CN104226330B - A kind of Au/Co (OH)2Nano array structure catalyst - Google Patents
A kind of Au/Co (OH)2Nano array structure catalyst Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 65
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000000758 substrate Substances 0.000 claims abstract description 39
- 239000010931 gold Substances 0.000 claims abstract description 34
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 25
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 239000006260 foam Substances 0.000 claims abstract description 17
- BTJIUGUIPKRLHP-UHFFFAOYSA-N 4-nitrophenol Chemical compound OC1=CC=C([N+]([O-])=O)C=C1 BTJIUGUIPKRLHP-UHFFFAOYSA-N 0.000 claims abstract description 10
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910052737 gold Inorganic materials 0.000 claims abstract description 9
- 230000008859 change Effects 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 229910001429 cobalt ion Inorganic materials 0.000 claims description 17
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical compound [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 claims description 17
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 15
- 239000004202 carbamide Substances 0.000 claims description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 14
- 239000008367 deionised water Substances 0.000 claims description 14
- 229910021641 deionized water Inorganic materials 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 9
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- 239000011259 mixed solution Substances 0.000 claims description 9
- 238000011065 in-situ storage Methods 0.000 claims description 8
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 claims description 7
- PLIKAWJENQZMHA-UHFFFAOYSA-N 4-aminophenol Chemical compound NC1=CC=C(O)C=C1 PLIKAWJENQZMHA-UHFFFAOYSA-N 0.000 claims description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- 238000001556 precipitation Methods 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 5
- 150000001868 cobalt Chemical class 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 230000009467 reduction Effects 0.000 claims description 5
- 238000003786 synthesis reaction Methods 0.000 claims description 5
- 229910021503 Cobalt(II) hydroxide Inorganic materials 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- ASKVAEGIVYSGNY-UHFFFAOYSA-L cobalt(ii) hydroxide Chemical compound [OH-].[OH-].[Co+2] ASKVAEGIVYSGNY-UHFFFAOYSA-L 0.000 claims description 3
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 3
- 239000012279 sodium borohydride Substances 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 229910017052 cobalt Inorganic materials 0.000 claims 5
- 239000010941 cobalt Substances 0.000 claims 5
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims 5
- RJHLTVSLYWWTEF-UHFFFAOYSA-K gold trichloride Chemical class Cl[Au](Cl)Cl RJHLTVSLYWWTEF-UHFFFAOYSA-K 0.000 claims 2
- OQUOOEBLAKQCOP-UHFFFAOYSA-N nitric acid;hexahydrate Chemical compound O.O.O.O.O.O.O[N+]([O-])=O OQUOOEBLAKQCOP-UHFFFAOYSA-N 0.000 claims 2
- 238000013019 agitation Methods 0.000 claims 1
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- 238000005984 hydrogenation reaction Methods 0.000 abstract description 4
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- 230000007423 decrease Effects 0.000 abstract description 2
- 238000002386 leaching Methods 0.000 abstract description 2
- 239000002923 metal particle Substances 0.000 abstract description 2
- 229910000510 noble metal Inorganic materials 0.000 abstract description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 238000004506 ultrasonic cleaning Methods 0.000 description 6
- 238000011161 development Methods 0.000 description 5
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 5
- 239000010970 precious metal Substances 0.000 description 5
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- QGUAJWGNOXCYJF-UHFFFAOYSA-N cobalt dinitrate hexahydrate Chemical compound O.O.O.O.O.O.[Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O QGUAJWGNOXCYJF-UHFFFAOYSA-N 0.000 description 3
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
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- 238000005516 engineering process Methods 0.000 description 2
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 2
- 238000002173 high-resolution transmission electron microscopy Methods 0.000 description 2
- 239000002815 homogeneous catalyst Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910020599 Co 3 O 4 Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
