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Acta Metall Sin  2016, Vol. 52 Issue (4): 505-512    DOI: 10.11900/0412.1961.2015.00531
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PREPARATION OF Ni-Pt/La2O3 CATALYST AND ITS KINETICS STUDY OF HYDROUS HYDRAZINE FOR HYDROGEN GENERATION
Yujie ZHONG1,Hongbin DAI2(),Ping WANG2
1 Institute of Metal Research, Chinese Academy of Sciences, Shenyang 110016, China
2 Key Laboratory of Advanced Energy Storage Materials of Guangdong Province, School of Materials Science and Engineering, South China University of Technology, Guangzhou 510641, China
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Yujie ZHONG,Hongbin DAI,Ping WANG. PREPARATION OF Ni-Pt/La2O3 CATALYST AND ITS KINETICS STUDY OF HYDROUS HYDRAZINE FOR HYDROGEN GENERATION. Acta Metall Sin, 2016, 52(4): 505-512.

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Abstract  

Safe and efficient hydrogen storage remains a grand challenge in the widespread implementation of hydrogen fuel cell technology. Recently, chemical hydrogen storage has emerged as a promising alternative for vehicular and portable applications. A number of hydrogen-rich materials have been experimentally demonstrated to deliver large amounts of hydrogen under mild conditions with controllable kinetics. Among these materials of interest, hydrous hydrazine (N2H4H2O) is a promising but yet not fully explored candidate. The development of highly efficient catalyst and its reaction kinetics law are the key issues of N2H4H2O-based hydrogen generation (HG) systems. Herein, a supported Ni-Pt/La2O3 catalyst was prepared by a combination of co-precipitation and galvanic replacement methods. Via optimizing preparing processes, the developed catalyst enabled a complete decomposition of N2H4H2O to generate H2 at a reaction rate of 340 h-1 at 323 K, which outperforms most reported N2H4H2O decomposition catalysts. Phase/structural analyses by XRD, TEM and XPS were carried out to gain insight into the catalytic performance of the Ni-Pt/La2O3 catalyst. In addition, the effects of temperature, concentration of N2H4H2O and NaOH, and amount of catalyst on the N2H4H2O decomposition were investigated over the Ni-Pt/La2O3 catalyst. The kinetic rate equation may be represented by the expression: r = -d[N2H4H2O]/dt = 2435exp(-51.53/(RT))[N2H4H2O]0.3[NaOH]0(0.12)[Ni]1.03. The obtained results should lay the experimental and theoretical foundation for developing practical application of N2H4H2O-based HG system.

Key words:  hydrous hydrazine      hydrogen generation      catalyst      reaction kinetics     
Received:  15 October 2015     
Fund: Supported by National Outstanding Youth Science Foundation of China (No.51125003) and National Natural Science Foundation of China (No.51471168)

URL: 

https://www.ams.org.cn/EN/10.11900/0412.1961.2015.00531     OR     https://www.ams.org.cn/EN/Y2016/V52/I4/505

Fig.1  Schematic of preparation of Ni-Pt/La2O3 catalyst using a combination of co-precipitation and galvanic replacement methods
Fig.2  XRD spectra of Ni/La2O3, Ni90Pt10@Pt/La(OH)3 and Ni-Pt/La2O3 catalyst samples
Fig.3  TEM (a), HRTEM (b), HAADF-STEM (c) images of the Ni90Pt10/La2O3 (Pt∶Ni=1∶30) catalyst and corresponding EDS analysis result along the direction indicated by the black line in Fig.3c (d)
Fig.4  XPS results of Ni/La2O3, Pt/La2O3 and Ni90Pt10/La2O3 (Pt∶Ni=1∶30) catalysts
Method Catalyst sample Reaction rate
h-1
H2 selectivity
%
Co-precipitation
Ni/La2O3 6 72
Ni90Pt10/La2O3 200 96
Pt/La2O3 0 0
Co-precipitation/
replacement

