The CO Methanation Over The Rh and Ru Promoted NiO-CeO2-ZrO2 Catalysts

被引:0
作者
Balikci Derekaya, Filiz [1 ]
Kilinc, Yusuf Serkan [2 ]
机构
[1] Gazi Univ, Fac Engn, Chem Engn Dept, TR-06570 Ankara, Turkey
[2] Gazi Univ, Grad Sch Nat & Appl Sci, Adv Technol Dept, TR-06500 Ankara, Turkey
来源
GAZI UNIVERSITY JOURNAL OF SCIENCE | 2018年 / 31卷 / 04期
关键词
Catalysts; Methanation; Surfactant; Carbonmonoxide;
D O I
暂无
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
In this study, Rh and Ru promoted NiO-CeO2-ZrO2 catalysts were prepared with different Rh and Ru loadings (3, 4, 5 (wt.%)) by using two different methods. N-2 phsisorption, X-Ray diffraction, scanning electron microscope with energy-dispersive (SEM-EDX) techniques were used in order to characterize the catalysts. Catalytic activities of the catalysts were tested for CO methanation. The selective CO methanation catalytic activity tests were made over the most active catalysts. The effect of the Rh and Ru loading and preparation method on the CO methanation was discussed. The Ru and Rh have different effect on the surface areas of the catalysts and identifiable peaks for Rh and Ru not observed from the XRD analysis. Because of the low ratio of Rh and Ru in catalysts structures, both Ru and Rh containing catalysts gave similar CO methanation activity results. The 50% conversion temperatures of the 3% Ru/NiO-CeO2-ZrO2 catalysts which were prepared by the co-precipitation and surfactant assisted coprecipitation are 191 degrees C and 185 degrees C, respectively. Selective CO methanation was made over the 3% Ru/NiO-CeO2-ZrO2 catalysts. Catalysts gave good activity until 300 C. Because of the reversed water gas shift reaction activities of the catalysts were decreased after this temperature.
引用
收藏
页码:1064 / 1077
页数:14
相关论文
共 27 条
[1]   Catalytic methanation reaction over supported nickel-rhodium oxide for purification of simulated natural gas [J].
Abu Bakar, Wan Azelee Wan ;
Ali, Rusmidah ;
Toemen, Susilawati .
JOURNAL OF NATURAL GAS CHEMISTRY, 2011, 20 (06) :585-594
[2]   Ethanol steam reforming over Rh/CexZr1-xO2 catalysts:: Impact of the CO-CO2-CH4 interconversion reactions on the H2 production [J].
Birot, Anne ;
Epron, Florence ;
Descorme, Claude ;
Duprez, Daniel .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2008, 79 (1-2) :17-25
[3]   Synthesis and characterization of porous media produced by a sol-gel method [J].
Boonamnuayvitaya, V ;
Tayamanon, C ;
Sae-ung, S ;
Tanthapanichakoon, W .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (05) :1686-1691
[4]   Selective CO methanation catalysts for fuel processing applications [J].
Dagle, Robert A. ;
Wang, Yong ;
Xia, Guan-Guang ;
Strohm, James J. ;
Holladay, Jamelyn ;
Palo, Daniel R. .
APPLIED CATALYSIS A-GENERAL, 2007, 326 (02) :213-218
[5]   Rh, Ru and Pt ternary perovskites type oxides BaZr(1-x)MexO3 for methane dry reforming [J].
de Caprariis, Benedetta ;
de Filippis, Paolo ;
Palma, Vincenzo ;
Petrullo, Antonietta ;
Ricca, Antonio ;
Ruoccob, Concetta ;
Scarsella, Marco .
APPLIED CATALYSIS A-GENERAL, 2016, 517 :47-55
[6]   Design of Rh@Ce0.2Zr0.8O2-Al2O3 nanocomposite for ethanol steam reforming [J].
De Rogatis, Loredana ;
Montini, Tiziano ;
Casula, Maria E. ;
Fornasiero, Paolo .
JOURNAL OF ALLOYS AND COMPOUNDS, 2008, 451 (1-2) :516-520
[7]  
Derekaya Balikci F, 2014, TURK J CHEM, V38, P568
[8]   Ru-based catalysts for CO selective methanation reaction in H2-rich gases [J].
Djinovic, Petar ;
Galletti, Camilla ;
Specchia, Stefania ;
Specchia, Vito .
CATALYSIS TODAY, 2011, 164 (01) :282-287
[9]   Difference in the selectivity of CO and CO2 methanation reactions [J].
Fujita, SI ;
Takezawa, N .
CHEMICAL ENGINEERING JOURNAL, 1997, 68 (01) :63-68
[10]   Influence of the preparation method on the performance of Rh catalysts on CeO2 for WGS reaction [J].
Galletti, C. ;
Djinovic, P. ;
Specchia, S. ;
Batista, J. ;
Levec, J. ;
Pintar, A. ;
Specchia, V. .
CATALYSIS TODAY, 2011, 176 (01) :336-339