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- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
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- FDWREHZXQUYJFJ-UHFFFAOYSA-M gold monochloride Chemical compound [Cl-].[Au+] FDWREHZXQUYJFJ-UHFFFAOYSA-M 0.000 description 1
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- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
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Abstract
一种Au/Co(OH)2纳米阵列结构化催化剂,属于催化技术领域。泡沫镍基底上直接生长了矩形片状形貌的纳米阵列,形成的纳米材料结构确定、有序、可实现高的比表面积。泡沫镍基底上的微米片连结着宏观规模的基底和纳米级的贵金属颗粒,这确保了足够的附着力并且避免了在催化反应中的沥出。单片方形纳米片的平均尺寸为1.5微米宽,金颗粒尺寸为3‑5nm。它可有效用于对硝基苯酚的加氢还原反应,反应速率为30.8s‑1g‑1,Au/Co(OH)2纳米阵列结构化催化剂同时具有出色的循环稳定性能,经过6次循环使用后形貌基本没有变化,更为重要的是催化性能也基本保持不变。解决了传统整体催化剂活性组分分布不均匀,与载体的粘结性不强,反应中活性逐步下降的问题。The invention discloses an Au/Co(OH) 2 nano-array structured catalyst, belonging to the technical field of catalysis. Nano-arrays with rectangular flake-like morphology are directly grown on the foamed nickel substrate, and the formed nano-materials have a definite and orderly structure and can achieve high specific surface area. The microplatelets on the nickel foam substrate link the macroscale substrate and the nanoscale noble metal particles, which ensures sufficient adhesion and avoids leaching during the catalytic reaction. The average size of the monolithic square nanosheets is 1.5 micrometers wide, and the gold particles are 3‑5 nm in size. It can be effectively used for the hydrogenation reduction reaction of p-nitrophenol with a reaction rate of 30.8 s ‑1 g ‑1 , and the Au/Co(OH) 2 nanoarray structured catalyst also has excellent cycle stability after 6 cycles After use, the morphology basically does not change, and more importantly, the catalytic performance also basically remains unchanged. It solves the problem of uneven distribution of active components of traditional monolithic catalysts, weak bonding with the carrier, and gradual decline in activity during the reaction.
Description
技术领域technical field
本发明属于催化技术领域,具体涉及生长在泡沫镍基底上的结构有序,尺寸分布均匀的Au/Co(OH)2纳米阵列结构化催化剂及其制备方法。The invention belongs to the technical field of catalysis, and in particular relates to an Au/Co(OH) 2 nano-array structured catalyst with ordered structure and uniform size distribution grown on a nickel foam substrate and a preparation method thereof.
背景技术Background technique
随着国民经济的迅猛发展,中国面临资源匮乏与环境恶化的双重压力,资源的有效利用已经成为紧迫的国家重大需求。催化剂作为工业生产中关键一步,它的研发及应用与能源化工的各个方面息息相关。催化剂按反应体系的相态分为均相催化剂和多相催化剂,在当前工业应用领域,多采用多相催化剂。多相催化剂又称非均相催化剂,用在不同反应相的催化反应中,即催化剂与反应物处于不同的相态。近几年在多相催化研究领域,大量研究工作主要集中在粒状和粉末状催化剂的研究上,而传统的颗粒状催化剂填装的催化反应器在通常情况下床层压降较大,床层间存在较大的温度梯度,且反应物在催化剂颗粒表面分布不均匀。为了克服这些缺点,近年来,一种催化剂活性组分与整体式催化剂载体复合在一起的新型催化剂-结构化催化剂的研究引起了人们的极大关注。与粒状或粉状末催化剂相比,这种催化剂可以强化催化反应过程,提高催化效率,降低能耗,简化生产流程,并已在环保、催化燃烧及催化精馏等领域得到了广泛的应用。With the rapid development of the national economy, China is facing the dual pressure of resource scarcity and environmental degradation, and the effective use of resources has become an urgent national major demand. Catalyst is a key step in industrial production, its research and development and application are closely related to all aspects of energy and chemical industry. Catalysts are divided into homogeneous catalysts and heterogeneous catalysts according to the phase state of the reaction system. In the current industrial application field, heterogeneous catalysts are mostly used. Heterogeneous catalysts, also known as heterogeneous catalysts, are used in catalytic reactions in different reaction phases, that is, the catalyst and the reactants are in different phase states. In recent years, in the field of heterogeneous catalysis research, a large amount of research work has mainly focused on the research of granular and powdery catalysts. However, the catalytic reactor filled with traditional granular catalysts usually has a large bed pressure drop, and the bed layer There is a large temperature gradient between them, and the reactants are unevenly distributed on the surface of the catalyst particles. In order to overcome these disadvantages, in recent years, the research of a new catalyst-structured catalyst in which the catalytic active components are composited with the monolithic catalyst support has attracted great attention. Compared with granular or powdered powder catalysts, this catalyst can strengthen the catalytic reaction process, improve catalytic efficiency, reduce energy consumption, and simplify the production process, and has been widely used in the fields of environmental protection, catalytic combustion, and catalytic distillation.
