Effects of Pressure and Temperature in Hydrothermal Preparation of MoS2 Catalyst for Methanation Reaction

被引:14
作者
Choi, Jae-Myeong [1 ]
Kim, Sung-Hyun [1 ]
Lee, Seung-Jae [2 ]
Kim, Seong-Soo [2 ]
机构
[1] Korea Univ, Dept Chem & Biol Engn, 145 Anam Ro, Seoul 02841, South Korea
[2] Korea Inst Energy Res, Biomass & Wastes Energy Lab, 152 Gajeong Ro, Daejeon 34129, South Korea
关键词
MoS2; Hydrothermal reaction; Pressure; Temperature; Catalytic activity; MOLYBDENUM SULFIDE CATALYSTS; IN-SITU DECOMPOSITION; EX AMMONIUM TETRATHIOMOLYBDATE; TETRAALKYLAMMONIUM THIOMOLYBDATES; PROGRAMMED REDUCTION; SURFACE-AREA; HYDRODESULFURIZATION ACTIVITY; NANOCRYSTALLINE MOS2; ASSISTED SYNTHESIS; DISULFIDE MOS2;
D O I
10.1007/s10562-018-2372-x
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
Unsupported MoS2 catalysts were prepared for the methanation reaction by varying the pressure and temperature in the hydrothermal reaction by using ammonium tetrathiomolybdate (ATTM). The physical and chemical characteristics of the catalysts were analyzed by using XRD, SEM, TEM, BET, XPS, H-2-TPR, and CO-TPD techniques. The catalyst particles were formed in the bent fringe shape by stacking the (0 0 2) planes, and consisted mostly of MoS2, with some Mo2S5 and MoS3. It was found that the BET surface and active sites such as surface Mo4+ and sulfur vacancies increased with increasing preparation pressure, which could contribute to the improvement of MoS2 catalytic activity. The increase in preparation temperature not only favored the decomposition of ATTM into MoS2, but also lowered the number of active sites accessible for the reaction. Thus, it was suggested that the preparation temperature should be controlled at 350 A degrees C to improve the catalytic activity. [GRAPHICS] .
引用
收藏
页码:1803 / 1814
页数:12
相关论文
共 53 条
[1]   On the interpretation of temperature programmed reduction patterns of transition metals sulphides [J].
Afanasiev, P .
APPLIED CATALYSIS A-GENERAL, 2006, 303 (01) :110-115
[2]   Surfactant-assisted synthesis of highly dispersed molybdenum sulfide [J].
Afanasiev, P ;
Xia, GF ;
Berhault, G ;
Jouguet, B ;
Lacroix, M .
CHEMISTRY OF MATERIALS, 1999, 11 (11) :3216-3219
[3]   The influence of reducing and sulfiding conditions on the properties of unsupported MoS2-based catalysts [J].
Afanasiev, Pavel .
JOURNAL OF CATALYSIS, 2010, 269 (02) :269-280
[4]   Characterization and HDS activity of mesoporous MoS2 catalysts prepared by in situ activation of tetraalkylammonium thiomolybdates [J].
Alonso, G ;
Berhault, G ;
Aguilar, A ;
Collins, V ;
Ornelas, C ;
Fuentes, S ;
Chianelli, RR .
JOURNAL OF CATALYSIS, 2002, 208 (02) :359-369
[5]   Preparation of MoS2 and WS2 catalysts by in situ decomposition of ammonium thiosalts [J].
Alonso, G ;
Del Valle, M ;
Cruz, J ;
Licea-Claverie, A ;
Petranovskii, V ;
Fuentes, S .
CATALYSIS LETTERS, 1998, 52 (1-2) :55-61
[6]   Preparation of MoS2 catalysts by in situ decomposition of tetraalkylammonium thiomolybdates [J].
Alonso, G ;
Del Valle, M ;
Cruz, J ;
Petranovskii, V ;
Licea-Claverie, A ;
Fuentes, S .
CATALYSIS TODAY, 1998, 43 (1-2) :117-122
[7]   Comparative study of MoS2 and Co/MoS2 catalysts prepared by ex situ in situ activation of ammonium and tetraalkylammonium thiomolybdates [J].
Alvarez, L ;
Espino, J ;
Ornelas, C ;
Rico, JL ;
Cortez, MT ;
Berhault, G ;
Alonso, G .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2004, 210 (1-2) :105-117
[8]   Crystallite size determination of highly dispersed unsupported MoS2 catalysts [J].
Calais, C ;
Matsubayashi, N ;
Geantet, C ;
Yoshimura, Y ;
Shimada, H ;
Nishijima, A ;
Lacroix, M ;
Breysse, M .
JOURNAL OF CATALYSIS, 1998, 174 (02) :130-141
[9]   Direct synthesis of methanethiol from H2S-rich syngas over sulfided Mo-based catalysts [J].
Chen, Aiping ;
Wang, Qi ;
Li, Qiaoling ;
Hao, Yingjuan ;
Fang, Weiping ;
Yang, Yiquan .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2008, 283 (1-2) :69-76
[10]   Comparative study on MoS2 and WS2 for electrocatalytic water splitting [J].
Chen, Tzu-Yin ;
Chang, Yung-Huang ;
Hsu, Chang-Lung ;
Wei, Kung-Hwa ;
Chiang, Chia-Ying ;
Li, Lain-Jong .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (28) :12302-12309