CN102861576A - Pd/ZnO/C composite nano catalyst and preparation method thereof - Google Patents
Pd/ZnO/C composite nano catalyst and preparation method thereof Download PDFInfo
- Publication number
- CN102861576A CN102861576A CN201210367268XA CN201210367268A CN102861576A CN 102861576 A CN102861576 A CN 102861576A CN 201210367268X A CN201210367268X A CN 201210367268XA CN 201210367268 A CN201210367268 A CN 201210367268A CN 102861576 A CN102861576 A CN 102861576A
- Authority
- CN
- China
- Prior art keywords
- zno
- catalyst
- composite nano
- nano
- preparation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Catalysts (AREA)
Abstract
本发明公开一种Pd/ZnO/C复合纳米催化剂及其制备方法,所述的一种Pd/ZnO/C复合纳米催化剂,其中Pd、ZnO、C按质量比计算,即Pd:ZnO:C为0.5:1:1的比例复合而成的纳米催化剂;其中所述的C为过200目筛的活性炭。其制备方法即首先制备ZnO纳米粒子,然后按照质量比为1:1,把过200目筛的活性炭与ZnO纳米粒子在乙二醇水溶液中搅拌充分混合均匀后得到的混合液用液相还原法负载纳米Pd颗粒即得Pd/ZnO/C复合纳米催化剂。本发明的一种Pd/ZnO/C复合纳米催化剂抗中毒能力强,在碱性溶液中对乙醇有很好催化氧化性能。
The invention discloses a Pd/ZnO/C composite nano catalyst and a preparation method thereof. The Pd/ZnO/C composite nano catalyst, wherein Pd, ZnO, and C are calculated by mass ratio, that is, Pd:ZnO:C is A nano-catalyst compounded at a ratio of 0.5:1:1; wherein the C is activated carbon passing through a 200-mesh sieve. The preparation method is to first prepare ZnO nanoparticles, and then according to the mass ratio of 1:1, stir the activated carbon and ZnO nanoparticles that have passed through a 200-mesh sieve in an aqueous solution of ethylene glycol and mix them well. The Pd/ZnO/C composite nano-catalyst is obtained by loading nano-Pd particles. The Pd/ZnO/C composite nano-catalyst of the invention has strong anti-poisoning ability and good catalytic oxidation performance to ethanol in alkaline solution.
Description
技术领域 technical field
本发明属于纳米催化剂材料制备技术领域,具体涉及一种对乙醇具有高催化活性Pd/ZnO/C复合纳米催化剂及其制备方法 The invention belongs to the technical field of preparation of nano-catalyst materials, in particular to a Pd/ZnO/C composite nano-catalyst with high catalytic activity to ethanol and its preparation method
背景技术 Background technique
目前对燃料电池的研究越来越多,这主要是由于一些小分子化合物比如甲醇、乙醇等物质来源广泛,可以用在燃料电池中直接做燃料。但是甲醇有一定的挥发性和毒性,会对人身产生危害,而乙醇具有高能量密度,可以用于一些电子设备和电动汽车上,关于直接乙醇燃料电池的研究更受关注[1-5]。Pt是一种对乙醇氧化研究比较多的金属,但是乙醇的完全氧化反应是一个12电子的反应,在纯金属Pt上的反应缓慢而且它对乙醇氧化的最终产物大部分是乙酸,并不是CO2 [6-7],在乙醇的氧化过程中,会生成一些类CO的中间产物,会造成Pt催化剂中毒,催化活性会明显下降。 At present, there are more and more researches on fuel cells, mainly because some small molecular compounds such as methanol, ethanol and other substances have a wide range of sources, and can be used directly as fuel in fuel cells. However, methanol has certain volatility and toxicity, which will cause harm to the human body, while ethanol has high energy density and can be used in some electronic devices and electric vehicles. Research on direct ethanol fuel cells has attracted more attention [1-5] . Pt is a metal that has been studied more on the oxidation of ethanol, but the complete oxidation reaction of ethanol is a 12-electron reaction, the reaction on pure metal Pt is slow, and most of the final products of its oxidation of ethanol are acetic acid, not CO 2 [6-7] , in the oxidation process of ethanol, some CO-like intermediate products will be generated, which will cause Pt catalyst poisoning, and the catalytic activity will decrease significantly.
研究表明,在催化剂中加入氧化物会提高对乙醇的氧化能力,抵制CO中毒。Pang[8]用溶胶-凝胶法制备了SnO2-CNTs/Pt 催化剂,该催化剂在酸性溶液中对乙醇有很高的催化活性,SnO2的引入使得催化剂的长时间循环性能更好。Zhang[9]等合成了具有核壳结构(厚约2nm)的Pt/CNTSnO2催化剂,在酸性溶液中对乙醇的氧化电流是Pt/C 的1.57倍。B.RuizCamacho[10]研究发现在加入氧化物SnO2,TiO2,ZnO制备Pt/SnO2/C,Pt/TiO2/C和Pt/ZnO/C相对于Pt/C都有比较好的电催化性能,但是Pt/ZnO/C的催化稳定性不好。而且Pt本身的昂贵,储量有限,在实际应用中存在一定的局限性。比较而言Pd的价格相对便宜,储量丰富,用Pd代替Pt,可以降低醇类燃料电池阳极催化剂的成本.在碱性溶液中Pd/C相对于Pt/C对乙醇有更好的催化活性,稳定性和抗CO中毒能力[11]。 Studies have shown that adding oxides to the catalyst will improve the ability to oxidize ethanol and resist CO poisoning. Pang [8] prepared SnO 2 -CNTs/Pt catalyst by sol-gel method. The catalyst has high catalytic activity to ethanol in acidic solution. The introduction of SnO 2 makes the long-term cycle performance of the catalyst better. Zhang [9] et al. synthesized a Pt/CNTSnO 2 catalyst with a core-shell structure (thickness about 2nm), and the oxidation current of ethanol in acidic solution was 1.57 times that of Pt/C. B.RuizCamacho [10] found that adding oxides SnO 2 , TiO 2 , ZnO to prepare Pt/SnO 2 /C, Pt/TiO 2 /C and Pt/ZnO/C have better electricity than Pt/C Catalytic performance, but the catalytic stability of Pt/ZnO/C is not good. Moreover, Pt itself is expensive and its reserves are limited, so there are certain limitations in practical applications. In comparison, the price of Pd is relatively cheap and the reserves are abundant. Using Pd instead of Pt can reduce the cost of the anode catalyst for alcohol fuel cells. Compared with Pt/C in alkaline solution, Pd/C has better catalytic activity for ethanol, Stability and anti-CO poisoning ability [11] .