结构化催化剂通常由三部分构成:结构化基体、涂层及催化活性组分。目前,结构化催化剂的载体主要有陶瓷基和金属基,陶瓷基载体抗震性差,使用寿命短;金属基载体具有壁薄、几何面积和空隙率大、导热性能良好、热容小和强度高等优点,而且从金属基的模拟结果进行分析,其传热能力好,压降极低,并且结构易于控制,这将极大提升金属基的催化效率,因而它显示出了极好的应用前景。同时,银凤翔等人提出可以将金属基催化剂当成一个整体式组件,应用到吸/放热反应的直接耦合过程,这将提升反应热热效率,实现资源、能量、设备和流程的一体化,大大强化反应过程。Structured catalysts usually consist of three parts: a structured substrate, a coating, and a catalytically active component. At present, the supports of structured catalysts mainly include ceramic base and metal base. The ceramic base support has poor shock resistance and short service life; the metal base support has the advantages of thin wall, large geometric area and porosity, good thermal conductivity, small heat capacity and high strength. , and analyzed from the simulation results of the metal base, it has good heat transfer capacity, extremely low pressure drop, and easy control of the structure, which will greatly improve the catalytic efficiency of the metal base, so it shows an excellent application prospect. At the same time, Yin Fengxiang and others proposed that the metal-based catalyst can be used as an integral component and applied to the direct coupling process of endothermic/exothermic reactions, which will improve the thermal efficiency of the reaction and realize the integration of resources, energy, equipment and processes. Strengthen the reaction process.
随着纳米材料可控合成技术的发展和分析手段的进步,为高性能催化剂的开发带来新的契机。纳米阵列材料以其新颖的结构、独特的光电特性和催化特性,在纳米器件制作等领域的应用有着巨大的优势和潜力受到人们的极大关注。另一方面,催化剂材料尺寸的微细化已经被证明是提高催化性能的有效途径,通过增大表面与气体、液体等反应原子的接触机会,使活性得到提高。对于结构规整的纳米阵列来说,可以通过减小一维纳米材料的尺寸来增大催化剂整体材料的比表面积。With the development of controllable synthesis technology of nanomaterials and the improvement of analytical methods, new opportunities have been brought for the development of high-performance catalysts. Due to its novel structure, unique photoelectric and catalytic properties, nano-array materials have great advantages and potentials in the field of nano-device fabrication and have attracted great attention. On the other hand, the miniaturization of the size of catalyst materials has been proved to be an effective way to improve the catalytic performance. By increasing the contact opportunities between the surface and reactive atoms such as gases and liquids, the activity is improved. For structured nanoarrays, the specific surface area of the overall catalyst material can be increased by reducing the size of the one-dimensional nanomaterials.
