Effect of preparation and operation conditions on the catalytic performance of cobalt-based catalysts for light olefins production

被引:33
作者
Feyzi, Mostafa [1 ]
Khodaei, Mohammad Mehdi [1 ]
Shahmoradi, Jahangir [1 ]
机构
[1] Razi Univ, Fac Chem, Kermanshah, Iran
关键词
Support; Promoter; Light olefins; Operational condition; FISCHER-TROPSCH SYNTHESIS; RAY ABSORPTION-SPECTROSCOPY; CO HYDROGENATION; MANGANESE OXIDE; SYNTHESIS GAS; IRON; SUPPORT; SELECTIVITY; DISPERSION; PROMOTION;
D O I
10.1016/j.fuproc.2011.09.021
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Cobalt-based catalysts were prepared by precipitation method. This research investigated the effects of different supports cobalt loading, promoters, loading of promoters and calcination conditions on the catalytic performance of cobalt catalysts for Fisher-Tropsch synthesis (FTS). It was found that the catalyst containing 40 wt.% Co/TiO2 promoted with 6 wt.% Zn was an optimal catalyst for the conversion of synthesis gas to hydrocarbons especially light olefins. The activity and selectivity of optimal catalyst were studied in different operational conditions. The results showed that the best operational conditions were the H-2/CO reversible arrow 2/1 molar feed ratio at 240 degrees C and GHSV = 1100 h(-1) under atmospheric pressure. Characterization of catalysts were carried out by using X-ray diffraction (XRD), thermal gravimetric analysis (TGA), hydrogen temperature program reduction (H-2-TPR), N-2 physisorption measurements such as Brunauer-Emmett-Teller (BET) and Barrett-Joyner-Halenda (BJH) methods. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:90 / 98
页数:9
相关论文
共 41 条
[1]  
Anderson RB., 1984, FISCHER TROPSCH SYNT
[2]   SELECTIVE SYNTHESIS OF ETHYLENE FROM SYNTHESIS GAS OVER HYBRID CATALYST SYSTEM [J].
ARAKAWA, H ;
KIYOZUMI, Y ;
SUZUKI, K ;
TAKEUCHI, K ;
MATSUZAKI, T ;
SUGI, Y ;
FUKUSHIMA, T ;
MATSUSHITA, S .
CHEMISTRY LETTERS, 1986, (08) :1341-1342
[3]   EFFECTS OF MANGANESE OXIDE AND SULFATE ON OLEFIN SELECTIVITY OF IRON SUPPORTED CATALYSTS IN THE FISCHER-TROPSCH REACTION [J].
BARRAULT, J ;
FORQUY, C ;
PERRICHON, V .
APPLIED CATALYSIS, 1983, 5 (01) :119-125
[4]   Water-gas-shift kinetics in the iron-based low-temperature Fischer-Tropsch synthesis [J].
Botes, F. Gideon .
APPLIED CATALYSIS A-GENERAL, 2007, 328 (02) :237-242
[5]   X-RAY ABSORPTION-SPECTROSCOPY, X-RAY PHOTOELECTRON-SPECTROSCOPY, AND ANALYTICAL ELECTRON-MICROSCOPY STUDIES OF COBALT CATALYSTS .1. CHARACTERIZATION OF CALCINED CATALYSTS [J].
CASTNER, DG ;
WATSON, PR ;
CHAN, IY .
JOURNAL OF PHYSICAL CHEMISTRY, 1989, 93 (08) :3188-3194
[6]  
COOPER ME, 1990, APPL CATAL, V57, P5
[7]  
Cornils B, 2000, CATALYSIS A Z CONCIS
[8]   Effects of promoters and calcination conditions on the catalytic performance of iron-manganese catalysts for Fischer-Tropsch synthesis [J].
Feyzi, Mostafa ;
Irandoust, Mohsen ;
Mirzaei, Ali Akbar .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (05) :1136-1143
[9]   KINETIC-STUDIES ON THE FISCHER-TROPSCH SYNTHESIS FOR ELUCIDATION OF THE EFFECT OF ALKALI AS PROMOTOR IN IRON CATALYSTS [J].
GAUBE, J ;
HERZOG, K ;
KONIG, L ;
SCHLIEBS, B .
CHEMIE INGENIEUR TECHNIK, 1986, 58 (08) :682-683
[10]  
Griboval-Constant A, 2002, STUD SURF SCI CATAL, V144, P609