鉴于ZnO的催化活性,本发明制备了一种在碱性溶液中对乙醇有较好催化活性和稳定性的新型催化剂Pd/ZnO/C,传统的实验室制备Pt/ZnO/C催化剂所需的设备复杂,且产率低,本发明先合成氧化锌,原材料便宜,操作简单,且产率较高,再负载金属Pd粒径较小且分布均匀,与Pd/C催化剂相比,催化活性有明显提高。由于目前直接乙醇燃料电池研究有限,以及各个实验体系不同等原因,尚无本发明的类似报道。 In view of the catalytic activity of ZnO, the present invention has prepared a kind of novel catalyst Pd/ZnO/C that ethanol has good catalytic activity and stability in alkaline solution, and traditional laboratory preparation Pt/ZnO/C catalyst needs The equipment is complicated and the yield is low. The present invention first synthesizes zinc oxide, the raw material is cheap, the operation is simple, and the yield is high. The particle size of the loaded metal Pd is small and evenly distributed. Compared with the Pd/C catalyst, the catalytic activity is relatively high. Significantly improved. Due to the limited research on direct ethanol fuel cells at present and the different experimental systems, there is no similar report of the present invention.
参考文献 references
[1] Song SQ, Zhou WJ, Zhou ZH, Jiang LH, Sun GQ, Xin Q, et al.Direct ethanol PEM fuel cells:the case of platinum based anodes[J]. Int J Hydrogen Energy 2005;30:995-1001 [1] Song SQ, Zhou WJ, Zhou ZH, Jiang LH, Sun GQ, Xin Q, et al. Direct ethanol PEM fuel cells: the case of platinum based anodes[J]. Int J Hydrogen Energy 2005;30:995- 1001
[2] Lamy C, Rousseau S, Belgsir EM, Coutanceau C, Leger JM.Recent progress in the direct ethanol fuel cell: develo pment of new platinum -tin electrocatalysts[J]. Electrochim Acta 2004; 49:3901-3018 [2] Lamy C, Rousseau S, Belgsir EM, Coutanceau C, Leger JM.Recent progress in the direct ethanol fuel cell: development of new platinum -tin electrocatalysts[J]. Electrochim Acta 2004; 49:3901-3018
[3] Rousseau S, Coutanceau C, Lamy C. Direct ethanol fuel cell (DEFC): electrical performances and react ion products distribution under operating conditions with different platinum-based anodes[J]. J Power Sources 2006;158:18-24 [3] Rousseau S, Coutanceau C, Lamy C. Direct ethanol fuel cell (DEFC): electrical performances and reaction ion products distribution under operating conditions with different platinum-based anodes[J]. J Power Sources 2006-258:18
[4]Antolini E. Catalysts for direct ethanol fuel cells[J]. J. Power Sources 2007; 170: 1-12 [4]Antolini E. Catalysts for direct ethanol fuel cells[J]. J. Power Sources 2007; 170: 1-12
[5]E. Antolini,F. Colmati,E.R. Gonzalez.Ethanol oxidation on carbon supported (PtSn) alloy/SnO2 and (PtSnPd) alloy/SnO2 catalysts with a fixed Pt/SnO2 atomic ratio:Effect of the alloy phase characteristics[J].Journal of Power Sources 193 (2009) 555-561 [5] E. Antolini, F. Colmati, ER Gonzalez. Ethanol oxidation on carbon supported (PtSn) alloy/SnO 2 and (PtSnPd) alloy/SnO 2 catalysts with a fixed Pt/SnO 2 atomic ratio:Effect of the alloy phase characteristics[J]. Journal of Power Sources 193 (2009) 555-561
[6]H. Wang, Z. Jusys, R.J. Behm. Ethanol Electro oxidation on a Carbon-Supported Pt Catalyst: Reaction Kinetics and Product Yields[J]. J. Phys. Chem. B., 2004, 108, 19413-19424 [6]H. Wang, Z. Jusys, R.J. Behm. Ethanol Electro oxidation on a Carbon-Supported Pt Catalyst: Reaction Kinetics and Product Yields[J]. J. Phys. Chem. B., 2004, 108, 19413-19424
[7]G.A. Camara, T. Iwasita, Parallel pathways of ethanol oxidation: The effect of ethanol concentration[J]. Journal of Electroanalytical Chemistry.2005,578,315-321 [7] G.A. Camara, T. Iwasita, Parallel pathways of ethanol oxidation: The effect of ethanol concentration[J]. Journal of Electroanalytical Chemistry.2005,578,315-321
[8]H.L. Pang, J.P. Lu, J.H. Chen, C.T. Huang, B. Liu, X.H. Zhang.Preparation of SnO2-CNTs supported Pt catalysts and their electrocatalytic properties for ethanol oxidation [J].Electrochimica Acta 54 (2009) 2610-2615 [8]H.L. Pang, J.P. Lu, J.H. Chen, C.T. Huang, B. Liu, X.H. Zhang. Preparation of SnO2-CNTs supported Pt catalysts and their electrocatalytic properties for ethanol oxidation [J]. Electrochimica (261 Acta 54)
