Ammonia Hydrothermally Treated SiO2 Supported Rh-Based Catalyst for CO Hydrogenation to C2 Oxygenates: Remarkable Effect of Support Pore Size

被引:6
作者
Chen, Weimiao [1 ]
Song, Xiangen [1 ]
Ning, Lili [1 ]
Ding, Yunjie [1 ,2 ]
机构
[1] Chinese Acad Sci, Dalian Inst Chem Phys, Dalian Natl Lab Clean Energy, Dalian 116023, Peoples R China
[2] Chinese Acad Sci, Dalian Inst Chem Phys, State Key Lab Catalysis, Dalian 116023, Peoples R China
关键词
PARTICLE-SIZE; ETHANOL-PRODUCTION; SYNGAS CONVERSION; SURFACE-STRUCTURE; CARBON-MONOXIDE; FT-IR; RH-MN-LI/SIO2; SILICA; RH/SIO2; CALCINATION;
D O I
10.1021/acs.iecr.0c03676
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Silica is a traditional carrier for Rh-based catalyst for CO hydrogenation to C-2 oxygenates, and its pretreatment with various organic solvents under specified conditions usually affects the surface and textural properties of silica and thus the catalytic performance of Rh-based catalyst. In this paper, silica samples were hydrothermally treated with different concentrations of ammonia and were used to support Rh-based catalysts. The as-made supports and the respective catalysts were characterized by N-2 adsorption-desorption, TEM, XRD, FT-IR, H-2-TPR, CO chemisorption, CO-TPD, and temperature-programmed surface reaction (TPSR). The results showed that the hydrothermal treatment enlarged the pore size of silica gradually from 8.1 nm on parent sample to 26.5 nm on that treated by 10% ammonia. Smaller pore size usually with higher surface area of silica was beneficial to the formation of highly dispersed Rh species; however, the mean Rh particle sizes here were within the optimal range of 2-4 nm. It was also demonstrated that, with the increasing of pore size of silica, the CO insertion ability weakened, while the CO dissociation capability strengthened relatively; meanwhile, the diffusion limitation of CO could be eliminated gradually, leading to a decrease of the local H-2/CO ratio during CO hydrogenation reaction. This could restrain the hydrogenation ability but facilitate the CO dissociation or insertion. Consequently, carbon chain propagation was much promoted to give more C-2(+) hydrocarbons, while the hydrogenation of C-2 oxygenate precursors was prohibited to yield much less ethanol. Moreover, Rh-based catalysts supported on larger pore sizes of silica were more stable than that on the untreated one. This finding provides a useful strategy to effectively adjust the catalytic performance of Rh-based catalyst through controlling internal diffusion by selecting a support with the proper pore size.
引用
收藏
页码:18798 / 18807
页数:10
相关论文
共 49 条
[1]   HIGH-PRESSURE INSITU FT-IR STUDY OF CO HYDROGENATION OVER RH/SIO2 CATALYST [J].
ARAKAWA, H ;
FUKUSHIMA, T ;
ICHIKAWA, M ;
TAKEUCHI, K ;
MATSUZAKI, T ;
SUGI, Y .
CHEMISTRY LETTERS, 1985, (01) :23-26
[2]   EFFECT OF RH PARTICLE-SIZE ON CO DESORPTION FROM RH/ALUMINA MODEL CATALYSTS [J].
BELTON, DN ;
SCHMIEG, SJ .
SURFACE SCIENCE, 1988, 202 (1-2) :238-254
[3]  
BOWKER M, 1992, CATAL TODAY, V15, P77
[4]   A Simple Method for Preparing the Highly Dispersed Supported Co3O4 on Silica Support [J].
Chen, Jianfeng ;
Zhang, Yurui ;
Tan, Li ;
Zhang, Yi .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (07) :4212-4215
[5]  
Chen W, 2005, J NAT GAS CHEM, V14, P199
[6]   Promotion effect of support calcination on ethanol production from CO hydrogenation over Rh/Fe/Al2O3 catalysts [J].
Chen, Weimiao ;
Ding, Yunjie ;
Song, Xiangeng ;
Wang, Tao ;
Luo, Hongyuan .
APPLIED CATALYSIS A-GENERAL, 2011, 407 (1-2) :231-237
[7]   An effective method of controlling metal particle size on impregnated Rh-Mn-Li/SiO2 catalyst [J].
Chen, WM ;
Ding, YJ ;
Jiang, DH ;
Pan, ZD ;
Luo, HY .
CATALYSIS LETTERS, 2005, 104 (3-4) :177-180
[8]   The effects of PVP-modified SiO2 on the catalytic performance of CO hydrogenation over Rh-Mn-Li/SiO2 catalysts [J].
Ding, Dan ;
Yu, Jun ;
Guo, Qiangsheng ;
Guo, Xiaoming ;
Xiao, Xiuzhen ;
Mao, Dongsen ;
Lu, Guanzhong .
RSC ADVANCES, 2017, 7 (76) :48420-48428
[9]   EFFECTS OF SUPPORT ON THE ADSORPTION AND DISSOCIATION OF CO AND ON THE REACTIVITY OF SURFACE CARBON ON RH CATALYSTS [J].
ERDOHELYI, A ;
SOLYMOSI, F .
JOURNAL OF CATALYSIS, 1983, 84 (02) :446-460
[10]   HYDROGENATION OF ADSORBED CARBON-MONOXIDE ON SUPPORTED PLATINUM GROUP-METALS [J].
FUJIMOTO, K ;
KAMEYAMA, M ;
KUNUGI, T .
JOURNAL OF CATALYSIS, 1980, 61 (01) :7-14