The hydrogenation of 24 coals (LV bituminous to lignite) in the presen
ce of Mo was studied. The hydrogenation temperatures were 300, 350 and
400 degrees C, the hydrogen pressures 5 and 10 MPa, and the reaction
time 30 min. At 300 degrees C the Mo salts deposited on the coals do n
ot decompose to the active MoS2 state, so the hydrogenation process is
not significantly different from that in the absence of a catalyst an
d is influenced by the ease of diffusion, with a consequent increase i
n conversion with increasing macropore volume. At 350 and 400 degrees
C, MoS2 acts as a good catalyst and conversion is much greater than in
the absence of a catalyst. Under these conditions, opening of pores i
n the coals has been detected as conversion increases; micropores deve
lop to macropores in such a manner that the MoS2 particles can penetra
te progressively into pores originally inaccessible, so an increase in
the micropore volume or surface area favours conversion. This pore-op
ening is accompanied by an increase in cross-link density. At 5 MPa of
H-2, and increasing with temperature, some of the radicals formed are
incorporated into the macromolecular structure by repolymerization re
actions which result in blockage of the microporosity.