[9]Xinwei Zhang,Hong Zhu,Zhijun Guo, et al.Design and preparation of CNTSnO2 core-shell composites with thin shell and its application for ethanol oxidation[J].International Journal of Hydrogen Energy 35 (2010) 8841-8847 [9]Xinwei Zhang, Hong Zhu, Zhijun Guo, et al.Design and preparation of CNTSnO2 core-shell composites with thin shell and its application for ethanol oxidation[J].International Journal of Hydrogen Energy 35 (2010) 8841-8847
[10]B.RuizCamachoa, C. Moraisa,et al. Enhancing oxygen reduction reaction activity and stability of platinum via oxide-carbon composites[J]. Catalysis Today,2012,1-8 [10]B.RuizCamachoa, C. Moraisa, et al. Enhancing oxygen reduction reaction activity and stability of platinum via oxide-carbon composites[J]. Catalysis Today, 2012, 1-8
[11]Liang Ma, Deryn Chu, Rongrong Chen. Comparison of ethanol electro-oxidation on Pt/C and Pd/C catalysts in alkaline media[J]. International Journal of Hydrogen Energy,37(2012)11185-11194 [11]Liang Ma, Deryn Chu, Rongrong Chen. Comparison of ethanol electro-oxidation on Pt/C and Pd/C catalysts in alkaline media[J]. International Journal of Hydrogen Energy, 37(2012) 11185-11194
发明内容 Contents of the invention
本发明的目的之一是为了解决上述催化剂催化活性较低,稳定性较差等技术问题而提供一种具有高催化活性,稳定性和抗中毒能力的Pd/ZnO/C复合纳米催化剂。 One of the purposes of the present invention is to provide a Pd/ZnO/C composite nano-catalyst with high catalytic activity, stability and anti-poisoning ability in order to solve technical problems such as low catalytic activity of the above-mentioned catalyst and poor stability.
本发明的目的之二是提供上述的一种Pd/ZnO/C复合纳米催化剂的制备方法。 The second object of the present invention is to provide a method for preparing the above-mentioned Pd/ZnO/C composite nano-catalyst.
本发明的技术原理 Technical principle of the present invention
考虑到在碱性环境中Pd对乙醇的催化氧化具有比Pt更高的活性,在酸、碱介质中都有很好的稳定性,ZnO具有良好的电化学活性,水热稳定性,是一种性能优良的电催化剂和催化剂载体。把ZnO引入到乙醇催化氧化的Pd催化剂体系,制备成Pd/ZnO/C复合纳米催化剂,研究结果表明此催化剂对乙醇氧化反应具有很高的催化活性。 Considering that Pd has a higher activity than Pt in the catalytic oxidation of ethanol in an alkaline environment, and has good stability in acid and alkali media, ZnO has good electrochemical activity and hydrothermal stability, and is a A kind of electrocatalyst and catalyst carrier with excellent performance. Pd/ZnO/C composite nanocatalyst was prepared by introducing ZnO into the Pd catalyst system for the catalytic oxidation of ethanol. The research results showed that the catalyst had high catalytic activity for the oxidation of ethanol.
本发明的技术方案 Technical scheme of the present invention
一种Pd/ZnO/C复合纳米催化剂,其中Pd、ZnO、C按质量比计算,即Pd:ZnO:C为0.5:1:1的比例复合而成的纳米催化剂; A Pd/ZnO/C composite nano-catalyst, wherein Pd, ZnO, and C are calculated by mass ratio, that is, a nano-catalyst composited by a ratio of Pd:ZnO:C of 0.5:1:1;
其中所述的C为过200目筛的活性炭,所述的过200目筛的活性炭优选为Vulcan XC-72活性炭粉。 Wherein said C is the activated carbon that crosses 200 mesh sieves, and the described activated carbon that crosses 200 mesh sieves is preferably Vulcan XC-72 activated carbon powder.
上述的一种Pd/ZnO/C复合纳米催化剂的制备方法,具体包括如下步骤: The preparation method of above-mentioned a kind of Pd/ZnO/C composite nano-catalyst specifically comprises the following steps:
(1)、ZnO纳米颗粒制备 (1) Preparation of ZnO nanoparticles
将ZnSO4溶液、NaOH溶液和碳酸氢铵在搅拌条件下反应生成细小的碱式碳酸锌颗粒,再将碱式碳酸锌颗粒于80℃条件下干燥后,在400℃条件下进行煅烧,得到白色颗粒,即为ZnO粒子; React ZnSO 4 solution, NaOH solution and ammonium bicarbonate under stirring conditions to form fine basic zinc carbonate particles, then dry the basic zinc carbonate particles at 80°C, and then calcinate at 400°C to obtain white Particles are ZnO particles;
(2)、然后按照质量比为1:1,把过200目筛的活性炭与步骤(1)所得的ZnO纳米粒子在乙二醇水溶液中搅拌充分混合均匀,得到混合溶液; (2) Then according to the mass ratio of 1:1, stir the activated carbon passed through a 200-mesh sieve and the ZnO nanoparticles obtained in step (1) in an aqueous ethylene glycol solution and mix them well to obtain a mixed solution;