负载型金催化剂具有良好的低温催化活性、较好的抗中毒性能和催化稳定性能,广泛应用于CO的低温氧化(Bond,G. C.;Thompson,D.T.Cat.Rev._Sci.Eng.1999,41,319.)、芳香胺的催化加氢(Chen,Y. Y.;Qiu,J.S.;Wang,X.K.;Xiu,J.H.J.Catal.2006,242,227.)、链烷烃的氧化(Hughes,M.D.;Xu,Y. J.;Jenkins,P.Nature2005,437,1132.)、多元醇的选择性氧化(Berndt,H.Appl.Catal.,A:Chem.2003,244,169.)。相对于其它贵金属如铂和钯,金的价格要比这两者便宜,这使得金催化剂在实际工业应用中更有发展前景。不过即使是金这一种贵金属,其价格仍然昂贵,单纯利用贵金属作为催化剂,工业成本太高,而通过将贵金属负载在载体上,会大幅降低生产成本并大幅提升贵金属的利用效率。Supported gold catalysts have good low-temperature catalytic activity, good anti-poisoning performance and catalytic stability, and are widely used in the low-temperature oxidation of CO (Bond, G. C.; Thompson, D.T.Cat.Rev._Sci.Eng.1999, 41, 319 .), catalytic hydrogenation of aromatic amines (Chen, Y. Y.; Qiu, J.S.; Wang, X.K.; Xiu, J.H.J. Catal.2006, 242, 227.), oxidation of paraffins (Hughes, M.D.; Xu, Y. J.; Jenkins, P. Nature 2005, 437, 1132.), selective oxidation of polyols (Berndt, H. Appl. Catal., A: Chem. 2003, 244, 169.). Compared with other precious metals such as platinum and palladium, the price of gold is cheaper than these two, which makes gold catalysts more promising for practical industrial applications. However, even gold, a precious metal, is still expensive. The industrial cost of using precious metals as catalysts is too high. However, by loading precious metals on the carrier, the production cost will be greatly reduced and the utilization efficiency of precious metals will be greatly improved.
但是到目前为止,对于纳米阵列应用于结构化催化剂的研究工作还较少,一定程度上限制了高性能催化剂的工业开发和应用。基于此我们提出基于Co(OH)2纳米阵列为载体合成Au/Co(OH)2纳米阵列结构化催化剂,形成的纳米结构确定、有序,可实现高的比表面积,解决传统整体催化剂活性组分分布不均匀,与载体的粘结性不强的问题。在这里我们以对硝基苯酚的加氢还原反应评价了Au/Co(OH)2纳米阵列结构化催化剂的性能。But so far, there are few researches on the application of nanoarrays to structured catalysts, which limits the industrial development and application of high-performance catalysts to a certain extent. Based on this, we propose to synthesize Au/Co(OH) 2 nanoarray structured catalysts based on Co(OH) 2 nanoarrays as the carrier. The problem of uneven distribution and weak adhesion with the carrier. Here we evaluated the performance of Au/Co(OH) 2 nanoarray structured catalysts for the hydrogenation reduction reaction of p-nitrophenol.
发明内容Contents of the invention
本发明的目的是提供一种Au/Co(OH)2纳米阵列结构化催化剂的设计合成。The purpose of the present invention is to provide a design synthesis of Au/Co(OH) 2nano -array structured catalyst.
本发明提供的一种Au/Co(OH)2纳米阵列结构化催化剂是直接在泡沫镍基底上生长Co(OH)2纳米片阵列,再通过原位还原氯金酸得到Au/Co(OH)2纳米阵列催化剂。A kind of Au/Co(OH) 2nano -array structured catalyst provided by the present invention is to directly grow Co(OH) 2nanosheet arrays on the foamed nickel substrate, and then obtain Au/Co(OH) by reducing chloroauric acid in situ 2 Nanoarray Catalysts.
