Catalytic activity of NiMo sulfide supported on a particular carbon black of hollow microsphere in the liquefaction of a subbituminous coal

被引:33
作者
Sakanishi, K
Hasuo, H
Kishino, M
Mochida, I
Okuma, O
机构
[1] KYUSHU UNIV,INST ADV MAT STUDY,KASUGA,FUKUOKA 816,JAPAN
[2] KOBE STEEL LTD,POLYMER & CHEM TECHNOL LAB,KOBE,HYOGO 65122,JAPAN
关键词
D O I
10.1021/ef950096w
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
The liquefaction of Wyoming coal (subbituminous coal) was investigated with an autoclave of 50 mt capacity, using Ketjen Black (KB)-supported NiMo catalyst, which has higher hydrogenation activity of 1-methylnaphtalene than a commercial NiMo/Al(2)O3. KB-supported NiMo catalyst gave the oil and oil plus asphaltene yield of 54 and 69% under reaction conditions of 440 degrees C, 60 min, and 13 MPa. These yields were much higher than those of a commercial NiMo/Al2O3 and synthesized FeS2 catalysts. The KB-supported NiMo catalyst was found to be recovered from the solid products using polar solvents such as THF because it is highly dispersed in liquid products due to its low specific gravity and the hydrophobic property of its surface. It was also found that KB-supported NiMo catalyst suffered the least deactivation by coke formation and mineral matter deposition because the recovered catalyst as THFI residue appeared to regenerate the activity to a level similar to the fresh catalyst.
引用
收藏
页码:216 / 219
页数:4
相关论文
共 23 条
[1]   BEHAVIOR OF TETRAHYDROQUINOLINE IN TEMPERATURE-STAGED LIQUEFACTION OF SUBBITUMINOUS COAL [J].
BURGESS, CE ;
SCHOBERT, HH .
FUEL, 1991, 70 (03) :372-379
[2]   HYDRODENITROGENATION OF QUINOLINE AND COAL USING PRECIPITATED TRANSITION-METAL SULFIDES [J].
CURTIS, CW ;
CAHELA, DR .
ENERGY & FUELS, 1989, 3 (02) :168-174
[3]  
DERBYSHIRE FJ, 1988, CATALYTIC COAL LIQUE
[4]   IRON COMPOUNDS AND IRON CATALYSTS - ACTIVITY IN REACTIONS RELEVANT TO DIRECT COAL-LIQUEFACTION [J].
FARCASIU, M ;
SMITH, C ;
PRADHAN, VR ;
WENDER, I .
FUEL PROCESSING TECHNOLOGY, 1991, 29 (03) :199-208
[5]   COMPARATIVE-STUDY OF ALUMINA-SUPPORTED AND CARBON-SUPPORTED CATALYSTS FOR HYDROGENOLYSIS AND HYDROGENATION OF MODEL COMPOUNDS AND COAL-DERIVED LIQUIDS [J].
GROOT, CK ;
DEBEER, VHJ ;
PRINS, R ;
STOLARSKI, M ;
NIEDZWIEDZ, WS .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1986, 25 (04) :522-530
[6]  
HILLEROVA E, 1991, APPL CATAL, V67, P231
[7]   HIGHLY DISPERSED COAL-LIQUEFACTION CATALYSTS [J].
HIRSCHON, AS ;
WILSON, RB .
FUEL, 1992, 71 (09) :1025-1031
[8]   NI EXAFS STUDIES OF THE NI-MO-S STRUCTURE IN CARBON-SUPPORTED AND ALUMINA-SUPPORTED NI-MO CATALYSTS [J].
LOUWERS, SPA ;
PRINS, R .
JOURNAL OF CATALYSIS, 1992, 133 (01) :94-111
[9]   ROLES OF CATALYST SUPPORT IN THE SELECTIVE HYDROTREATMENT OF A SOLVENT REFINED COAL [J].
MOCHIDA, I ;
OISHI, T ;
KORAL, Y ;
FUJITSU, H .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1984, 23 (02) :203-205
[10]   Catalysis in coal liquefaction [J].
Mochida, I ;
Sakanishi, K .
ADVANCES IN CATALYSIS, VOL 40, 1994, 40 :39-85