Effects of Cr Promoter on Structure and Fischer-Tropsch Synthesis Performance over Fe-Based Catalysts

被引:3
作者
Wang Hulin [1 ,2 ]
Yang Yong [1 ]
Wang Hong [1 ,2 ]
Qing Ming [1 ,2 ]
Xiang Hongwei [1 ]
Li Yongwang [1 ]
机构
[1] Chinese Acad Sci, Shanxi Inst Coal Chem, State Key Lab Coal Convers, Taiyuan 030001, Shanxi, Peoples R China
[2] Chinese Acad Sci, Grad Univ, Beijing 100049, Peoples R China
关键词
Fischer-Tropsch synthesis; iron-based catalyst; chromium promoter; solid solution; fixed-bed reactor; IRON-MANGANESE CATALYST; PRECURSORS; REDUCTION; CHROMIUM;
D O I
10.3724/SP.J.1088.2010.91246
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The effects of promoter Cr content in the Fe-based Fischer-Tropsch synthesis (FTS) catalysts on the textural properties, reduction behavior, and phase transformation of the catalysts during reduction and reaction were investigated by N(2) adsorption, X-ray diffraction, Mossbauer spectroscopy, X-ray photoelectron spectroscopy, H(2) differential thermogravimetric analysis, and CO temperature-programmed reduction over the coprecipitated Fe-based catalysts. The FTS performance of the Fe-based catalysts promoted with Cr was studied in a fixed-bed reactor under the conditions of H(2)/CO = 2.0, 260-300 degrees C, 1.5 MPa, and 2 000 ml/(g.h). The results showed that the strong interaction existed between Fe and Cr species by the formation of Fe-Cr solid solution, alpha-(Fe(1-x)Cr(x))(2)O(3). With the increase of promoter Cr content in the Fe-based catalysts, the phases of the catalysts gradually transformed to the Fe-rich phase and Cr-rich phase. Because the Fe-Cr solid solution strongly inhibited the reduction of the catalyst, Cr-promoted Fe-based catalysts exhibited low activity due to its lower extents of both reducibility and carburization. The promoter Cr enhanced the formation of methane and light hydrocarbon products but inhibited the activity of water-gas-shift reaction.
引用
收藏
页码:809 / 816
页数:8
相关论文
共 20 条
[1]  
BROMFIELD TC, 2005, Patent No. 049765
[2]   Highly active and stable iron Fischer-Tropsch catalyst for synthesis gas conversion to liquid fuels [J].
Bukur, DB ;
Lang, XS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (09) :3270-3275
[3]   Effect of reduction pressure on precipitated potassium promoted iron-manganese catalyst for Fischer-Tropsch synthesis [J].
Ding, Mingyue ;
Yang, Yong ;
Xu, Jian ;
Tao, Zhichao ;
Wang, Hulin ;
Wang, Hong ;
Xiang, Hongwei ;
Li, Yongwang .
APPLIED CATALYSIS A-GENERAL, 2008, 345 (02) :176-184
[4]   XPS study of duplex stainless steel oxidized by oxygen atoms [J].
Donik, Crtomir ;
Kocijan, Aleksandra ;
Grant, John T. ;
Jenko, Monika ;
Drenik, Aleksander ;
Pihlar, Boris .
CORROSION SCIENCE, 2009, 51 (04) :827-832
[5]   Practical and theoretical aspects of the catalytic Fischer-Tropsch process [J].
Dry, ME .
APPLIED CATALYSIS A-GENERAL, 1996, 138 (02) :319-344
[6]   The influence of Cr precursors in the ethylene polymerization on Cr/SiO2 catalysts [J].
Gaspar, AB ;
Dieguez, LC .
APPLIED CATALYSIS A-GENERAL, 2002, 227 (1-2) :241-254
[7]   Insight into CH4 Formation in Iron-Catalyzed Fischer-Tropsch Synthesis [J].
Huo, Chun-Fang ;
Li, Yong-Wang ;
Wang, Jianguo ;
Jiao, Haijun .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2009, 131 (41) :14713-14721
[8]   Phase transformations in iron Fischer-Tropsch catalysts during temperature-programmed reduction [J].
Jin, YM ;
Datye, AK .
JOURNAL OF CATALYSIS, 2000, 196 (01) :8-17
[9]   EFFECTS OF ADDITION OF CHROMIUM, MANGANESE, OR MOLYBDENUM TO IRON CATALYSTS FOR CARBON-DIOXIDE HYDROGENATION [J].
LEE, MD ;
LEE, JF ;
CHANG, CS ;
DONG, TY .
APPLIED CATALYSIS, 1991, 72 (02) :267-281
[10]   Structure and site evolution of iron oxide catalyst precursors during the Fischer-Tropsch synthesis [J].
Li, SZ ;
Meitzner, GD ;
Iglesia, E .
JOURNAL OF PHYSICAL CHEMISTRY B, 2001, 105 (24) :5743-5750