-600°C for 2 to 4 hours at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,但不构成对本发明保护范围的限制。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention, but it does not constitute a limitation to the protection scope of the present invention.
实施例1Example 1
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(0.5mmol)搅扦溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(5mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,160℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (0.5 mmol) and stir to dissolve, and then add the same amount of H 2 MoO 4 respectively ; dissolve urea (5 mmol) in 40 mL Water, add the urea solution dropwise to the above solution through the sealing funnel, stir for 30min; transfer to the reactor, react at 160℃ for 8h, cool to room temperature after the reaction, collect the precipitate, wash several times and then vacuum dry; collect the sample Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
数据分析:data analysis:
1、SEM分析1. SEM analysis
图1为本发明实施例1制备的Co 3O 4/CuMoO 4的SEM图。从扫描图中可以看出,通过水热合成的Co 3O 4/CuMoO 4形貌呈海胆状。 Figure 1 is an SEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention. It can be seen from the scan that the Co 3 O 4 /CuMoO 4 synthesized by hydrothermal method has a sea urchin-like appearance.
2、TEM测试2. TEM test
图2为本发明实施例1制备的Co 3O 4/CuMoO 4的TEM图,从投射图中可以进一步证实海胆状的催化剂。 Figure 2 is a TEM image of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention. The projection image can further confirm the sea urchin-like catalyst.
3、BET测试3. BET test
图3为本发明实施例1制备的Co 3O 4/CuMoO 4的氮气吸附脱附等温曲线。 FIG. 3 is a nitrogen adsorption and desorption isotherm curve of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention.
4、XRD4. XRD
图4为本发明实施例1制备的Co 3O 4/CuMoO 4的XRD测试。图中所标示出的为CuMoO 4与Co 3O 4对应晶面的特征峰。 Fig. 4 is an XRD test of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention. Marked in the figure are the characteristic peaks of CuMoO 4 and Co 3 O 4 corresponding crystal planes.
5、催化产氢性能的测试5. Test of catalytic hydrogen production performance
图5为本发明实施例1制备的Co 3O 4/CuMoO 4作为催化剂催化氨硼烷水解产氢的性能测试,NH 3BH 3用量3mmol,NaOH 20mmol,催化剂10mg。测得25℃下Co 3O 4/CuMoO 4作为催化剂每分钟产氢121.5mL。 Fig. 5 is a performance test of Co 3 O 4 /CuMoO 4 prepared in Example 1 of the present invention as a catalyst to catalyze the hydrolysis of ammonia borane to produce hydrogen. The amount of NH 3 BH 3 is 3 mmol, NaOH 20 mmol, and the catalyst 10 mg. It is measured that Co 3 O 4 /CuMoO 4 is used as a catalyst to produce 121.5 mL of hydrogen per minute at 25°C.
实施例2Example 2
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应8h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 8 hours; filter and wash with suction, and dry in a vacuum oven at 40°C for 3 hours;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(0.5mmol)搅扦溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(5mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,160℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (0.5 mmol) and stir to dissolve, and then add the same amount of H 2 MoO 4 respectively ; dissolve urea (5 mmol) in 40 mL Water, add the urea solution dropwise to the above solution through the sealing funnel, stir for 30min; transfer to the reactor, react at 160℃ for 8h, cool to room temperature after the reaction, collect the precipitate, wash several times and then vacuum dry; collect the sample Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例3Example 3
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,110℃反应12h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reaction kettle, react at 110°C for 12h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(0.5mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(5mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,160℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (0.5 mmol) and stir to dissolve, then add the same amount of H 2 MoO 4 respectively ; dissolve urea (5 mmol) in 40 mL of water , The urea solution was added dropwise to the above solution through the sealing funnel, stirring for 30min; transferred to the reactor, reacted at 160℃ for 8h, after the reaction, cooled to room temperature, collected the precipitate, washed several times and dried in vacuum; Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例4Example 4
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱60℃干燥6h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry at 60°C in a vacuum oven for 6h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(0.5mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(5mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,160℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (0.5 mmol) and stir to dissolve, then add the same amount of H 2 MoO 4 respectively ; dissolve urea (5 mmol) in 40 mL of water , The urea solution was added dropwise to the above solution through the sealing funnel, stirring for 30min; transferred to the reactor, reacted at 160℃ for 8h, after the reaction, cooled to room temperature, collected the precipitate, washed several times and dried in vacuum; Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例5Example 5
