Optimization of two-stage liquefaction of Tanito Harum coal with FeNi catalyst supported on carbon black

被引:11
作者
Priyanto, U
Sakanishi, K
Okuma, O
Murti, SDS
Watanabe, I
Korai, Y
Mochida, I [1 ]
机构
[1] Kyushu Univ, Inst Mat Study, Kasuga, Fukuoka 8168580, Japan
[2] Natl Inst Resources & Environm, Tsukuba, Ibaraki 3058569, Japan
[3] New Ind Res Org, Chuo Ku, Kobe, Hyogo 6500047, Japan
关键词
D O I
10.1021/ef0002647
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
Two-stage liquefaction of Tanito Harum coal (Indonesian sub-bituminous coal) was examined in an autoclave of 50 mt capacity at various temperatures for the first stage and various reaction times for the first and second stages under the hydrogen pressure of 15 MPa, using Fe(10 wt %)Ni(10 wt %) catalyst supported on carbon nanoparticles (Ketjen Black:KB). When the total reaction time in the first and second stages was fixed to 120 min, the best conditions of two stage liquefaction were at 380 degreesC for 15 min in the first stage and then at 450 degreesC for 105 min in the second stage at a hydrogen pressure of 15 MPa, providing the maximum oil yields of 80 and 66 wt % (daf coal base) with or without H-donor solvent, respectively. The results also showed that these conditions produced fewer amounts of hydrocarbon gases and lower sulfur content in the oil. The conversion of II-donor solvent (tetralin) after the liquefaction was much lower (13%) than that of the single-stage liquefaction (21%). In addition, the residue yield was much lower (9%) than that of the single-stage (15%) in the solvent-free liquefaction. It is confirmed that prolonged reaction time in the second stage is more favorable than in the first stage. The effects of the first-stage (low temperature) liquefaction both with and without solvent are discussed to explain the optimum conditions of two-stage liquefaction.
引用
收藏
页码:856 / 862
页数:7
相关论文
共 25 条
[1]  
[Anonymous], 1980, COAL LIQUEFACTION CH
[2]   Liquefaction studies of some Indonesian low rank coals [J].
Artanto, Y ;
Jackson, WR ;
Redlich, PJ ;
Marshall, M .
FUEL, 2000, 79 (11) :1333-1340
[3]   COAL-LIQUEFACTION BY MOLYBDENUM CATALYZED HYDROGENATION IN THE ABSENCE OF SOLVENT [J].
DERBYSHIRE, FJ ;
DAVIS, A ;
LIN, R ;
STANSBERRY, PG ;
TERRER, MT .
FUEL PROCESSING TECHNOLOGY, 1986, 12 (1-3) :127-141
[4]  
DERBYSHIRE FJ, 1988, CATALYSIS COAL LIQUE
[5]   Effects of catalytic activity and solvent composition on two-stage coal liquefaction [J].
Hasuo, HU ;
Sakanishi, K ;
Taniguchi, H ;
Kishino, M ;
Mochida, I .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1453-1457
[6]   Nickel molybdate-catalysed hydrogenation of brown coal without solvent or added sulfur [J].
Hulston, CKJ ;
Redlich, PJ ;
Jackson, WR ;
Larkins, FP ;
Marshall, M .
FUEL, 1996, 75 (12) :1387-1392
[7]   Thermal cracking of coal residues: Kinetics of asphaltene decomposition [J].
Martinez, MT ;
Benito, AM ;
Callejas, MA .
FUEL, 1997, 76 (09) :871-877
[8]   Progresses of coal liquefaction catalysts in Japan [J].
Mochida, I ;
Sakanishi, K ;
Suzuki, N ;
Sakurai, M ;
Tsukui, Y ;
Kaneko, T .
CATALYSIS SURVEYS FROM JAPAN, 1998, 2 (01) :17-30
[9]   A MULTISTAGE COAL-LIQUEFACTION PROTOTYPE [J].
MOCHIDA, I ;
SAKANISHI, K ;
KORAI, Y ;
FUJITSU, H .
FUEL PROCESSING TECHNOLOGY, 1986, 14 :113-124
[10]   DESIGN OF RECOVERABLE CATALYSTS FOR A MULTISTAGE COAL-LIQUEFACTION PROCESS [J].
MOCHIDA, I ;
SAKANISHI, K ;
SAKATA, R ;
HONDA, K ;
UMEZAWA, T .
ENERGY & FUELS, 1994, 8 (01) :25-30