所述的乙二醇水溶液,即乙二醇和去离子水按体积比计算,即乙二醇:去离子水为1:3的比例组成的溶液; The ethylene glycol aqueous solution, that is, ethylene glycol and deionized water is calculated by volume ratio, that is, a solution composed of ethylene glycol: deionized water at a ratio of 1:3;
所述的预处理的Vulcan XC-72活性炭粉,即控制温度为90℃,将活性炭Vulcan XC-72在5mol/L的HNO3中强力搅拌回流5h,冷却至室温后过滤并水洗,控制温度在130℃真空干燥、研磨、过200目筛,即得预处理的Vulcan XC-72活性炭粉; The pretreated Vulcan XC-72 activated carbon powder, that is, the temperature is controlled at 90°C, the activated carbon Vulcan XC-72 is vigorously stirred and refluxed in 5mol/L HNO 3 for 5h, cooled to room temperature, filtered and washed with water, the temperature is controlled at Vacuum drying at 130°C, grinding, and passing through a 200-mesh sieve to obtain pretreated Vulcan XC-72 activated carbon powder;
(3)、用液相还原法负载纳米Pd颗粒; (3) Loading nano Pd particles by liquid phase reduction method;
步骤(2)得到的混合液中逐滴加入PdCl2水溶液,搅拌均匀后,加入含有两个结晶水的柠檬酸三钠作为稳定剂,控制金属Pd与柠檬酸三钠的摩尔比为1:5,超声震荡混合均匀,再用碱性溶液NaOH调节溶液的pH值至11,然后加入硼氢化钠作为还原剂,继续恒温反应3h,然后冷却至室温,抽虑洗涤至滤饼中无Cl-,控制温度为90℃下真空干燥,即得到黑色粉末状Pd/ZnO/C复合纳米催化剂,其中金属Pd的负载量为wt.20%; Add PdCl aqueous solution dropwise to the mixed solution obtained in step (2), stir evenly, add trisodium citrate containing two crystal waters as a stabilizer, and control the molar ratio of metal Pd to trisodium citrate to be 1:5 , and ultrasonically oscillate to mix evenly, then adjust the pH value of the solution to 11 with alkaline solution NaOH, then add sodium borohydride as a reducing agent, continue the constant temperature reaction for 3 hours, then cool to room temperature, filter and wash until there is no Cl - in the filter cake, Control the temperature at 90°C and vacuum dry to obtain a black powdery Pd/ZnO/C composite nanocatalyst, in which the metal Pd loading is wt.20%;
上述混合液中加入的PdCl2水溶液、柠檬酸三钠和硼氢化钠的量,按混合液中所含的Zn:PdCl2水溶液中所含的金属Pd:柠檬酸三钠:硼氢化钠的摩尔比为2.6:1:5:6。 The amount of PdCl2 aqueous solution, trisodium citrate and sodium borohydride added in the above mixed solution is based on the Zn contained in the mixed solution: the metal Pd contained in the PdCl2 aqueous solution: trisodium citrate: the mole of sodium borohydride The ratio is 2.6:1:5:6.
上述所得的一种Pd/ZnO/C复合纳米催化剂,对乙醇的氧化反应具有很高的催化活性。 The Pd/ZnO/C composite nano-catalyst obtained above has high catalytic activity for the oxidation reaction of ethanol.
本发明的有益效果 Beneficial effects of the present invention
本发明的一种Pd/ZnO/C复合纳米催化剂,由于含有ZnO,从而提高了Pd/ZnO/C复合纳米催化剂的抗中毒能力,Pd/ZnO/C复合纳米催化剂稳定性能更好。 The Pd/ZnO/C composite nano catalyst of the present invention contains ZnO, thereby improving the anti-poisoning ability of the Pd/ZnO/C composite nano catalyst, and the Pd/ZnO/C composite nano catalyst has better stability.
进一步,本发明的一种Pd/ZnO/C复合纳米催化剂,在碱性溶液中对乙醇有很好催化氧化性能。 Further, a Pd/ZnO/C composite nano-catalyst of the present invention has good catalytic oxidation performance for ethanol in alkaline solution.
综上所述,本发明的一种Pd/ZnO/C复合纳米催化剂在粒径分布,对乙醇的催化性能,以及稳定性方面都有更好的效果。 In summary, a Pd/ZnO/C composite nanocatalyst of the present invention has better effects in terms of particle size distribution, catalytic performance on ethanol, and stability. the
附图说明 Description of drawings
图1、Pd/ZnO/C复合纳米催化剂的TEM图; Figure 1. TEM images of Pd/ZnO/C composite nanocatalysts;
图2、Pd/ZnO/C复合纳米催化剂的XRD图; Figure 2. XRD pattern of Pd/ZnO/C composite nanocatalyst;
图3、Pd/ZnO/C复合纳米催化剂在1mol·L-1KOH溶液中的溶出伏安曲线; Figure 3. Stripping voltammetry curve of Pd/ZnO/C composite nanocatalyst in 1mol L -1 KOH solution;
图4、Pd/C催化剂与Pd/ZnO/C复合纳米催化剂分别在1mol/LCH3CH2OH和1mol/L KOH溶液中的循环伏安曲线; Figure 4. Cyclic voltammetry curves of Pd/C catalyst and Pd/ZnO/C composite nanocatalyst in 1mol/LCH 3 CH 2 OH and 1mol/L KOH solutions respectively;
图5、Pd/C催化剂与Pd/ZnO/C复合纳米催化剂在1M KOH+1M C2H5OH中时间电流曲线。 Fig. 5. Time-current curves of Pd/C catalyst and Pd/ZnO/C composite nanocatalyst in 1M KOH+1M C 2 H 5 OH.
具体实施方式 Detailed ways
下面通过具体的实施例并结合附图对本发明进一步阐述,但并不限制本发明。 The present invention will be further described below through specific embodiments in conjunction with the accompanying drawings, but the present invention is not limited.
