Effect of Calcination Temperature on the Performance of the Ni@SiO2 Catalyst in Methane Dry Reforming

被引:95
作者
Han, Bolin [1 ]
Zhao, Long [1 ]
Wang, Fagen [1 ,2 ]
Xu, Leilei [3 ]
Yu, Hao [4 ]
Cui, Yi [5 ]
Zhang, Jianming [1 ]
Shi, Weidong [1 ]
机构
[1] Jiangsu Univ, Sch Chem & Chem Engn, Zhenjiang 212013, Jiangsu, Peoples R China
[2] Qingdao Univ Sci & Technol, Shandong Key Lab Biochem Anal, Coll Chem & Mol Engn, Qingdao 266042, Peoples R China
[3] Nanjing Univ Informat Sci & Technol, Sch Environm Sci & Engn, Nanjing 210044, Peoples R China
[4] Shandong Univ Sci & Technol, Coll Chem & Environm Engn, Qingdao 266590, Shandong, Peoples R China
[5] Chinese Acad Sci, Suzhou Inst Nanotech & Nanobion, Vacuum Interconnected Nanotech Workstn, Suzhou 215123, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
METAL-SUPPORT INTERACTION; PARTICLE-SIZE; SYNGAS PRODUCTION; SHELL; OXIDATION; COKING;
D O I
10.1021/acs.iecr.0c01213
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Calcination plays an important role in obtaining high-performance catalysts for heterogeneous reactions. In this work, the effect of calcination temperature on the performance of the Ni@SiO2 catalyst in the methane dry reforming reaction was investigated. The calcination temperature from 823 to 1223 K led to different sizes of Ni nanoparticles and strengths of metal-support interactions in the catalysts, which consequently affected the performance of the reforming reaction. The highest performance was neither achieved over Ni@SiO2-T (T = 823 and 923 K) catalysts with small Ni sizes and weak metal-support interactions nor gained over Ni@SiO2-T (T = 1123 and 1223 K) catalysts with big Ni sizes and strong metal-support interactions, while it was obtained over the Ni@SiO2-1023 catalyst with intermediate Ni size and intermediate metal-support interactions. The volcanic relationship between the catalytic performance and catalyst calcination temperature was assigned to both the Ni size effect and metal-support interaction that their combination significantly influenced the performance of the methane dry reforming reaction. The combination strategy may provide a possible optimization approach for other heterogeneous catalytic reactions.
引用
收藏
页码:13370 / 13379
页数:10
相关论文
共 31 条
[1]   Syngas Production via Methane Dry Reforming over Ceria-Magnesia Mixed Oxide-Supported Nickel Catalysts [J].
Al-Swai, Basem M. ;
Osman, Noridah ;
Alnarabiji, Mohamad Sahban ;
Adesina, Adesoji A. ;
Abdullah, Bawadi .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2019, 58 (02) :539-552
[2]   Thermodynamic analysis of methane dry reforming: Effect of the catalyst particle size on carbon formation [J].
Aramouni, Nicolas Abdel Karim ;
Zeaiter, Joseph ;
Kwapinski, Witold ;
Ahmad, Mohammad N. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 150 :614-622
[3]   INFLUENCE OF ORDER-DISORDER PARAMETERS ON THE REDUCIBILITY OF NI-CONTAINING AND CU-CONTAINING SILICATES - APPLICATION TO TALC AND CHRYSOCOLLA [J].
CARRIAT, JY ;
CHE, M ;
KERMAREC, M ;
DECARREAU, A .
CATALYSIS LETTERS, 1994, 25 (1-2) :127-140
[4]   Silica-Ceria sandwiched Ni core-shell catalyst for low temperature dry reforming of biogas: Coke resistance and mechanistic insights [J].
Das, S. ;
Ashok, J. ;
Bian, Z. ;
Dewangan, N. ;
Wai, M. H. ;
Du, Y. ;
Borgna, A. ;
Hidajat, K. ;
Kawi, S. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2018, 230 :220-236
[5]   Low-Temperature CO2 Methanation over CeO2-Supported Ru Single Atoms, Nanoclusters, and Nanoparticles Competitively Tuned by Strong Metal-Support Interactions and H-Spillover Effect [J].
Guo, Yu ;
Mei, Sheng ;
Yuan, Kun ;
Wang, De-Jiu ;
Liu, Hai-Chao ;
Yan, Chun-Hua ;
Zhang, Ya-Wen .
ACS CATALYSIS, 2018, 8 (07) :6203-6215
[6]   Uncoupling the size and support effects of Ni catalysIs for dry reforming of methane [J].
Han, Joung Woo ;
Park, Jun Seong ;
Choi, Min Suk ;
Lee, Hyunjoo .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2017, 203 :625-632
[7]   Kinetics underpinning the C-CO2 gasification of waste tyre char and its interaction with coal char upon co-gasification [J].
Issac, Miriam ;
Dai, Baiqian ;
Zhang, Lian .
FUEL, 2019, 256
[8]   Effect of metal particle size on coking during CO2 reforming of CH4 over Ni-alumina aerogel catalysts [J].
Kim, JH ;
Suh, DJ ;
Park, TJ ;
Kim, KL .
APPLIED CATALYSIS A-GENERAL, 2000, 197 (02) :191-200
[9]  
Kong W., 2019, ENERGY TECHNOL, V7
[10]   Ni stabilised on inorganic complex structures: superior catalysts for chemical CO2 recycling via dry reforming of methane [J].
le Sache, E. ;
Pastor-Perez, L. ;
Watson, D. ;
Sepulveda-Escribano, A. ;
Reina, T. R. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2018, 236 :458-465