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(0.5mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(5mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,150℃反应10h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (0.5 mmol) and stir to dissolve, then add the same amount of H 2 MoO 4 respectively ; dissolve urea (5 mmol) in 40 mL of water , The urea solution was added dropwise to the above solution through a liquid-sealed funnel, and stirred for 30 minutes; transferred to the reactor, reacted at 150°C for 10 hours, cooled to room temperature after the reaction, collected the precipitate, washed several times and then dried in vacuum; Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例6Example 6
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(0.5mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(5mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅扦30min;转移至反应釜,180℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (0.5 mmol) and stir to dissolve, then add the same amount of H 2 MoO 4 respectively ; dissolve urea (5 mmol) in 40 mL of water , The urea solution was added dropwise to the above solution through a liquid-sealed funnel, and stirred for 30 minutes; transferred to the reactor, reacted at 180°C for 8 hours, cooled to room temperature after the reaction, collected the precipitate, washed several times and dried in vacuum; the sample was collected Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例7Example 7
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(1mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(10mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅扦30min;转移至反应釜,160℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 (1 mmol) and stir to dissolve, then add the same amount of H 2 MoO 4 respectively ; dissolve urea (10 mmol) in 40 mL of water, The urea solution was added dropwise to the above solution through a liquid-sealed funnel, and stirred for 30 minutes; transferred to a reactor, reacted at 160°C for 8 hours, cooled to room temperature after the reaction, collected the precipitate, washed several times and dried in vacuum; Calcined in a muffle furnace at 500°C for 2h at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例8Example 8
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(2mmol)搅拌溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(20mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,160℃反应8h,反应结束后冷却至 室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中500℃煅烧2h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 ( 2 mmol) and stir to dissolve, and then add the same amount of H 2 MoO 4 respectively ; dissolve urea (20 mmol) in 40 mL of water, The urea solution was added dropwise to the above solution through a sealed liquid funnel, and stirred for 30 min; transferred to the reactor, reacted at 160°C for 8 hours, cooled to room temperature after the reaction, collected the precipitate, washed several times and then dried in vacuum; Calcined in a Furnace at 500℃ for 2h at a heating rate of 2℃/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 ;
实施例9Example 9
1、取4.5mmol Co(NO 3) 2·6H 2O、2.25mmol C 6H 12N 4、1.5mmol Na 3C 6H 5O 7·2H 2O溶于35mL去离子水中,持续搅拌直至溶解;将上述溶液转移至100mL反应釜,100℃反应24h;抽滤水洗,真空烘箱40℃干燥3h; 1, taken 4.5mmol Co (NO 3) 2 · 6H 2 O, 2.25mmol C 6 H 12 N 4, 1.5mmol Na 3 C 6 H 5 O 7 · 2H 2 O was dissolved in 35mL of deionized water, stirring was continued until dissolved ; Transfer the above solution to a 100mL reactor, react at 100°C for 24h; filter and wash with suction, and dry in a vacuum oven at 40°C for 3h;
2、将上述沉淀称取90mg分散在40mL的H 2O中;加CuCl 2(2mmol)搅扦溶解,再对应分别加相同物质的量的H 2MoO 4;将尿素(20mmol)溶于40mL水,将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌30min;转移至反应釜,160℃反应8h,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;将收集样品在马弗炉中600℃煅烧3h,升温速率为2℃/min得到最终催化剂Co 3O 4/CuMoO 42. Weigh 90 mg of the above precipitate and disperse it in 40 mL of H 2 O; add CuCl 2 ( 2 mmol) and stir to dissolve, then add the same amount of H 2 MoO 4 respectively ; dissolve urea (20 mmol) in 40 mL of water , The urea solution was added dropwise to the above solution through the sealing funnel, stirring for 30min; transferred to the reactor, reacted at 160℃ for 8h, after the reaction, cooled to room temperature, collected the precipitate, washed several times and dried in vacuum; It was calcined in a muffle furnace at 600°C for 3 hours at a heating rate of 2°C/min to obtain the final catalyst Co 3 O 4 /CuMoO 4 .
以上所述是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也视为本发明的保护范围。The above are the preferred embodiments of the present invention. It should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, several improvements and modifications can be made, and these improvements and modifications are also considered This is the protection scope of the present invention.

Claims (10)

  1. 一种Co 3O 4/CuMoO 4复合物,其特征在于:由纳米棒组成的海胆状Co 3O 4/CuMoO 4复合物。 A Co 3 O 4 /CuMoO 4 composite, which is characterized in that: a sea urchin-like Co 3 O 4 /CuMoO 4 composite composed of nanorods.
