Effect of Al2O3/SiO2 ratio on iron-based catalysts, for Fischer-Tropsch synthesis

被引:31
作者
Wan, Hai-Jun
Wu, Bao-Shan
Zhang, Cheng-Hua
Teng, Bo-Tao
Tao, Zhi-Chao
Yang, Yong
Zhu, Yu-Lei
Xiang, Hong-Wei
Li, Yong-Wang [1 ]
机构
[1] Chinese Acad Sci, State Key Lab Coal Convers, Inst Coal Chem, Taiyuan 030001, Peoples R China
[2] Chinese Acad Sci, Grad Sch, Beijing 100039, Peoples R China
基金
中国国家自然科学基金;
关键词
Fischer-Tropsch synthesis; precipitated iron-based catalysts; Mossbauer spectroscopy;
D O I
10.1016/j.fuel.2005.12.016
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A systematic study was undertaken to investigate the effects of Al2O3/SiO2 ratio on reduction, carburization and catalytic behavior of iron-based Fischer-Tropsch synthesis (FFS) catalysts promoted with potassium and copper. The catalysts were characterized by N-2 physical adsorption, CO2 temperature-programmed desorption (TPD), H-2 temperature-programmed reduction (TPR) and Mossbauer effect spectroscopy (MES). CO2-TPD indicated that Al2O3 binder has stronger acidity than SiO2 binder and weakens the surface basicity of the catalysts. H-2-TPR profiles suggested that the lower Al2O3/SiO2 ratio promotes the reduction of Fe2O3 --> Fe3O4. With further increasing Al2O3/SiO2 ratio, the transformation of Fe2O3-->Fe3O4 shifts to higher temperatures. The MES results showed that the increase of Al2O3/SiO2 ratio leads to the relatively large crystallite size of alpha-Fe2O3 and inhibits carburization of the catalyst. During reaction tests in a fixed bed reactor it was found that a maximum in catalyst activity is noted at the Al2O3/SiO2 ratio of 5/20 (weight basis). The selectivity to olefins shows a rapid decrease and the formations of methane and light hydrocarbons are promoted with increasing Al2O3/SiO2 ratio. The oxygenate selectivity in total products increases with increasing Al2O3/SiO2 ratio. (C) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1371 / 1377
页数:7
相关论文
共 26 条
[1]   EFFECTS OF POTASSIUM PROMOTION ON THE ACTIVITY AND SELECTIVITY OF IRON FISCHER-TROPSCH CATALYSTS [J].
ARAKAWA, H ;
BELL, AT .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (01) :97-103
[2]   BINDER SUPPORT EFFECTS ON THE ACTIVITY AND SELECTIVITY OF IRON CATALYSTS IN THE FISCHER-TROPSCH SYNTHESIS [J].
BUKUR, DB ;
LANG, X ;
MUKESH, D ;
ZIMMERMAN, WH ;
ROSYNEK, MP ;
LI, CP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (08) :1588-1599
[3]   Supported iron catalysts for slurry phase Fischer-Tropsch synthesis [J].
Bukur, DB ;
Sivaraj, C .
APPLIED CATALYSIS A-GENERAL, 2002, 231 (1-2) :201-214
[4]   PROMOTER EFFECTS ON PRECIPITATED IRON CATALYSTS FOR FISCHER-TROPSCH SYNTHESIS [J].
BUKUR, DB ;
MUKESH, D ;
PATEL, SA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (02) :194-204
[5]   FISCHER-TROPSCH SYNTHESIS OVER REDUCED AND UNREDUCED IRON-OXIDE CATALYSTS [J].
DICTOR, RA ;
BELL, AT .
JOURNAL OF CATALYSIS, 1986, 97 (01) :121-136
[6]   Changes in physico-chemical properties of iron-based Fischer-Tropsch catalyst induced by SiO2 addition [J].
Dlamini, H ;
Motjope, T ;
Joorst, G ;
ter Stege, G ;
Mdleleni, M .
CATALYSIS LETTERS, 2002, 78 (1-4) :201-207
[7]   Fischer-Tropsch reactions and the environment [J].
Dry, ME .
APPLIED CATALYSIS A-GENERAL, 1999, 189 (02) :185-190
[8]  
DRY ME, 1983, APPLIED IND CATALYSI, V2, P167
[9]   Effect of reaction conditions on the product distribution during Fischer-Tropsch synthesis over an industrial Fe-Mn catalyst [J].
Ji, YY ;
Xiang, HW ;
Yang, JL ;
Xu, YY ;
Li, YW ;
Zhong, B .
APPLIED CATALYSIS A-GENERAL, 2001, 214 (01) :77-86
[10]   Phase transformations in iron Fischer-Tropsch catalysts during temperature-programmed reduction [J].
Jin, YM ;
Datye, AK .
JOURNAL OF CATALYSIS, 2000, 196 (01) :8-17