Performance of Si-modified Pd catalyst in acetylene hydrogenation: catalyst deactivation behavior

被引:48
作者
Kim, WJ [1 ]
Shin, EW [1 ]
Kang, JH [1 ]
Moon, SH [1 ]
机构
[1] Seoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Seoul 151744, South Korea
关键词
acetylene hydrogenation; Pd catalyst; Si modification; deactivation; green oil; sintering;
D O I
10.1016/S0926-860X(03)00367-3
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
The deactivation behavior of Si-modified Pd catalysts in acetylene hydrogenation was studied using thermogravimetric analysis (TGA), infrared (IR) spectroscopy, and reaction tests. TGA and IR analyses of green oil produced on the catalyst indicate that it is produced in smaller amounts and its average chain length is shorter on a Si-modified catalyst than on an unmodified one. The above findings are due to deposition of Si species on the Pd surface; such deposits effectively block multiply-coordinated adsorption sites on the catalyst and suppress the formation of green oil on the catalyst surface, specifically on or in the vicinity of Pd. The Si species also retard the sintering of Pd crystallites during the regeneration step and allow for the slow deactivation of the catalyst during acetylene hydrogenation, after regeneration. The improvement in the deactivation behavior of the Si-modified catalyst is believed to arise from the geometric modification of the Pd surface with small clusters of the Si species. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:305 / 313
页数:9
相关论文
共 30 条
[1]   HYDROGENATION OF ACETYLENE OVER SUPPORTED METAL-CATALYSTS .2. [C-14]TRACER STUDY OF DEACTIVATION PHENOMENA [J].
ALAMMAR, AS ;
WEBB, G .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS I, 1978, 74 :657-664
[2]   HYDROGENATION OF ACETYLENE OVER SUPPORTED METAL-CATALYSTS .1. ADSORPTION OF [C-14]ACETYLENE AND [C-14]ETHYLENE ON SILICA SUPPORTED RHODIUM, IRIDIUM AND PALLADIUM AND ALUMINA SUPPORTED PALLADIUM [J].
ALAMMAR, AS ;
WEBB, G .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS I, 1978, 74 :195-205
[3]  
BATTISTON GC, 1982, APPL CATAL, V2, P2
[4]  
BOITIAUX JP, 1985, HYDROCARB PROCESS, V64, P51
[5]  
COLTHUP NB, 1975, INTRO INFRARED RAMAN, P223
[6]  
DENHARTOG AJ, 1990, J MOL CATAL, V60, P99
[7]  
GANDMAN ZE, 1975, INT CHEM ENG, V15, P183
[8]   CHARACTERIZATION OF SUPPORTED PALLADIUM CATALYSTS .2. PD/SIO2 [J].
JUSZCZYK, W ;
KARPINSKI, Z .
JOURNAL OF CATALYSIS, 1989, 117 (02) :519-532
[9]   Selective hydrogenation of acetylene on Pd/SiO2 catalysts promoted with Ti, Nb and Ce oxides [J].
Kang, JH ;
Shin, EW ;
Kim, WJ ;
Park, JD ;
Moon, SH .
CATALYSIS TODAY, 2000, 63 (2-4) :183-188
[10]   Ethylene selectivity variation in acetylene hydrogenation reactor with the hydrogen/acetylene ratio at the reactor inlet [J].
Kim, WJ ;
Choi, CH ;
Moon, SH .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2002, 19 (04) :617-621