A comparative study of ZrO2, Y2O3 and Sm2O3 promoted Ni/SBA-15 catalysts for evaluation of CO2/methane reforming performance

被引:68
作者
Taherian, Zahra [1 ]
Yousefpour, Mardali [1 ]
Tajally, Mohammad [1 ]
Khoshandam, Behnam [2 ]
机构
[1] Semnan Univ, Fac Mat & Met Engn, Semnan, Iran
[2] Semnan Univ, Oil Gas & Chem Engn Dept, Semnan, Iran
关键词
Dry reforming of methane; Catalyst activity; Samaria; Zirconia; Yttria; Nickel catalyst; Promoter; ALKALINE-EARTH PROMOTERS; SYNGAS PRODUCTION; MESOPOROUS SILICA; NICKEL-CATALYSTS; NI/GAMMA-AL2O3; CATALYSTS; COKE FORMATION; METHANE; NI; SUPPORT; SURFACE;
D O I
10.1016/j.ijhydene.2017.05.095
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Ni-based/SBA-15 catalysts, were promoted by 3wt% of samaria (Sm2O3), Yttria (Y2O3) and Zirconia (ZrO2), by two-solvent impregnation method. The catalysts characterization was performed by N2 adsorption-desorption, X-ray Diffraction (XRD), X-ray Fluorescence (XRF), High Resolution Transmission Electron Microscopy (HRTEM), Field Emission Electron Scanning Microscopy (FESEM), Temperature Programmed Oxidation/Reduction (TPO/TPR) and NH3-Temperature Programmed Desorption (NH3-TPD) techniques. Then, evaluated by CO2/methane reforming. The CO2/methane reforming outcomes revealed that samaria-promoted catalyst showed excellent activity, stability and cock resistance, while yttria-promoted catalyst just illustrated good activity at high temperature and zirconia-promoted catalyst didn't show any modification in catalytic performance in comparison to Ni-based catalyst with no promoter. Samaria-promoted TEM and TPR analysis, indicated adding samaria improved the NiO particles interaction with SBA-15 support pores wall and NiO dispersion. The TPO analysis displayed that coke deposition in samaria-promoted sample after 12 h reaction is less than yttria-promoted during stream of 5 h. Also, it is suggested that for samaria containing catalyst, cock deposition occurred on the support. Therefore, nickel active sites were preserved for time on stream of 12 h, which is the main reason for samaria-promoted catalyst superior stability than other's. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:16408 / 16420
页数:13
相关论文
共 39 条
[1]   Role of La2O3 as Promoter and Support in Ni/γ-Al2O3 Catalysts for Dry Reforming of Methane [J].
Al-Fatesh, Ahmed S. ;
Naeem, Muhammad A. ;
Fakeeha, Anis H. ;
Abasaeed, Ahmed E. .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2014, 22 (01) :28-37
[2]   Hydrogen and syngas production by methane dry reforming on SBA-15 supported nickel catalysts: On the effect of promotion by Ce0.75Zr0.25O2 mixed oxide [J].
Albarazi, Abdulkader ;
Beaunier, Patricia ;
Da Costa, Patrick .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (01) :127-139
[3]   Effect of Ni loadings on the activity and coke formation of MgO-modified Ni/Al2O3 nanocatalyst in dry reforming of methane [J].
Alipour, Zahra ;
Rezaei, Mehran ;
Meshkani, Fereshteh .
JOURNAL OF ENERGY CHEMISTRY, 2014, 23 (05) :633-638
[4]   Effect of alkaline earth promoters (MgO, CaO, and BaO) on the activity and coke formation of Ni catalysts supported on nanocrystalline Al2O3 in dry reforming of methane [J].
Alipour, Zahra ;
Rezaei, Mehran ;
Meshkani, Fereshteh .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2014, 20 (05) :2858-2863
[5]   Syngas production via methane steam reforming with oxygen: plasma reactors versus chemical reactors [J].
Cormier, JM ;
Rusu, I .
JOURNAL OF PHYSICS D-APPLIED PHYSICS, 2001, 34 (18) :2798-2803
[6]   Influence of active metal loading and oxygen mobility on coke-free dry reforming of Ni-Co bimetallic catalysts [J].
Djinovic, Petar ;
Crnivec, Ilja Gasan Osojnik ;
Erjavec, Bostjan ;
Pintar, Albin .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2012, 125 :259-270
[7]   THE ROLE OF OXYGEN IN THE PARTIAL OXIDATION OF METHANE OVER A SAMARIUM OXIDE CATALYST [J].
EKSTROM, A ;
LAPSZEWICZ, JA .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1988, 110 (15) :5226-5228
[8]   Low temperature dry reforming of methane on rhodium and cobalt based catalysts: Active phase stabilization by confinement in mesoporous SBA-15 [J].
El Hassan, N. ;
Kaydouh, M. N. ;
Geagea, H. ;
El Zein, H. ;
Jabbour, K. ;
Casale, S. ;
El Zakhem, H. ;
Massiani, P. .
APPLIED CATALYSIS A-GENERAL, 2016, 520 :114-121
[9]   Production of synthetic gasoline and diesel fuel from dry reforming of methane [J].
Er-rbib, Hanaa ;
Bouallou, Chakib ;
Werkoff, Francois .
WHEC 2012 CONFERENCE PROCEEDINGS - 19TH WORLD HYDROGEN ENERGY CONFERENCE, 2012, 29 :156-165
[10]   Effect of support surface on methane dry-reforming catalyst preparation [J].
Frontera, P. ;
Macario, A. ;
Aloise, A. ;
Antonucci, P. L. ;
Giordano, G. ;
Nagy, J. B. .
CATALYSIS TODAY, 2013, 218 :18-29