K. Sakanishi et al., SOLVENT-FREE LIQUEFACTION OF BROWN AND SUBBITUMINOUS COALS USING NIMOSULFIDE CATALYST SUPPORTED ON CARBON NANOPARTICLES, Energy & fuels, 12(2), 1998, pp. 284-288
Single-and two-stage liquefaction processes of Yallourn (YLC), South B
anko (SEC), and Tanitoharum (THC) coals were performed in an autoclave
of 50-mL capacity at variable solvent (tetralin)/coal ratios from 0 t
o 1.5 under the reaction hydrogen pressure of 15 MPa, using NiMo sulfi
de supported on carbon nanoparticles or commercial NiMo/alumina and sy
nthetic pyrite catalysts. Although the oil yield decreased very much w
ith all the catalysts by reducing the amount of solvent to zero, the N
iMo/carbon catalyst gave much higher oil yields of 52 and 64%, respect
ively, in the single-stage (450 degrees C, 60 min) and two-stage (360
degrees C, 60 min; 450 degrees C, 60 min) liquefaction under the solve
nt-free conditions compared with the yield of around 40% by the other
two catalysts in both single-and two-stage liquefaction under the same
conditions. The oil yield depended on the coal species under the solv
ent-free conditions, being in the order of SBC > YLC > THC regardless
of the reaction conditions. SBC provided the highest oil yields of 60
and 68% in the single-and two-stage liquefaction, respectively, reflec
ting its higher reactivity and lower gas yield. THC gave the lowest oi
l yields among the coals examined, although the oil yield reached 60%
by the two-stage Liquefaction even under the solvent-free conditions.
The oil produced with NiMo/carbon catalyst carried lighter fractions i
n the boiling range 100-300 degrees C than those with the other cataly
sts regardless of the reaction conditions and coal species. Such excel
lent performance of the NiMo/carbon catalyst reflects its higher hydro
genation activity as well as the high dispersion on the coal surface a
t the initial stage of coal liquefaction, suppressing the retrogressiv
e reactions. It is confirmed that the major portion of solid coal was
solubilized during the heating and the initial stage to work as the se
lf-producing solvent under the solvent-free reaction conditions. The d
esign of coal liquefaction with the least use of solvent is discussed
for the higher productivity.