本发明提供上述一种Au/Co(OH)2纳米阵列结构化催化剂的设计合成,采用原位水热合成技术在泡沫镍基底上生长了氢氧化钴矩形微米片,之后通过原位还原氯金酸,在矩形微米片上均匀负载金颗粒得到结构有序、竖直有序地生长在泡沫镍基底上,尺寸分布均匀的Au/Co(OH)2纳米阵列结构化催化剂。具体制备方法如下:The present invention provides the design and synthesis of the above-mentioned Au/Co(OH) 2 nano-array structured catalyst, using in-situ hydrothermal synthesis technology to grow cobalt hydroxide rectangular micro-sheets on the foamed nickel substrate, and then reducing gold chloride in situ Au/Co(OH) 2 nano-array structured catalyst with ordered structure, vertical and orderly growth on nickel foam substrate, and uniform size distribution. The specific preparation method is as follows:
a.将8cm2的泡沫镍基底用盐酸超声清洗5-10min,再用无水乙醇或丙酮超声清洗5-10min,再用去离子水清洗干净,得到泡沫镍基底备用;a. Ultrasonic cleaning of 8 cm 2 nickel foam substrates with hydrochloric acid for 5-10 minutes, then ultrasonic cleaning with absolute ethanol or acetone for 5-10 minutes, and then cleaning with deionized water to obtain foam nickel substrates for use;
b.将可溶性钴盐、氟化铵和尿素溶解在去离子水中配成溶液,其中钴离子的浓度为0.01-2mol/L,氟化铵与钴离子的物质的量比为1∶4,尿素与钴离子的物质的量比为1∶5;b. Dissolve soluble cobalt salt, ammonium fluoride and urea in deionized water to form a solution, wherein the concentration of cobalt ions is 0.01-2mol/L, the ratio of ammonium fluoride to cobalt ions is 1:4, and urea The substance ratio with cobalt ion is 1:5;
c.将步骤a所得泡沫镍基底浸入步骤b所得混合溶液,并于反应釜中120℃温度水热12h,反应结束后自然冷却至室温;所得基底用水和无水乙醇洗涤,去掉杂质,在80℃烘箱中干燥2-4h;c. Immerse the foamed nickel substrate obtained in step a into the mixed solution obtained in step b, and heat it in a reactor at 120° C. for 12 hours, and cool it to room temperature naturally after the reaction; the obtained substrate is washed with water and absolute ethanol to remove impurities. Dry in an oven at ℃ for 2-4h;
d.将可溶性钴盐和尿素溶解在去离子水中配成溶液,其中钴离子的浓度为0.025-2mol/L,尿素与钴离子的物质的量比为1∶10;d. Soluble cobalt salt and urea are dissolved in deionized water to form a solution, wherein the concentration of cobalt ions is 0.025-2mol/L, and the mass ratio of urea and cobalt ions is 1: 10;
e.将步骤c中所得基底浸入步骤d所得混合溶液,并于反应釜中100℃温度水热10h,反应结束后自然冷却至室温;所得基底用水和无水乙醇洗涤,去掉杂质,在80℃烘箱中干燥2-4h;e. Immerse the substrate obtained in step c into the mixed solution obtained in step d, and heat it in a reaction kettle at 100°C for 10 hours, and cool it to room temperature naturally after the reaction; wash the obtained substrate with water and absolute ethanol to remove impurities, and heat it at 80°C Dry in oven for 2-4h;
f.将步骤e所得基底通过沉积沉淀法,使用NaBH4原位还原5-600μL氯金酸得到Au/Co(OH)2纳米阵列结构化催化剂。f. Using NaBH 4 to reduce 5-600 μL chloroauric acid in situ to obtain the Au/Co(OH) 2 nano-array structured catalyst by the deposition precipitation method on the substrate obtained in step e.
