Dry reforming of CH4 over stabilized Ni-La@KCC-1 catalyst: Effects of La promoter and optimization studies using RSM

被引:56
作者
Abdulrasheed, A. A. [1 ,3 ]
Jalil, A. A. [1 ,2 ]
Hamid, M. Y. S. [1 ]
Siang, T. J. [1 ]
Abdullah, T. A. T. [2 ]
机构
[1] Univ Teknol Malaysia, Fac Engn, Sch Chem & Energy Engn, Utm Johor Bahru 81310, Johor, Malaysia
[2] Univ Teknol Malaysia, Ctr Hydrogen Energy, Inst Future Energy, Utm Johor Bahru 81310, Johor, Malaysia
[3] Abubakar Tafawa Balewa Univ, Dept Chem Engn, PMB 0248, Bauchi, Bauchi State, Nigeria
关键词
Bimetallic catalyst; Fibrous silica; Dry reforming; Coke resistance; Optimization; SYNGAS PRODUCTION; SURFACE MODIFICATION; CO2; METHANATION; NI; NANOPARTICLES; CARBON; SILICA; PEROVSKITES; PERFORMANCE; DESIGN;
D O I
10.1016/j.jcou.2019.12.018
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A bimetallic Ni-La catalyst supported on fibrous silica KCC-1 (KAUST Catalysis Centre 1) was prepared by in situ one-pot hydrothermal method. The catalyst was characterized by XRD, BET, FESEM-EDX, TEM, H-2-TPR, FTIRpyrrole, O-2 -TPO and XPS. The H-2 -TPR result revealed that the addition of La2O3 enhanced the reducibility of Ni2+, as observed by the 25.1 % increase in H-2 consumption. This is an evidence of improved dispersion as also indicated in the TEM images. Extra affinity for CO2 chemisorption and activation was provided by the La promoted catalyst with strong and intense basic sites to improve product selectivity. Therefore, the activity of catalyst was improved with significant enhancement in CO2 conversion and H-2/CO selectivity. As a result, the activation energy for CO2 and CH4 conversions were reduced by a margin of 10.4 kJ/mol and 2.2 kJ/mol respectively. Ni-La@KCC-1 catalyst showed no sign of deactivation throughout the 22 h time on stream while Ni@ KCC-1 deactivated after 15 h at a higher reactant feed composition. From ANOVA analysis, the reaction temperature is the most significant variable that influence CH4 conversion. The reaction operating condition was obtained that gives the optimum CH4 conversion. The model predicted response was 98.2 % fitted to the observed experimental values.
引用
收藏
页码:230 / 239
页数:10
相关论文
共 52 条
[1]  
Abdullah A.S., 2019, INT J AMBIENT ENERGY, P1
[2]   Recent advances in dry reforming of methane over Ni-based catalysts [J].
Abdullah, Bawadi ;
Ghani, Nur Azeanni Abd ;
Vo, Dai-Viet N. .
JOURNAL OF CLEANER PRODUCTION, 2017, 162 :170-185
[3]   Surface modification of activated carbon for adsorption of SO2 and NOX: A review of existing and emerging technologies [J].
Abdulrasheed, A. A. ;
Jalil, A. A. ;
Triwahyono, S. ;
Zaini, M. A. A. ;
Gambo, Y. ;
Ibrahim, M. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 94 :1067-1085
[4]   A review on catalyst development for dry reforming of methane to syngas: Recent advances [J].
Abdulrasheed, Abdulrahman ;
Jalil, Aishah Abdul ;
Gambo, Yahya ;
Ibrahim, Maryam ;
Hambali, Hambali Umar ;
Hamill, Muhamed Yusuf Shahul .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2019, 108 :175-193
[5]  
[Anonymous], J CO2 UTIL
[6]  
[Anonymous], J CO2 UTIL
[7]   Catalyst design for dry reforming of methane: Analysis review [J].
Aramouni, Nicolas Abdel Karim ;
Touma, Jad G. ;
Abu Tarboush, Belal ;
Zeaiter, Joseph ;
Ahmad, Mohammad N. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 82 :2570-2585
[8]   Dry reforming of methane over CeO2 supported Ni, Co and Ni-Co catalysts [J].
Ay, Hale ;
Uner, Deniz .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2015, 179 :128-138
[9]   Modelling and optimization of syngas production from methane dry reforming over ceria-supported cobalt catalyst using artificial neural networks and Box-Behnken design [J].
Ayodele, Bamidele V. ;
Cheng, Chin Kui .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2015, 32 :246-258
[10]   CO2 methanation over Ni-promoted mesostructured silica nanoparticles: Influence of Ni loading and water vapor on activity and response surface methodology studies [J].
Aziz, M. A. A. ;
Jalil, A. A. ;
Triwahyono, S. ;
Saad, M. W. A. .
CHEMICAL ENGINEERING JOURNAL, 2015, 260 :757-764