X射线粉末衍射仪为德国Bruker D8-ADVANCE型,辐射源为CuK ( =0.15418nm),步长0.0167°,每步停留1s,扫描范围为20-90°; The X-ray powder diffractometer is a German Bruker D8-ADVANCE type, and the radiation source is CuK ( =0.15418nm), the step size is 0.0167°, each step stays for 1s, and the scanning range is 20-90°;
上海辰华仪器公司CHI660A电化学工作站; Shanghai Chenhua Instrument Company CHI660A Electrochemical Workstation;
本发明所用的试剂或原料的规格及生产厂家信息如下: The specifications and manufacturer's information of reagents or raw materials used in the present invention are as follows:
氯化钯(PdCl2,上海精细化工材料研究所,分析纯); Palladium chloride (PdCl 2 , Shanghai Institute of Fine Chemical Materials, analytically pure);
Vulcan XC-72(美国Cabot公司,98%);乙醇(江苏强盛功能化学股份有限公司,分析纯); Vulcan XC-72 (Cabot, USA, 98%); Ethanol (Jiangsu Qiangsheng Functional Chemistry Co., Ltd., analytically pure);
乙二醇(国药集团化学试剂有限公司,分析纯); Ethylene glycol (Sinopharm Chemical Reagent Co., Ltd., analytically pure);
氢氧化钠(上海化学试剂有限公司,分析纯); Sodium hydroxide (Shanghai Chemical Reagent Co., Ltd., analytically pure);
碳酸氢氨(上海骏惠化工有限公司,分析纯); Ammonium bicarbonate (Shanghai Junhui Chemical Co., Ltd., analytically pure);
七水合硫酸锌(南京化学试剂有限公司,分析纯); Zinc sulfate heptahydrate (Nanjing Chemical Reagent Co., Ltd., analytically pure);
Nafion溶液(5(wt)%,美国DuPont公司)。 Nafion solution (5 (wt)%, DuPont, USA).
实施例1Example 1
一种Pd/ZnO/C复合纳米催化剂的制备方法,具体步骤如下: A kind of preparation method of Pd/ZnO/C composite nano-catalyst, concrete steps are as follows:
(1)、ZnO纳米颗粒的制备(1) Preparation of ZnO nanoparticles
取1.0mol/LZnSO4溶液50ml,快速搅拌下滴加浓度为0.5mol/L的NaOH溶液10ml,滴加完毕后加入6g碳酸氢铵继续搅拌,此时原料呈半透明乳胶状,生成了细小的碱式碳酸锌颗粒,将碳酸锌颗粒放入烘箱中控制温度为80℃条件下干燥后,在400℃条件下进行煅烧1h,得到白色颗粒,即为ZnO纳米粒子; Get 50ml of 1.0mol/L ZnSO4 solution, add 10ml of NaOH solution with a concentration of 0.5mol/L dropwise under rapid stirring, add 6g of ammonium bicarbonate after the dropwise addition and continue stirring. Basic zinc carbonate particles, put the zinc carbonate particles in an oven to control the temperature at 80°C and dry them, then calcinate them at 400°C for 1 hour to obtain white particles, which are ZnO nanoparticles;
(2)、复合催化剂的制备(2), preparation of composite catalyst
按照质量比为1:1,把经过预处理的Vulcan XC-72活性炭粉与步骤(1)所得的ZnO纳米粒子共40mg加入到120ml由乙二醇和去离子水按体积比计算,即乙二醇:去离子水为1:3组成的乙二醇水溶液中,控制温度为60℃,利用磁力搅拌器强力搅拌充分混合均匀,得到混合液; According to the mass ratio of 1:1, add a total of 40mg of pretreated Vulcan XC-72 activated carbon powder and ZnO nanoparticles obtained in step (1) to 120ml by volume ratio of ethylene glycol and deionized water, that is, ethylene glycol : Deionized water is ethylene glycol aqueous solution with a composition of 1:3, the temperature is controlled at 60°C, and the magnetic stirrer is used to vigorously stir and mix well to obtain a mixed solution;
所述的预处理的Vulcan XC-72活性炭粉,即将Vulcan XC-72活性炭粉在5mol/L的HNO3,控制温度为90℃,强力搅拌5h,冷却至室温后过滤并水洗;再控制温度在130℃真空干燥6h,然后研磨并过200目筛,得到预处理的Vulcan XC-72活性炭粉; The pretreated Vulcan XC-72 activated carbon powder is to add Vulcan XC-72 activated carbon powder to 5mol/L HNO 3 , control the temperature at 90°C, stir vigorously for 5h, filter and wash with water after cooling to room temperature; then control the temperature at Vacuum dry at 130°C for 6 hours, then grind and pass through a 200-mesh sieve to obtain pretreated Vulcan XC-72 activated carbon powder;
(3)、用液相还原法负载纳米Pd颗粒 (3) Loading nano-Pd particles by liquid phase reduction method
步骤(2)得到的混合液中逐滴加入2mmol/L的PdCl2溶液46.99mL,搅拌1h后,加入138.18mg的含有两个结晶水的柠檬酸三钠作为稳定剂,即控制金属Pd与柠檬酸三钠的摩尔比为1:5,超声震荡30min,混合均匀,再用碱性溶液NaOH调节溶液的pH值至11,然后加入21.33mg的硼氢化钠作为还原剂,继续反应3h,然后冷却至室温,抽虑洗涤至滤饼中无Cl-,控制温度为90℃下真空干燥12h,即得到黑色粉末状Pd/ZnO/C复合纳米催化剂,金属Pd的负载量为wt.20%。 Add 46.99 mL of 2 mmol/L PdCl 2 solution dropwise to the mixture obtained in step (2), stir for 1 hour, then add 138.18 mg of trisodium citrate containing two crystal waters as a stabilizer, that is, to control the interaction between metal Pd and lemon The molar ratio of trisodium acid is 1:5, ultrasonically oscillate for 30 minutes, mix well, then adjust the pH value of the solution to 11 with alkaline solution NaOH, then add 21.33 mg of sodium borohydride as a reducing agent, continue the reaction for 3 hours, and then cool to room temperature, filter and wash until there is no Cl - in the filter cake, and vacuum-dry at a temperature of 90°C for 12 hours to obtain a black powdery Pd/ZnO/C composite nanocatalyst with a metal Pd loading of wt.20%.
