Supercritical-phase process for selective synthesis of heavy hydrocarbons from syngas on cobalt catalysts

被引:33
作者
Yan, SR
Fan, L
Zhang, ZX
Zhou, JL
Fujimoto, K
机构
[1] Chinese Acad Sci, Inst Coal Chem, Taiyuan 030001, Shanxi, Peoples R China
[2] Univ Tokyo, Sch Engn, Dept Appl Chem, Bunkyo Ku, Tokyo 113, Japan
关键词
supercritical fluid; FT synthesis; medium-size 1-olefin addition; Co/SiO2; catalyst;
D O I
10.1016/S0926-860X(98)00049-0
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
Supercritical-phase Fischer-Tropsch synthesis co-fed with 1-tetradecene was carried out over Co/SiO2 catalysts. It was found that a supercritical fluid could extract the product from the catalyst bed efficiently, and as a result, the mass transfers for both reactants and products were enhanced, 1-Tetradecene added as a chain initiator could participate in the chain growth process. This consequently increased the rate of formation of hydrocarbons larger than C-14 Significantly, and decreased the yield of C-1-C-13 hydrocarbons, leading to a flatter carbon number distribution of product than that obtained without olefin addition. In addition, wax composition analysis also showed that the average molecular weight and degree of saturation of wax increased due to addition of 1-tetradecene. The effects of catalyst pore size, concentration of co-fed 1-olefin, and CO/H-2 ratio of syngas were investigated. (C) 1998 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:247 / 254
页数:8
相关论文
共 13 条
[1]   SUPERCRITICAL PHASE FISCHER-TROPSCH SYNTHESIS - CATALYST PORE-SIZE EFFECT [J].
FAN, L ;
YOKOTA, K ;
FUJIMOTO, K .
AICHE JOURNAL, 1992, 38 (10) :1639-1648
[2]   REACTIONS OF SELECTED 1-OLEFINS AND ETHANOL ADDED DURING THE FISCHER-TROPSCH SYNTHESIS [J].
HANLON, RT ;
SATTERFIELD, CN .
ENERGY & FUELS, 1988, 2 (02) :196-204
[3]   MECHANISTIC ASPECTS OF THE FORMATION OF HYDROCARBONS AND ALCOHOLS FROM CO HYDROGENATION [J].
HINDERMANN, JP ;
HUTCHINGS, GJ ;
KIENNEMANN, A .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1993, 35 (01) :1-127
[4]   SELECTIVITY CONTROL AND CATALYST DESIGN IN THE FISCHER-TROPSCH SYNTHESIS - SITES, PELLETS, AND REACTORS [J].
IGLESIA, E ;
REYES, SC ;
MADON, RJ ;
SOLED, SL .
ADVANCES IN CATALYSIS, VOL 39, 1993, 39 :221-302
[5]   ESTIMATES OF RATE COEFFICIENTS FOR ELEMENTARY PROCESSES OCCURRING DURING FISCHER-TROPSCH SYNTHESIS OVER RU TIO2 [J].
KOMAYA, T ;
BELL, AT .
JOURNAL OF CATALYSIS, 1994, 146 (01) :237-248
[6]   Non-ASF product distributions due to secondary reactions during Fischer-Tropsch synthesis [J].
Kuipers, EW ;
Scheper, C ;
Wilson, JH ;
Vinkenburg, IH ;
Oosterbeek, H .
JOURNAL OF CATALYSIS, 1996, 158 (01) :288-300
[7]   CHAIN-LENGTH DEPENDENCE OF ALPHA-OLEFIN READSORPTION IN FISCHER-TROPSCH SYNTHESIS [J].
KUIPERS, EW ;
VINKENBURG, IH ;
OOSTERBEEK, H .
JOURNAL OF CATALYSIS, 1995, 152 (01) :137-146
[8]  
NAKAMURA R, 1988, P 9 INT C CAT OTT, V2, P759
[9]   DIFFUSION LIMITATIONS IN FISCHER-TROPSCH CATALYSTS [J].
POST, MFM ;
VANTHOOG, AC ;
MINDERHOUD, JK ;
SIE, ST .
AICHE JOURNAL, 1989, 35 (07) :1107-1114
[10]   FISCHER-TROPSCH SYNTHESIS - C-14 TRACER STUDY OF ALKENE INCORPORATION [J].
TAU, LM ;
DABBAGH, HA ;
DAVIS, BH .
ENERGY & FUELS, 1990, 4 (01) :94-99