Low-temperature synthesis of rhodium phosphide on alumina and investigation of its catalytic activity toward the hydrodesulfurization of thiophene

被引:26
作者
Kanda, Yasuharu [1 ]
Matsukura, Yuki [2 ]
Sawada, Ayaka [3 ]
Sugioka, Masatoshi [4 ]
Uemichi, Yoshio [1 ]
机构
[1] Muroran Inst Technol, Grad Sch Engn, Coll Environm Technol, Appl Chem Res Unit, 27-1 Mizumoto, Muroran, Hokkaido 0508585, Japan
[2] Muroran Inst Technol, Grad Sch Engn, Div Appl Sci, 27-1 Mizumoto, Muroran, Hokkaido 0508585, Japan
[3] Muroran Inst Technol, Grad Sch Engn, Div Chem & Mat Engn, 27-1 Mizumoto, Muroran, Hokkaido 0508585, Japan
[4] Muroran Inst Technol, Grad Sch Engn, Coll Design & Mfg Technol, Aeronaut & Astronaut Unit, 27-1 Mizumoto, Muroran, Hokkaido 0508585, Japan
关键词
Rhodium phosphide catalyst; Alumina support; Hydrodesulfurization; Triphenylphosphine; Low-temperature synthesis; NOBLE-METAL PHOSPHIDES; MO-FREE CATALYSTS; HYDROPROCESSING CATALYSTS; REDUCTION TEMPERATURE; SUPPORTED MOLYBDENUM; PHOSPHORUS PROMOTION; PHASE; NI2P; PERFORMANCE; DIBENZOTHIOPHENE;
D O I
10.1016/j.apcata.2016.01.040
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
In this study, the low-temperature synthesis of rhodium phosphide (Rh2P) on alumina (Al2O3) using triphenylphosphine (TPP) as a phosphorus (P) source and its catalytic activity toward hydrodesulfurization (HDS) were investigated to prepare a highly active HDS catalyst. TPP was more easily reduced than phosphate, and Rh2P was formed in the P(T)/Rh/Al2O3 catalyst prepared from TTP at lower temperature as compared with the temperature required by Rh-P(A)/Al2O3 catalyst prepared from a phosphate precursor. However, after reduction at a low temperature (450 degrees C), excess P covered the surface of Rh2P. The optimal reduction temperature for HDS rate of the P(T)/Rh/Al2O3 catalyst (650 degrees C) was lower than that of the Rh-P(A)/Al2O3 catalyst (800 degrees C). Furthermore, this temperature was slightly higher than the optimal reduction temperature for CO uptake (600 degrees C). These results are explained as follows: HDS rate is increased by both elimination of excess P on the active sites at higher reduction temperatures and enhancement of the crystallinity of Rh2P. Furthermore, because the particle size of the P(T)/Rh/Al2O3 catalyst (ca. 1.2 nm) was substantially smaller than that of the Rh-P(A)/Al2O3 catalyst, the P(T)/Rh/Al2O3 catalyst exhibited greater HDS rate compared with the Rh-P(A)/Al2O3 catalyst. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:25 / 31
页数:7
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