利用透射电子显微镜对上述所得的Pd/ZnO/C复合纳米催化剂进行扫描,所得的TEM图片如图1所示,从图1中可以看出Pd均匀分散在催化剂中,所作的催化剂有很好的分散性,Pd粒径大小约为2-4nm。 The Pd/ZnO/C composite nano-catalyst obtained above is scanned by a transmission electron microscope, and the resulting TEM picture is shown in Figure 1. From Figure 1, it can be seen that Pd is evenly dispersed in the catalyst, and the catalyst made has a good Dispersion, Pd particle size is about 2-4nm.
利用X射线粉末衍射仪对上述所得的Pd/ZnO/C复合纳米催化剂进行XRD扫描,所用的X射线粉末衍射仪为德国Bruker D8-ADVANCE型,辐射源为CuK (=0.15418nm),步长0.0167°,每步停留1s,扫描范围为20-90°,获得Pd/ZnO/C复合纳米催化剂的XRD图如图2所示,并将图2所得的XRD图与Pd的标准卡片(JCPDS, No. 65-6174)Pd的特征衍射峰出现在40.11°(111),46.65°(200),68.11°(220),82.03°(311),86.60°(222)位置,同时对比ZnO的标准卡片(JCPDS, No. 65-3358),ZnO衍射峰出现在82.09°(112),86.54°(201),由此表明此制备方法成功制备出了含有Pd和ZnO的复合纳米催化剂。 Utilize X-ray powder diffractometer to carry out XRD scanning to the Pd/ZnO/C composite nano-catalyst of above-mentioned gain, used X-ray powder diffractometer is German Bruker D8-ADVANCE type, radiation source is CuK ( =0.15418nm), the step length is 0.0167°, each step stays for 1s, and the scanning range is 20-90°. The XRD pattern of the Pd/ZnO/C composite nanocatalyst is shown in Figure 2, and the XRD pattern obtained in Figure 2 is compared with Pd's standard card (JCPDS, No. 65-6174) Pd's characteristic diffraction peaks appear at 40.11° (111), 46.65° (200), 68.11° (220), 82.03° (311), 86.60° (222) , and compared with the standard card of ZnO (JCPDS, No. 65-3358), the diffraction peaks of ZnO appear at 82.09° (112), 86.54° (201), which shows that this preparation method successfully prepared a composite containing Pd and ZnO nanocatalyst.
将上述所得的Pd/ZnO/C复合纳米催化剂制备催化电极,具体步骤如下:The Pd/ZnO/C composite nano-catalyst obtained above is prepared as a catalytic electrode, and the specific steps are as follows:
称取一定量上述制备的Pd/ZnO/C复合纳米催化剂,按质量比计算,即Pd/ZnO/C复合纳米催化剂:去离子水:乙醇:5% Nafion溶液为1:160:32:22的比例将Pd/ZnO/C复合纳米催化剂与去离子水、乙醇和5%Nafion溶液混和,超声震荡30min,得到黑色墨水状Pd/ZnO/C复合纳米催化剂混合溶液,用移液器量取4μl的Pd/ZnO/C复合纳米催化剂混合溶液,覆于玻碳电极表面,自然晾干后,电极制作完成,即得到覆着有Pd/ZnO/C复合纳米催化剂的催化电极。 Weigh a certain amount of Pd/ZnO/C composite nano-catalyst prepared above, and calculate by mass ratio, that is, Pd/ZnO/C composite nano-catalyst: deionized water: ethanol: 5% Nafion solution is 1:160:32:22 Mix the Pd/ZnO/C composite nanocatalyst with deionized water, ethanol and 5% Nafion solution, and oscillate ultrasonically for 30 minutes to obtain a black ink-like Pd/ZnO/C composite nanocatalyst mixed solution. Use a pipette to measure 4 μl of Pd /ZnO/C composite nano-catalyst mixed solution, covering the surface of the glassy carbon electrode, after natural drying, the electrode is fabricated, and the catalytic electrode covered with Pd/ZnO/C composite nano-catalyst is obtained.
所述的玻碳(GC)电极(d=3mm),使用前用0.3 m的Al2O3粉末在麂皮上磨至镜面,再分别用去离子水和无水乙醇超声洗涤。 For the glassy carbon (GC) electrode (d=3mm), use 0.3 The Al 2 O 3 powder of m was ground on suede to a mirror surface, and then ultrasonically washed with deionized water and absolute ethanol, respectively.
上述所得的Pd/ZnO/C复合纳米催化剂的催化性质表征Characterization of Catalytic Properties of the Pd/ZnO/C Composite Nanocatalysts Obtained Above
将制备好的具有Pd/ZnO/C复合纳米催化剂的催化电极作为工作电极,以饱和甘汞电极(SCE)为参比电极,金属铂电极为辅助电极组成三电极测试系统,在CHI660A上进行循环伏安测试和时间电流曲线测试。 The prepared catalytic electrode with Pd/ZnO/C composite nano-catalyst was used as the working electrode, the saturated calomel electrode (SCE) was used as the reference electrode, and the metal platinum electrode was used as the auxiliary electrode to form a three-electrode test system, which was cycled on CHI660A Volt-ampere test and time-current curve test.
首先测定Pd/ZnO/C复合纳米催化剂在1mol·L-1KOH溶液中的溶出伏安曲线如图3所示,从图3中可以看出在-0.5V出现了氢的吸附峰,表明Pd/ZnO/C复合纳米催化剂有一定的活性比表面积。 Firstly, the stripping voltammetry curve of the Pd/ZnO/C composite nanocatalyst in 1mol L -1 KOH solution is measured, as shown in Figure 3. From Figure 3, it can be seen that there is a hydrogen adsorption peak at -0.5V, indicating that Pd /ZnO/C composite nanocatalyst has a certain active specific surface area.