步骤b,d中可溶性钴盐为六水合硝酸钴。将上述制得的Au/Co(OH)2纳米阵列结构化催化剂应用于对硝基苯酚的还原合成对氨基苯酚,反应条件为在室温条件下,取(5-70ml)0.625mM或2.5mM的对硝基苯酚水溶液,加入0-65ml水,通氮气5-10min,磁力搅拌,加入硼氢化钠10-20mg,溶液颜色由淡黄色变成亮黄色,加入适量催化剂(泡沫镍大小为2*4cm2)。The soluble cobalt salt in steps b and d is cobalt nitrate hexahydrate. The Au/Co(OH) nano - array structured catalyst prepared above is applied to the reduction of p-nitrophenol to synthesize p-aminophenol, the reaction conditions are at room temperature, take (5-70ml) 0.625mM or 2.5mM For p-nitrophenol aqueous solution, add 0-65ml of water, blow nitrogen for 5-10min, stir magnetically, add 10-20mg of sodium borohydride, the color of the solution changes from light yellow to bright yellow, add an appropriate amount of catalyst (the size of nickel foam is 2*4cm 2 ).
本发明的优点在于:(1)泡沫镍基底上直接生长了矩形片状形貌的纳米阵列,形成的纳米材料结构确定、有序、可实现高的比表面积;(2)泡沫镍基底 上的微米片连结着宏观规模的基底和纳米级的贵金属颗粒,这确保了足够的附着力并且避免了在催化反应中的沥出。(3)纳米阵列结构具有良好的电子传输性能,并且有利于活性物种的扩散;(4)微米片提供了三维支架的稳定支撑结构,使得催化剂重复使用六次后催化活性基本保持不变。基于以上优点,Au/Co(OH)2纳米阵列结构化催化剂表现出优异的催化性能。所制得的结构化催化剂可有效的用于对硝基苯酚的加氢还原反应,反应物转化率高,产物选择性高。此外它也可解决由均相催化剂和散堆颗粒催化剂带来的一系列问题,使该工艺满足环保和可持续发展的要求。它可有效用于对硝基苯酚的加氢还原反应,反应速率为30.8s-1g-1,Au/Co(OH)2纳米阵列结构化催化剂同时具有出色的循环稳定性能,经过6次循环使用后形貌基本没有变化,更为重要的是催化性能也基本保持不变。解决了传统整体催化剂活性组分分布不均匀,与载体的粘结性不强,反应中活性逐步下降的问题。这种阵列式结构化催化剂的设计策略可以拓展到在金属基底上合成其它的金属氧化物纳米阵列,并且为新型高效结构化催化剂的设计提供了新思路。The present invention has the advantages of: (1) directly grow nano-arrays of rectangular plate shape on the foamed nickel substrate, and the nanomaterial structure formed is definite, orderly, and can realize high specific surface area; (2) the nano-arrays on the foamed nickel substrate The microsheets link the macroscale substrate and the nanoscale noble metal particles, which ensure sufficient adhesion and avoid leaching during catalytic reactions. (3) The nano-array structure has good electron transport performance and is conducive to the diffusion of active species; (4) the micro-sheet provides a stable support structure of the three-dimensional scaffold, so that the catalytic activity of the catalyst remains basically unchanged after six times of repeated use. Based on the above advantages, the Au/Co(OH) 2 nanoarray structured catalyst exhibits excellent catalytic performance. The prepared structured catalyst can be effectively used in the hydrogenation reduction reaction of p-nitrophenol, and has high conversion rate of reactants and high product selectivity. In addition, it can also solve a series of problems caused by homogeneous catalysts and random particle catalysts, so that the process can meet the requirements of environmental protection and sustainable development. It can be effectively used in the hydrogenation reduction reaction of p-nitrophenol, the reaction rate is 30.8s -1 g -1 , the Au/Co(OH) 2 nano-array structured catalyst also has excellent cycle stability, after 6 cycles After use, the morphology basically does not change, and more importantly, the catalytic performance also basically remains unchanged. It solves the problem of uneven distribution of active components of traditional monolithic catalysts, weak bonding with the carrier, and gradual decline in activity during the reaction. The design strategy of this array structured catalyst can be extended to the synthesis of other metal oxide nanoarrays on metal substrates, and provides a new idea for the design of new efficient structured catalysts.
