Laboratory-scale coking of coal-petroleum mixtures in sealed reactors

被引:8
作者
Fickinger, AE [1 ]
Badger, MW [1 ]
Mitchell, GD [1 ]
Schobert, HH [1 ]
机构
[1] Penn State Univ, Energy Inst, University Pk, PA 16802 USA
关键词
D O I
10.1021/ef030187q
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
Three highly fluid bituminous coals-from the Pittsburgh, Powellton, and Eagle seams-were reacted with atmospheric resid and decant oil in microautoclave reactors under nitrogen at temperatures of 450-500 degreesC. This exploratory study is the first step in evaluating the prospects for adding coal to delayed cokers to obtain coal-derived components in the liquid product. Subsequent hydrotreating (not studied here) of the liquid would produce a jet fuel with good stability toward pyrolytic decomposition. Coal-derived components appear in the oil fraction from coal-resid reactions at 465 degreesC. This reaction temperature represents a "coke jump", in which the yield of solid, as a function of temperature, increases dramatically. This behavior is not observed when the individual feedstocks are reacted alone. Further evidence for coal-petroleum interactions in this system is exhibited by the fact that (i) the product slates from the co-coking reactions are not linear combinations of the products from the feedstocks reacted individually and (ii) the fluidity profiles of the Powellton-resid mixtures are similar to those for two interacting coking coals. The effect of changing coal with the same petroleum feedstock is minimal, although the coals are very similar in composition and properties. In contrast, changing from resid to decant oil with the same coal causes major changes in the product slate.
引用
收藏
页码:976 / 986
页数:11
相关论文
共 53 条
[1]  
*AM SOC TEST MAT, 1998, PETR PROD LUBR FOSS
[2]   Relationship between the formation of aromatic compounds and solid deposition during thermal degradation of jet fuels in the pyrolytic regime [J].
Andrésen, JM ;
Strohm, JJ ;
Sun, L ;
Andresen, JM .
ENERGY & FUELS, 2001, 15 (03) :714-723
[3]  
[Anonymous], 1963, CHEM COAL UTILIZATIO
[4]   Structural ordering of Pennsylvania anthracites on heat treatment to 2000-2900°C [J].
Atria, JV ;
Rusinko, F ;
Schobert, HH .
ENERGY & FUELS, 2002, 16 (06) :1343-1347
[5]   COPROCESSING TECHNOLOGY DEVELOPMENT IN CANADA [J].
BOEHM, FG ;
CARON, RD ;
BANERJEE, DK .
ENERGY & FUELS, 1989, 3 (02) :116-119
[6]  
Burgess C., 1997, P 9 INT C COAL SCI, V3, P1373
[7]   Effect of coal characteristics and molybdenum sulfide catalyst on conversions and yields of heavy products from liquefaction in phenanthrene [J].
Burgess, CE ;
Schobert, HH .
ENERGY & FUELS, 1996, 10 (03) :718-725
[8]   Relationship of coal characteristics determined by pyrolysis gas chromatography mass spectrometry and nuclear magnetic resonance to liquefaction reactivity and product composition [J].
Burgess, CE ;
Schobert, HH .
ENERGY & FUELS, 1998, 12 (06) :1212-1222
[9]   Direct liquefaction for production of high yields of feedstocks for specialty chemicals or thermally stable jet fuels [J].
Burgess, CE ;
Schobert, HH .
FUEL PROCESSING TECHNOLOGY, 2000, 64 (1-3) :57-72
[10]  
BURGESS CE, 1994, THESIS PENNSYLVANIA