Two-dimensional porous SiO2 nanomesh supported high dispersed Ni nanoparticles for CO methanation

被引:31
作者
Li, Panpan [1 ]
Zhu, Mingyuan [1 ]
Dan, Jianming [1 ]
Kang, Lihua [1 ]
Lai, Linfei [2 ,3 ]
Cai, Xiaoyi [4 ]
Zhang, Jianshu [1 ]
Yu, Feng [1 ]
Tian, Zhiqun [5 ]
Dai, Bin [1 ]
机构
[1] Shihezi Univ, Sch Chem & Chem Engn, Key Lab Green Proc Chem Engn Xinjiang Bingtuan, Shihezi 832003, Peoples R China
[2] Nanjing Tech Univ, Key Lab Flexible Elect KLOFE, Jiangsu Natl Synerget Innovat Ctr Adv Mat SICAM, Nanjing 211816, Jiangsu, Peoples R China
[3] Nanjing Tech Univ, Inst Adv Mat, Jiangsu Natl Synerget Innovat Ctr Adv Mat SICAM, Nanjing 211816, Jiangsu, Peoples R China
[4] Nanyang Technol Univ, Energy Res Inst NTU ERIAN, 1 Clean Tech Loop, Singapore 637141, Singapore
[5] Guangxi Univ, Collaborat Innovat Ctr Renewable Energy Mat, Nanning 530004, Peoples R China
基金
中国国家自然科学基金;
关键词
Two-dimensional materials; Porous silica nanomesh; CO methanation; Vermiculite; CARBON-MONOXIDE; NICKEL; CATALYSTS; SYNGAS; MCM-41; CE; PERFORMANCE; MECHANISM; DIOXIDE; PLASMA;
D O I
10.1016/j.cej.2017.06.010
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Two-dimensional (2D) porous SiO2 nanomesh obtained from mixed acid etching of vermiculite (VMT) was successfully used as a catalyst support for CO methanation. Compared with three-dimensional (3D) MCM-41, 2D VMT-SiO2 provided a superior position for implantation of NiO species. Although NiO/VMT-SiO2 has a total loading of 10 wt.% NiO as well as the NiO/MCM-41, the NiO particles on VMT-SiO2 were observed to show a better dispersion as the of 3D MCM-41 channels were easily blocked by large NiO particles. Moreover, on the basis of the H-2 temperature-programming reduction results, NiO particles on VMT-SiO2 were more easily reduced than those on MCM-41. These characteristics indicated that NiO/VMT-SiO2 was significantly superior to NiO/MCM-41. The as-obtained NiO/VMT-SiO2 exhibited a CO conversion of 85.9%, CH4 selectivity of 78% at 450 degrees C, 0.1151 s (1) turn over frequency at 320 degrees C and a gas hourly space velocity of 20745 ml/g/h. All of which were much better than those measured for NiO/MCM-41. We believed that 2D VMT-SiO2 as a new catalyst support open a prospect application of catalyst. (C) 2017 Published by Elsevier B.V.
引用
收藏
页码:774 / 780
页数:7
相关论文
共 41 条
[1]   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
[2]   CO2 reforming of methane to syngas I:: evaluation of hydrotalcite clay-derived catalysts [J].
Bhattacharyya, A ;
Chang, VW ;
Schumacher, DJ .
APPLIED CLAY SCIENCE, 1998, 13 (5-6) :317-328
[3]   Ni-based catalyst derived from Ni/Al hydrotalcite-like compounds by the urea hydrolysis method for CO methanation [J].
Bian, Li ;
Wang, Weihan ;
Xia, Rong ;
Li, Zhenhua .
RSC ADVANCES, 2016, 6 (01) :677-686
[4]   Water-Dispersible Magnetite-Reduced Graphene Oxide Composites for Arsenic Removal [J].
Chandra, Vimlesh ;
Park, Jaesung ;
Chun, Young ;
Lee, Jung Woo ;
Hwang, In-Chul ;
Kim, Kwang S. .
ACS NANO, 2010, 4 (07) :3979-3986
[5]   Silicon-nickel intermetallic compounds supported on silica as a highly efficient catalyst for CO methanation [J].
Chen, Xiao ;
Jin, Jianhui ;
Sha, Guangyan ;
Li, Chuang ;
Zhang, Bingsen ;
Su, Dangsheng ;
Williams, Christopher T. ;
Liang, Changhai .
CATALYSIS SCIENCE & TECHNOLOGY, 2014, 4 (01) :53-61
[6]   Nickel catalysts supported on amino-functionalized MCM-41 for syngas methanation [J].
Dai, Bin ;
Wen, Bo ;
Zhu, Mingyuan ;
Kang, Lihua ;
Yu, Feng .
RSC ADVANCES, 2016, 6 (71) :66957-66962
[7]  
Dan J., 2016, NANOSCI NANOTECHNOL
[8]   Methanation of carbon dioxide on Ni-incorporated MCM-41 catalysts: The influence of catalyst pretreatment and study of steady-state reaction [J].
Du, Guoan ;
Lim, Sangyun ;
Yang, Yanhui ;
Wang, Chuan ;
Pfefferle, Lisa ;
Haller, Gary L. .
JOURNAL OF CATALYSIS, 2007, 249 (02) :370-379
[9]  
Daza CE, 2011, REV FAC ING-UNIV ANT, P66
[10]   Steady state isotopic transient kinetic analysis (SSITKA) of CO hydrogenation on different Co catalysts [J].
Froseth, V ;
Storsæter, S ;
Borg, O ;
Blekkan, EA ;
Ronning, M ;
Holmen, A .
APPLIED CATALYSIS A-GENERAL, 2005, 289 (01) :10-15