进一步测定相同条件制备的Pd/C催化剂与Pd/ZnO/C复合纳米催化剂分别在1mol/LCH3CH2OH和1mol/L KOH溶液中的循环伏安曲线如图4所示,从图4上可以看出,Pd/ZnO/C复合纳米催化剂的催化性能远远高于Pd/C催化剂,Pd/ZnO/C复合纳米催化剂在正扫过程中,在很低的电位下,约为-0.6V(vs.SCE),乙醇就开始发生催化氧化,在-0.2 V时达到最大值,其峰电流密度约85mA/cm2;而此时Pd/C催化剂的峰电流密度仅为28.8mA/cm2,添加ZnO,使其电流密度增加了2.95倍。反向扫描时,因Pd/ZnO/C复合纳米催化剂中的Pd又重新转变为活性Pd原子,又对吸附在其上的乙醇进行催化氧化,其氧化峰在-0.40 V达到最大值,催化电流达60mA/cm2,从图4中可以看出,Pd/C催化剂的催化活性明显低于Pd/ZnO/C复合纳米催化剂。 The cyclic voltammetry curves of the Pd/C catalyst and Pd/ZnO/C composite nanocatalyst prepared under the same conditions were further measured in 1mol/LCH 3 CH 2 OH and 1mol/L KOH solutions respectively, as shown in Figure 4, from Figure 4 It can be seen that the catalytic performance of the Pd/ZnO/C composite nanocatalyst is much higher than that of the Pd/C catalyst, and the Pd/ZnO/C composite nanocatalyst is about -0.6V at a very low potential during the positive sweep process. (vs.SCE), ethanol begins to catalyze oxidation, reaching the maximum at -0.2 V, and its peak current density is about 85mA/cm 2 ; at this time, the peak current density of Pd/C catalyst is only 28.8mA/cm 2 , adding ZnO, the current density increased by 2.95 times. In the reverse scanning, because the Pd in the Pd/ZnO/C composite nanocatalyst is transformed into active Pd atoms again, the ethanol adsorbed on it is catalyzed and oxidized, and the oxidation peak reaches the maximum value at -0.40 V, and the catalytic current As can be seen from Figure 4 , the catalytic activity of the Pd/C catalyst is significantly lower than that of the Pd/ZnO/C composite nanocatalyst.
进一步测定Pd/C催化剂与Pd/ZnO/C复合纳米催化剂在1M KOH+1M C2H5OH中时间电流曲线如图5所示,从图5中可以看出随着反应时间的延长,Pd/C催化剂与Pd/ZnO/C复合纳米催化剂对乙醇氧化峰电流密度均有下降,但是Pd/C催化剂下降的速度更快,电流趋于稳定状态后,Pd/ZnO/C复合纳米催化剂的电流密度的大小为0.96 mA/cm2,Pd/C催化剂的电流密度大小为0.73 mA/cm2。随时间延长,乙醇氧化的中间产物会使催化剂中毒,活性降低,但是Pd/ZnO/C复合纳米催化剂的衰减幅度小,说明加入ZnO提高了Pd/ZnO/C复合纳米催化剂的抗中毒能力,Pd/ZnO/C复合纳米催化剂稳定性能更好。 Further measurement of the time-current curves of Pd/C catalyst and Pd/ZnO/C composite nano-catalyst in 1M KOH+1M C 2 H 5 OH is shown in Figure 5. It can be seen from Figure 5 that with the prolongation of the reaction time, the Pd /C catalyst and Pd/ZnO/C composite nanocatalyst have a decrease in the peak current density of ethanol oxidation, but the Pd/C catalyst declines faster. The magnitude of the density is 0.96 mA/cm 2 , and the magnitude of the current density of the Pd/C catalyst is 0.73 mA/cm 2 . Over time, the intermediate product of ethanol oxidation will poison the catalyst and reduce its activity, but the attenuation of the Pd/ZnO/C composite nanocatalyst is small, indicating that the addition of ZnO improves the anti-poisoning ability of the Pd/ZnO/C composite nanocatalyst. /ZnO/C composite nanocatalysts have better stability.
上述内容仅为本发明构思下的基本说明,而依据本发明的技术方案所作的任何等效变换,均应属于本发明的保护范围。 The above content is only a basic description of the concept of the present invention, and any equivalent transformation made according to the technical solution of the present invention shall belong to the protection scope of the present invention.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210367268XA CN102861576A (en) | 2012-09-27 | 2012-09-27 | Pd/ZnO/C composite nano catalyst and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210367268XA CN102861576A (en) | 2012-09-27 | 2012-09-27 | Pd/ZnO/C composite nano catalyst and preparation method thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102861576A true CN102861576A (en) | 2013-01-09 |
Family
ID=47440864
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210367268XA Pending CN102861576A (en) | 2012-09-27 | 2012-09-27 | Pd/ZnO/C composite nano catalyst and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102861576A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104998642A (en) * | 2015-07-23 | 2015-10-28 | 上海电力学院 | Preparation method of Pd-MnO2/GNRs anode catalyst for alcohol fuel cell |
CN108671628A (en) * | 2018-05-08 | 2018-10-19 | 重庆鑫泽环保设备有限公司 | Filter fiber in waste gas treatment equipment and preparation method thereof |
CN115011109A (en) * | 2022-07-26 | 2022-09-06 | 王卡 | Antibacterial platinum photocatalyst negative ion activated carbon filter cotton and preparation method thereof |
CN115893473A (en) * | 2022-11-09 | 2023-04-04 | 福州大学 | Alcohol gas-sensitive material based on ZnO and activated carbon composite, and preparation method and application thereof |
CN116058385A (en) * | 2022-11-18 | 2023-05-05 | 辽宁大学 | A palladium-zinc oxide nano-enzyme material with dual enzyme activity and its preparation method and application |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070204870A1 (en) * | 2006-02-27 | 2007-09-06 | Sarojini Deevi | Catalysts to reduce carbon monoxide such as in the mainstream smoke of a cigarette |
CN102544531A (en) * | 2012-03-05 | 2012-07-04 | 上海电力学院 | Pd/TiO2/C composite nano-catalyst, and preparation method and application thereof |
-
2012
