HYDROLIQUEFACTION OF COAL CATALYZED BY TIN-COMPOUNDS

被引:4
作者
BESSON, M [1 ]
BACAUD, R [1 ]
BRODSKI, D [1 ]
BUSSIERE, P [1 ]
CHARCOSSET, H [1 ]
DJEGAMARIADASSOU, G [1 ]
OBERSON, M [1 ]
SHARMA, BK [1 ]
机构
[1] UNIV PARIS 06,REACT SURFACE & STRUCT LAB,F-75252 PARIS 05,FRANCE
关键词
catalysis; coal; hydroliquefaction;
D O I
10.1016/0016-2361(90)90255-O
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
Although tin compounds have been shown to be active in hydroliquefaction of coal, the active tin species during the liquefaction has not yet been elucidated. Some recent work suggests that metallic tin promotes the liquefaction reaction. In this study, the hydroliquefaction of French Freyming coal was investigated in a batch reactor between 350 ° and 430 °C, using non-porous SnO2 aerosol with a low particle size (15 nm) as a catalyst precursor, or presulphided tin oxide or commercial metallic tin. Chemical analysis of the liquid phase was achieved by solvent extraction in n-hexane, toluene or THF. The hydrogen consumptions (from the gas phase or from the donor solvent), were also estimated. The main experimental techniques used for catalyst characterizations were applied to the residue of hydroliquefaction: 119Sn and 57Fe Mössbauer spectrometry, X-ray diffraction and electron microscopy associated with X-ray spectrometry. Tin sulphide was generally observed as the main product with small amounts of oxidized tin species. The size of SnS particles implies sintering, possibly due to mobile tin species such as metal, although this latter could not be detected. No evidence of coking of the surface of SnS was found. In some cases the intermetallic compound FeSn2 was shown, as formed by reaction of tin with pyritic iron of the mineral matter. By comparing the results of coal conversion with those of tin characterization, the active species was thought to be SnS, on which a competitive adsorption of H2S should proceed. This results in a shift of the mode of hydrogen transfer to the coal (from H-donor solvent as opposed to hydrogen itself), as the partial pressure of H2S in H2 increased. © 1990.
引用
收藏
页码:35 / 43
页数:9
相关论文
共 28 条
[1]  
BACAUD R, 1988, SEP INT S IND APPL M
[2]  
BACAUD R, 1987, CATALYST DEACTIVATIO, P289
[3]  
BACAUD R, 1987, COAL SCI TECHNOLOGY, P255
[4]   CATALYTIC HYDROLIQUEFACTION OF COAL - ABOUT THE METHODOLOGY IN BATCH EXPERIMENTS [J].
BESSON, M ;
BACAUD, R ;
CHARCOSSET, H ;
CEBOLLABURILLO, V ;
OBERSON, M .
FUEL PROCESSING TECHNOLOGY, 1986, 12 (1-3) :91-109
[5]   EVIDENCE FOR DIRECT INTERACTION OF HYDROGEN WITH BROWN COAL IN TIM-CATALYZED REACTIONS [J].
COCHRAN, SJ ;
HATSWELL, M ;
JACKSON, WR ;
LARKINS, FP .
FUEL, 1982, 61 (09) :831-833
[6]   INTERACTIONS OF IRON AND TIN-BASED PROMOTERS DURING BROWN COAL-LIQUEFACTION [J].
COOK, PS ;
CASHION, JD .
FUEL, 1988, 67 (10) :1428-1435
[7]   SN-119 MOSSBAUER STUDY OF THE PROMOTION OF VICTORIAN BROWN COAL HYDROLIQUEFACTION BY TIN-COMPOUNDS [J].
COOK, PS ;
CASHION, JD .
FUEL, 1986, 65 (01) :146-147
[8]   MOSSBAUER STUDY OF THE TIN CHEMISTRY OCCURRING DURING THE HYDROLIQUEFACTION OF TIN-TREATED VICTORIAN BROWN COAL [J].
COOK, PS ;
CASHION, JD ;
CASSIDY, PJ .
FUEL, 1985, 64 (08) :1121-1126
[9]   EVOLUTION OF HIGHLY DISPERSED CATALYSTS DURING HYDROLIQUEFACTION OF COAL [J].
DJEGAMARIADASSOU, G ;
BESSON, M ;
BRODZKI, D ;
CHARCOSSET, H ;
HUU, TV ;
VARLOUD, J .
FUEL PROCESSING TECHNOLOGY, 1986, 12 (1-3) :143-153
[10]  
Gordon K., 1946, J I FUEL, V20, P42