Ni90Pt10@Pt/La(OH)3 (Pt : Ni=1 : 30) 185 94
Ni90Pt10/La2O3 (Pt : Ni=1 : 40) 222 99
Ni90Pt10/La2O3 (Pt : Ni=1 : 35) 280 100
Ni90Pt10/La2O3 (Pt : Ni=1 : 30) 340 100
Ni90Pt10/La2O3 (Pt : Ni=1 : 25) 340 100
Ni90Pt10/La2O3 (Pt : Ni=1 : 20) 340 100
Table 1  Comparison of catalytic performance between the catalysts using co-precipiation and co-precipiation/replacement methods
Fig.5  Effect of reaction temperature on N2H4H2O decomposition in the presence of Ni90Pt10/La2O3 (Pt∶Ni=1∶30) catalyst (a) and Arrhenius plot for determination of the apparent activation energy Ea (Ea=6.19×8.314=51.53 kJ/ mol) (b) (Y—molar ratio of N2+H2 and N2H4, r—catalytic reaction rate, T—catalytic reaction temperature)
Fig.6  Effect of N2H4H2O concentration on N2H4H2O decomposition in the presence of Ni90Pt10/La2O3 (Pt∶Ni=1∶30) catalyst (a) and a plot of lnr vs ln[N2H4H2O] ([N2H4H2O]: 0.1~0.9 mol/L) (b)
Fig.7  Effect of NaOH concentration on N2H4H2O decomposition in the presence of Ni90Pt10/La2O3 (Pt∶Ni=1∶30) catalyst (a) and a plot of lnr vs ln[NaOH] ([NaOH]: 0.05~0.3 mol/L) (b)
Fig.8  Effect of catalyst (Ni) amount on N2H4H2O decomposition in the presence of Ni90Pt10/La2O3 (Pt∶Ni=1∶30) catalyst (a) and a plot of lnr vs ln[Ni] ([Ni]: 0.1’0.3 mol/L) (b)
[1] Wang P, Kang X D.Dalton Trans, 2008; 40: 5400
[2] Zhu Q L, Xu Q.Energy Environ Sci, 2015; 8: 478
[3] Demirci U B, Miele P.Energy Environ Sci, 2009; 2: 627
[4] Cho S J, Lee J, Lee Y S, Kim D P.Catal Lett, 2006; 109: 3
[5] Singh S K, Zhang X B, Xu Q.J Am Chem Soc, 2009; 131: 9894
[6] He L, Huang Y Q, Wang A Q, Wang X D, Zhang T.AIChE J, 2013; 59: 4297
[7] He L, Liang B L, Li L, Yang X F, Huang Y Q, Wang A Q, Wang X D, Zhang T.ACS Catal, 2015; 5: 1623
[8] He L, Huang Y Q, Wang X D, Chen X W, Delgado J J, Zhang T.Angew Chem Int Ed, 2012; 51: 6191
[9] Singh S K, Xu Q.J Am Chem Soc, 2009; 131: 18032
[10] He L, Huang Y Q, Wang A Q, Lu Y, Liu X Y, Chen X W, Delgado J J, Wang X D, Zhang T.J Catal, 2013; 298: 1
[11] Wen L, Du X Q, Su J, Luo W, Cai P, Cheng G Z.Dalton Trans, 2015; 13: 6212
[12] Singh S K, Singh A K, Aranishi K, Xu Q.J Am Chem Soc, 2011; 133: 19638
[13] Singh S K, Xu Q.Chem Commun, 2010; 46: 6545
[14] Singh A K, Xu Q.ChemCatChem, 2013; 5: 3000
[15] Singh A K, Xu Q.Int J Hydrogen Energy, 2014; 39: 9128
[16] Zhang J J, Kang Q, Yang Z H, Dai H B, Zhuang D W, Wang P.J Mater Chem, 2013; 1A: 11623
[17] Wang H L, Yan J M, Wang Z L, O S I, Jiang Q.J Mater Chem, 2013; 1A: 14957
[18] Wang H L, Yan J M, Li S J, Zhang X W, Jiang Q.J Mater Chem, 2015; 3A: 121
[19] Singh S K, Lu Z H, Xu Q.Eur J Inorg Chem, 2011; (14): 2232
[20] Singh S K, Iizuka Y, Xu Q.Int J Hydrogen Energy, 2011; 36: 11794
[21] Cao N, Su J, Luo W, Cheng G Z.Int J Hydrogen Energy, 2014; 39: 9726
[22] Cao N, Yang L, Du C, Su J, Luo W, Cheng G Z.J Mater Chem, 2014; 2A: 14344
[23] Jiang Y Y, Kang Q, Zhang J J, Dai H B, Wang P.J Power Sources, 2015; 273: 554
[24] Jiang Y Y, Dai H B, Zhong Y J, Chen D M, Wang P.Chem Eur J, 2015; 21: 15439
[25] Zhong Y J, Dai H B, Jiang Y Y, Chen D M, Zhu M, Sun L X, Wang P.J Power Sources, 2015; 300: 294
[26] Wang J, Zhang X B, Wang Z L, Wang L M, Zhang Y.Energy Environ Sci, 2012; 5: 6885
[27] Siegmann H C, Schlapbach L, Brundle C R.Phys Rev Lett, 1978; 40: 972
[28] Nikolla E, Schwank J, Linic S.J Am Chem Soc, 2009; 131: 2747
[29] Holewinski A, Xin H L, Nikolla E, Linic S.Curr Opin Chem Eng, 2013; 2: 312
[30] Zhang Q L, Wu Y, Sun X L, Ortega J.Ind Eng Chem Res, 2007; 46: 1120
[31] Zhang J S, Delgass W N, Fisher T S, Gore J P.J Power Sources, 2007; 164: 772
[32] Zhao B, Song J, Ran R, Shao Z P.Int J Hydrogen Energy, 2012; 37: 1133
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