- 2012-09-27 CN CN201210367268XA patent/CN102861576A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070204870A1 (en) * | 2006-02-27 | 2007-09-06 | Sarojini Deevi | Catalysts to reduce carbon monoxide such as in the mainstream smoke of a cigarette |
CN102544531A (en) * | 2012-03-05 | 2012-07-04 | 上海电力学院 | Pd/TiO2/C composite nano-catalyst, and preparation method and application thereof |
Non-Patent Citations (2)
Title |
---|
《燃料化学学报》 20110228 赵红晓等 "Pt-ZnO/C复合材料的合成及对醇类催化活性的研究" 摘要,第142页右栏第1段 1-5 第39卷, 第2期 * |
赵红晓等: ""Pt-ZnO/C复合材料的合成及对醇类催化活性的研究"", 《燃料化学学报》, vol. 39, no. 2, 28 February 2011 (2011-02-28), pages 142 - 1 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104998642A (en) * | 2015-07-23 | 2015-10-28 | 上海电力学院 | Preparation method of Pd-MnO2/GNRs anode catalyst for alcohol fuel cell |
CN108671628A (en) * | 2018-05-08 | 2018-10-19 | 重庆鑫泽环保设备有限公司 | Filter fiber in waste gas treatment equipment and preparation method thereof |
CN108671628B (en) * | 2018-05-08 | 2020-08-28 | 重庆鑫泽环保设备有限公司 | Filter fiber in waste gas treatment equipment and preparation method thereof |
CN115011109A (en) * | 2022-07-26 | 2022-09-06 | 王卡 | Antibacterial platinum photocatalyst negative ion activated carbon filter cotton and preparation method thereof |
CN115011109B (en) * | 2022-07-26 | 2023-11-14 | 王卡 | Preparation method of antibacterial platinum photocatalyst anion activated carbon filter cotton |
CN115893473A (en) * | 2022-11-09 | 2023-04-04 | 福州大学 | Alcohol gas-sensitive material based on ZnO and activated carbon composite, and preparation method and application thereof |
CN116058385A (en) * | 2022-11-18 | 2023-05-05 | 辽宁大学 | A palladium-zinc oxide nano-enzyme material with dual enzyme activity and its preparation method and application |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Liu et al. | Bifunctional carbon-based cathode catalysts for zinc-air battery: A review | |
Jung et al. | Doped lanthanum nickelates with a layered perovskite structure as bifunctional cathode catalysts for rechargeable metal–air batteries | |
Liu et al. | Preparation of Pd/MnO2-reduced graphene oxide nanocomposite for methanol electro-oxidation in alkaline media | |
Lv et al. | Nano-boron carbide supported platinum catalysts with much enhanced methanol oxidation activity and CO tolerance | |
CN108963282A (en) | A kind of fuel cell carbon carried platinum-based catalyst and the preparation method and application thereof of solvent-thermal method reduction | |
CN111001428B (en) | A kind of metal-free carbon-based electrocatalyst and preparation method and application | |
Yu et al. | Facile route to achieve bifunctional electrocatalysts for oxygen reduction and evolution reactions derived from CeO 2 encapsulated by the zeolitic imidazolate framework-67 | |
CN101161341A (en) | A method for preparing direct methanol fuel cell anode multicomponent catalyst | |
Wang et al. | Low-temperature plasma-assisted synthesis of iron and nitrogen co-doped CoFeP-N nanowires for high-efficiency electrocatalytic water splitting | |
Zhao et al. | Platinum nanoparticles supported on epitaxial TiC/nanodiamond as an electrocatalyst with enhanced durability for fuel cells | |
CN113270597B (en) | A kind of C3N4-coated carbon nanotube-supported NiFe bifunctional oxygen electrocatalyst and preparation method thereof | |
CN102861576A (en) | Pd/ZnO/C composite nano catalyst and preparation method thereof | |
CN110625135A (en) | An Efficient and Simple Method for Synthesizing Ru Nanocrystals with Different Shapes | |
Wang et al. | Pt decorated PdFe/C: extremely high electrocatalytic activity for methanol oxidation | |
Shixuan et al. | Oxygen reduction activity of a Pt-N4 single-atom catalyst prepared by electrochemical deposition and its bioelectrochemical application | |
CN103191757B (en) | PdNiW/C ternary alloy nano catalyst and preparation method thereof | |
Salarizadeh et al. | Comparison of methanol oxidation reaction process for NiCo2O4/X (X= rGO, MWCNTs, HCNs) nanocatalyst | |
Zhang et al. | Efficiently catalyzed sea urchin-like mixed phase SmMn2O5/MnO2 for oxygen reduction reaction in zinc-air battery | |
Qin et al. | Multi-functional layered double hydroxides supported by nanoporous gold toward overall hydrazine splitting | |
CN102806079B (en) | A kind of preparation method of Pd/SnO2/C composite nano catalyst | |
da Silva et al. | Electrochemical and fuel cell evaluation of PtIr/C electrocatalysts for ethanol electrooxidation in alkaline medium | |
Xie et al. | A NiMOF integrated with conductive materials for efficient bifunctional electrocatalysis of urea oxidation and oxygen evolution reactions | |
CN102881917B (en) | A kind of PdMg/C nanocatalyst and preparation method thereof | |
Li et al. | Mesoporous FeCo2O4 nanosheet-supported Pt for oxygen reduction and oxygen evolution reaction bi-functional catalytic performance | |
Qian et al. | Rational Design of Goethite-Sulfide Nanowire Heterojunctions for High Current Density Water Splitting |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130109 |