附图说明Description of drawings
图1是实施例1所制备的结构化催化剂的XRD图;Fig. 1 is the XRD pattern of the structured catalyst prepared in embodiment 1;
图2是实施例1所制备的结构化催化剂的SEM图;Fig. 2 is the SEM figure of the structured catalyst prepared in embodiment 1;
图3是实施例1所制备的结构化催化剂的HRTEM图;Fig. 3 is the HRTEM figure of the structured catalyst prepared in embodiment 1;
图4是实施例1所制备的结构化催化剂的催化性能图;Fig. 4 is the catalytic performance diagram of the structured catalyst prepared in embodiment 1;
图5是实施例1所制备的结构化催化剂的重复使用性能图;Fig. 5 is the repeated use performance diagram of the structured catalyst prepared in embodiment 1;
图6是实施例2所制备的结构化催化剂的SEM图;Fig. 6 is the SEM figure of the structured catalyst prepared in embodiment 2;
具体实施方式detailed description
下面结合具体实施例对本发明作进一步描述。The present invention will be further described below in conjunction with specific embodiments.
实施例1:Example 1:
a.将8cm2的泡沫镍基底用盐酸超声清洗5min,再用无水乙醇超声清洗5min,再用去离子水清洗干净,得到泡沫镍基底备用;a. Ultrasonic cleaning the 8 cm 2 nickel foam substrate with hydrochloric acid for 5 minutes, then ultrasonic cleaning with absolute ethanol for 5 minutes, and then cleaning with deionized water to obtain the nickel foam substrate for use;
b.将0.5820g六水合硝酸钴、0.2963g氟化铵和0.6000g尿素溶解在40mL去离子水中,搅拌均匀后,装入水热釜中;b. Dissolve 0.5820g of cobalt nitrate hexahydrate, 0.2963g of ammonium fluoride and 0.6000g of urea in 40mL of deionized water, stir evenly, and put it into a hydrothermal kettle;
c.将步骤a所得泡沫镍基底浸入步骤b所得混合溶液,并于反应釜中120℃ 温度水热12h,反应结束后自然冷却至室温;所得基底用水和无水乙醇洗涤,去掉杂质,在80℃烘箱中干燥2h;c. Immerse the foamed nickel substrate obtained in step a into the mixed solution obtained in step b, and heat it with water at 120°C for 12 hours in a reaction kettle, and cool it to room temperature naturally after the reaction; the obtained substrate is washed with water and absolute ethanol to remove impurities. Dry in an oven at ℃ for 2 hours;
d.将可溶性钴盐和尿素溶解在去离子水中配成溶液,其中钴离子的浓度为0.025mol/L,加入量为0.296g,尿素与钴离子的物质的量比为1∶10;d. Soluble cobalt salt and urea are dissolved in deionized water to form a solution, wherein the concentration of cobalt ions is 0.025mol/L, the addition is 0.296g, and the substance ratio of urea and cobalt ions is 1: 10;
e.将步骤c中所得基底浸入步骤d所得混合溶液,并于反应釜中100℃温度水热10h,反应结束后自然冷却至室温;所得基底用水和无水乙醇洗涤,去掉杂质,在80℃烘箱中干燥2h;e. Immerse the substrate obtained in step c into the mixed solution obtained in step d, and heat it in a reaction kettle at 100°C for 10 hours, and cool it to room temperature naturally after the reaction; wash the obtained substrate with water and absolute ethanol to remove impurities, and heat it at 80°C Dry in oven for 2h;
f.将步骤e所得基底通过沉积沉淀法,使用NaBH4原位还原200μL氯金酸得到Au/Co(OH)2纳米阵列结构化催化剂。单片方形纳米片的平均尺寸为1.5微米宽,5nm厚,金颗粒尺寸为3-5nm。f. The substrate obtained in step e was subjected to in-situ reduction of 200 μL of chloroauric acid with NaBH 4 to obtain an Au/Co(OH) 2 nanoarray structured catalyst by deposition precipitation method. The average size of the monolithic square nanosheets is 1.5 micrometers wide and 5 nm thick, and the gold particle size is 3-5 nm.