  2. 一种Co 3O 4/CuMoO 4复合物的制备方法,其特征在于,包括以下步骤: A preparation method of Co 3 O 4 /CuMoO 4 composite, which is characterized in that it comprises the following steps:
    (1)、取硝酸钴、六次甲基四胺、柠檬酸三钠溶于去离子水中,持续搅拌直至溶解,其中,硝酸钴、六次甲基四胺、柠檬酸三钠三者投料的物质的量比为6∶3∶2;(1). Dissolve cobalt nitrate, hexamethylenetetramine, and trisodium citrate in deionized water and continue stirring until dissolved. Among them, cobalt nitrate, hexamethylenetetramine, and trisodium citrate are charged The quantity ratio of the substances is 6:3:2;
    (2)、将上述溶液转移至反应釜,在一定温度下反应一段时间;(2) Transfer the above solution to the reaction kettle and react for a period of time at a certain temperature;
    (3)、然后,抽滤水洗,真空烘箱干燥;(3) Then, it is filtered and washed with water and dried in a vacuum oven;
    (4)、取步骤(3)中的沉淀物分散于水中;(4) Disperse the precipitate in step (3) in water;
    (5)、加CuCl 2搅拌溶解,再对应加入相同物质的量的H 2MoO 4(5) Add CuCl 2 and stir to dissolve, and then add H 2 MoO 4 corresponding to the same substance;
    (6)、将尿素溶于水中;(6) Dissolve urea in water;
    (7)、将尿素溶液通过封液漏斗逐滴滴加至上述溶液,搅拌;(7) Add the urea solution dropwise to the above solution through the sealing funnel, and stir;
    (8)、转移至反应釜,在一定温度下反应一段时间,反应结束后冷却至室温,收集沉淀,洗涤数次后真空干燥;(8) Transfer to the reactor, react for a period of time at a certain temperature, cool to room temperature after the reaction, collect the precipitate, wash it several times and then vacuum dry;
    (9)、将收集样品在马弗炉中煅烧一段时间后,得到最终催化剂Co 3O 4/CuMoO 4(9) After calcining the collected samples in a muffle furnace for a period of time, the final catalyst Co 3 O 4 /CuMoO 4 is obtained .
  3. 根据权利要求2所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:CuCl 2与尿素投料的物质的量为1∶10。 The method for preparing the Co 3 O 4 /CuMoO 4 composite according to claim 2, wherein the amount of the CuCl 2 and urea is 1:10.
  4. 根据权利要求2所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:步骤(2)中钴前驱体的合成条件为95~110℃反应8~24h。 The preparation method of the Co 3 O 4 /CuMoO 4 composite according to claim 2, wherein the synthesis conditions of the cobalt precursor in step (2) are 95-110° C. for 8-24 hours.
  5. 根据权利要求2所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:步骤(3)中真空烘箱的温度为40~60℃。 The method for preparing the Co 3 O 4 /CuMoO 4 composite according to claim 2, wherein the temperature of the vacuum oven in step (3) is 40-60°C.
  6. 根据权利要求5所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:步骤(3)中干燥时间为3~6h。 The method for preparing the Co 3 O 4 /CuMoO 4 composite according to claim 5, wherein the drying time in step (3) is 3 to 6 hours.
  7. 根据权利要求2所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:步骤(8)中,Co 3O 4/CuMoO 4的合成条件为150~180℃反应6~10h。 The preparation method of Co 3 O 4 /CuMoO 4 composite according to claim 2, characterized in that: in step (8), the synthesis condition of Co 3 O 4 /CuMoO 4 is 150-180° C. for 6-10 hours.
  8. 根据权利要求2所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:步骤(9)中,马弗炉温度为450~600℃煅烧2~4h。 The method for preparing the Co 3 O 4 /CuMoO 4 composite according to claim 2, characterized in that: in step (9), the muffle furnace temperature is 450 to 600° C. for calcination for 2 to 4 hours.
  9. 根据权利要求8所述的Co 3O 4/CuMoO 4复合物的制备方法,其特征在于:马弗炉升温速率为2℃/min。 The method for preparing the Co 3 O 4 /CuMoO 4 composite according to claim 8, wherein the temperature rise rate of the muffle furnace is 2° C./min.
  10. 一种如权利要求1-9任一项所述的Co 3O 4/CuMoO 4复合物作为催化剂在催化氨硼烷水解中的应用。 An application of the Co 3 O 4 /CuMoO 4 composite according to any one of claims 1-9 as a catalyst in the hydrolysis of ammonia borane.
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