Id. Rodriguez et al., LIQUEFACTION BEHAVIOR OF A SPANISH SUBBITUMINOUS - A COAL UNDER DIFFERENT CONDITIONS OF HYDROGEN AVAILABILITY, Fuel processing technology, 58(1), 1998, pp. 17-24
A Spanish subbituminous A coal was liquefied in a 250-ml autoclave for
1 h, at 17 MPa hydrogen pressure and 400 rpm stirring speed. The liqu
id products were fractionated into oils, asphaltenes, and preasphalten
es using pentane, toluene and THF as extractive solvents. The effect o
f hydrogen availability on liquefaction yields was explored using diff
erent tetralin:coal ratios under different temperatures. The results a
re compared with those obtained in earlier studies [1,2], under differ
ent hydrogen pressures and tetralin:coal ratios, and with other solven
ts and with catalysts. Total conversion, asphaltenes, preasphaltenes a
nd oils increase while gases decrease when the tetralin:coal ratio is
raised, not observing further conversion over 2:1, 3:1, 4:1 and 6:1 ra
tios, at 400, 425, 450 and 475 degrees C, respectively. Retrogressive
reactions are produced at 475 degrees C for tetralin:coal ratios under
4:1 but not for higher ones. In order to obtain the highest conversio
n (approximate to 84%), which coincides with vitrinite + exinite conte
nt, 475 degrees C and 6:1 or higher tetralin:coal ratios have to be us
ed. Such or higher conversions, can be obtained with more appropriate
operating conditions (425 degrees C, 3:1 solvent:coal ratio) if better
solvents or active catalysts are used. (C) 1998 Elsevier Science B.V.
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