Sf. Zhang et al., EFFECT OF COAL RANK ON HYDROCRACKING REACTIVITIES OF PRIMARY COAL EXTRACTS PREPARED IN A FLOWING-SOLVENT REACTOR - THE ARGONNE PREMIUM COALSAMPLE SET, Fuel, 75(13), 1996, pp. 1557-1567
Catalytic hydrocracking experiments were performed using 'primary' coa
l extracts, to establish correlations between coal rank and extract re
activities, in isolation from secondary effects associated with the co
al dissolution step. A strong correlation was obtained between liquefa
ction conversion and carbon content of the original coals: R(2)=0.96.
Strong correlations were also found between hydrocracking conversions
of material boiling >450 degrees C in the extracts and carbon content:
for 30 and 60 min hydrocracking reaction times, R(2)=0.92 and 0.93 re
spectively. The data indicate that the 450 degrees C b.p. material tak
en into solution during extraction of higher-rank coals is more diffic
ult to hydrocrack. Large shifts were observed between s.e.c. profiles
of liquefaction extracts and their corresponding hydrocracked (30 min)
products, including the apparent disappearance of most material appea
ring under the excluded peaks. The extension of reaction time from 30
to 60 min gave rise to much less significant changes. U.v. fluorescenc
e (u.v.-f.) spectra also showed that the first 30 min of hydrocracking
gave rise to more significant structural changes than subsequent reac
tion did. The use of reaction times <30 min might allow more detailed
information to be gleaned about the relative rates of coal extract hyd
rocracking as a function of coal rank. Matrix-assisted laser desorptio
n ionization mass spectrometry (MALDI-m.s.) was used to confirm (1) th
e presence of very large molecular mass materials in the extracts and
(2) the very significant reduction in molecular masses achieved by the
hydrocracking process. The results clearly show that in two-stage liq
uefaction processes, the overall yield of distillates (b.p. <450 degre
es C) is strongly influenced by coal rank. Copyright (C) 1996 Elsevier
Science Ltd.