Cu-Ni Nanocatalysts in Mesoporous MCM-41 and TiO2 to Produce Hydrogen for Fuel Cells via Steam Reforming Reactions

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Abstract:

We have synthesized mesoporous SiO2 (MCM-41) and TiO2 encapsulated bimetallic Cu-Ni nanocatalysts using an optimized one-pot hydrothermal procedure. The catalysts were characterized using BET, XRD, TGA-DSC and HRTEM techniques. While bimetallic Cu-Ni/MCM-41catalysts have high surface area- 634-1000 m2/g, Cu-Ni/TiO2 yields surface area of 250-350 m2/g depending on the metal loading (5-10 wt%). The XRD studies confirmed a long range ordered structure in Cu-Ni/MCM-41 and the presence of the catalytically active anatase phase in the crystalline Cu-Ni/TiO2. The results from HRTEM studies were consistent with the mesoporosity of both supports. These catalysts were tested for methanol conversion and H2/CO selectivity via steam reforming of methanol (SRM) reactions in a fixed bed reactor. There is a distinct difference in the performance of these two supports. Bimetallic 3.33%Cu6.67%Ni/TiO2 catalyst showed an impressive 99% H2 selectivity at as low as 150°C and a maximum conversion of 92% at 250 °C but 3.33%Cu6.67%Ni/MCM-41 catalyst did not show any H2 selectivity at 150°C and only ~12% conversion at 250°C. The effect of each support and relative metal loadings on the activity and selectivity of the SRM reaction products at different temperatures is discussed.

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[1] Shriver & Atkins, Inorganic Chemistry, fourth ed., W. H. Freeman and Company, New York, 2006, 170, 702.

Google Scholar

[2] S. Yong, C. Ooi, et al, Review of methanol reforming-Cu-based catalysts, surface reaction mechanisms, and reaction schemes, Int. J. Hydrogen Energy, (2013), 9541–9552.

DOI: 10.1016/j.ijhydene.2013.03.023

Google Scholar

[3] J. Abolfazl, M.A.A. Seyed, B. Bahamin, A.J. Moradian, Enhancement in thermal and hydothermal stabilities of novel mesoporous MCM, J. Porous Mater (2012), 19, 979- 988.

DOI: 10.1007/s10934-011-9556-8

Google Scholar

[4] P. Lo´pez, G. Mondrago-Galicia, M.E. Espinosa-Pesqueira, D. Mendoza-Ana. Hydrogen production from oxidative steam reforming of methanol: Effect of the Cu and Ni impregnation on ZrO2 and their molecular simulation studies Int. J. Hydrogen Energy, (2012).

DOI: 10.1016/j.ijhydene.2012.02.105

Google Scholar

[5] S. Sá, H. Silva, L. Brandão, J.M. Sousa, A. Mendes, Catalysts for methanol steam reforming- A review, App. Catalysis B: Environmental (2010), 99, 43-57.

DOI: 10.1016/j.apcatb.2010.06.015

Google Scholar

[6] M. Khzouz, J. Wood, B. Pollet, W. Bujalski, Characterization and activity test of Commercial Ni/Al2O3, Cu/ZnO/Al2O3 and prepared Ni–Cu/Al2O3 catalysts for hydrogen production from methane and methanol fuels, Int. J. Hydrogen Energy, (2013).

DOI: 10.1016/j.ijhydene.2012.07.026

Google Scholar

[7] A. Bshish, Z. Yaakob, B. Narayanan, B.; Ramakrishnan, R.; Ebshish, A. Steam-reforming of ethanol for hydrogen production. Chem. Papers. (2011), 65, 251-266.

DOI: 10.2478/s11696-010-0100-0

Google Scholar

[8] Y. Yang, J. Ma, et al, Production of hydrogen by steam reforming of ethanol over a Ni/ZnO catalyst. Int. J. Hydrogen Energy, (2006), 31, 877-882.

DOI: 10.1016/j.ijhydene.2005.06.029

Google Scholar

[9] G. Gabriella, R. Paola, A. L. Mattia, Cobalt-based nanoparticles as catalysts for low temperature hydrogen production by ethanol steam reforming. Int. J. Hydrogen Energy, (2013), 38, 82-91.

DOI: 10.1016/j.ijhydene.2012.10.054

Google Scholar

[10] V. Nichelea, M. Signorettoa, F. Menegazzoa, Glycerol steam reforming for hydrogen production : Design of Ni supported catalysts, App. Catalysis B: Environmental, ( 2012), 225 - 232.

DOI: 10.1016/j.apcatb.2011.10.003

Google Scholar

[11] Kosaraju, K., Rahman, A., Duncan, M., Tatineni, B., Basova, Y., Deshmane, V., Abrokwah, R., Hosseinnezhad, S., King, J., and Ilias, S. Future Energy, Environment, and Materials, (2014), 88, 337.

DOI: 10.2495/feem130401

Google Scholar

[12] B. Tatineni, S. Islam, Y. Basova, A. Rahman, et al, Development of Mesoporous Silica Encapsulated Pd-Ni Nanocatalyst for hydrogen production, ACS Symposium series (2011), 177-190.

DOI: 10.1021/bk-2011-1088.ch009

Google Scholar