所制备的结构化催化剂的XRD图见图1(负载金前后),SEM图见图2,HRTEM图见图3。The XRD pattern of the prepared structured catalyst is shown in Fig. 1 (before and after loading gold), the SEM pattern is shown in Fig. 2, and the HRTEM pattern is shown in Fig. 3.
将制得Au/Co(OH)2纳米阵列结构化催化剂应用于对硝基苯酚的还原合成对氨基苯酚。反应条件为在室温条件下,取70ml2.5mM的对硝基苯酚水溶液,通氮气5-10min,磁力搅拌,加入硼氢化钠20mg,溶液颜色由淡黄色变成亮黄色,加入上述制备的Au/Co(OH)2纳米阵列结构化催化剂。The prepared Au/Co(OH) 2 nano-array structured catalyst was applied to the reduction of p-nitrophenol to synthesize p-aminophenol. The reaction conditions are as follows: at room temperature, take 70ml of 2.5mM p-nitrophenol aqueous solution, pass nitrogen gas for 5-10min, stir magnetically, add 20mg of sodium borohydride, the color of the solution changes from light yellow to bright yellow, add the Au/ Co(OH) 2 Nanoarray Structured Catalysts.
催化性能图见图4(其中还包括与常规的纳米线Co3O4作为催化剂的比较情况),重复使用性能图见图5。The catalytic performance diagram is shown in Figure 4 (which also includes the comparison with the conventional nanowire Co 3 O 4 as a catalyst), and the repeated use performance diagram is shown in Figure 5 .
实施例2:Example 2:
a.将8cm2的泡沫镍基底用盐酸(1mol/L)超声清洗5min,再用无水乙醇超声清洗5min,再用去离子水清洗干净,得到铁基底备用;a. Ultrasonic cleaning of 8 cm 2 nickel foam substrates with hydrochloric acid (1mol/L) for 5 minutes, then ultrasonic cleaning with absolute ethanol for 5 minutes, and then cleaning with deionized water to obtain iron substrates for later use;
b.将1.164g六水合硝酸钴、0.56g六次甲基四胺溶解在40mL去离子水中,搅拌均匀后,装入水热釜中;b. Dissolve 1.164g of cobalt nitrate hexahydrate and 0.56g of hexamethylenetetramine in 40mL of deionized water, stir evenly, and put it into a hydrothermal kettle;
c.将步骤a所得泡沫镍基底浸入步骤b所得混合溶液,并于反应釜中100℃温度水热10h,反应结束后自然冷却至室温;所得基底用水和无水乙醇洗涤,去掉杂质,在80℃烘箱中干燥2h;c. Immerse the foamed nickel substrate obtained in step a into the mixed solution obtained in step b, and heat it with water at 100°C for 10 hours in a reaction kettle, and cool it to room temperature naturally after the reaction; the obtained substrate is washed with water and absolute ethanol to remove impurities. Dry in an oven at ℃ for 2 hours;
d.将步骤c所得基底通过沉积沉淀法,使用NaBH4原位还原200μL氯金酸得到Au/Co(Oh)2纳米阵列结构化催化剂。纳米片的厚度为10纳米左右,金颗粒尺寸为3-5nm。d. The substrate obtained in step c was subjected to in situ reduction of 200 μL of chloroauric acid with NaBH 4 to obtain an Au/Co(Oh) 2 nanoarray structured catalyst by deposition precipitation method. The thickness of the nanosheets is about 10 nanometers, and the size of the gold particles is 3-5nm.
所制备的结构化催化剂的SEM图见图6。The SEM image of the prepared structured catalyst is shown in Figure 6.
Claims (6)
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