INTERNAL CONSISTENCY OF COAL-GASIFICATION REACTIVITIES DETERMINED IN BENCH-SCALE REACTORS - EFFECT OF PYROLYSIS CONDITIONS ON CHAR REACTIVITIES UNDER HIGH-PRESSURE CO2
A. Megaritis et al., INTERNAL CONSISTENCY OF COAL-GASIFICATION REACTIVITIES DETERMINED IN BENCH-SCALE REACTORS - EFFECT OF PYROLYSIS CONDITIONS ON CHAR REACTIVITIES UNDER HIGH-PRESSURE CO2, Fuel, 77(13), 1998, pp. 1411-1420
Relationships between char preparation conditions and CO2-gasification
conversions have been examined using a wire-mesh, a fluidised-bed and
a 'hot-rod' (fixed-bed) reactor. Conversions from the direct gasifica
tion of untreated coal have been compared with those from the gasifica
tion of chars prepared: (i) in-situ under helium in each reactor, befo
re switching over to CO2; and (ii) from gasification in all three reac
tors of a char sample, pre-prepared in the fixed bed reactor. Conversi
ons from direct gasification were slightly higher than experiments whe
re samples were first pyrolysed in situ and gasified under CO2 in the
same reactor. In some cases, conversions were within experimental erro
r. Under these conditions and within several percentage points, the py
rolysis and gasification steps may be considered as additive. Lower ov
erall conversions observed in the hot-rod reactor have been attributed
to the combined effect of: (i) formation of a low reactivity char-owi
ng to tar-solids contact leading to secondary char deposition; and (ii
) poor contact between char and the reactive gas. in the wire-mesh and
the fluidised-bed reactors, direct CO2-gasification conversions were
considerably larger than those determined using the common sample of c
har, pre-prepared in the hot-rod (fixed-bed) reactor. This sharp drop
in overall conversion shows that care must be taken in interpreting re
activity data from 'two-reactor, two-step' procedures where char prepa
ration conditions are not identical to those of the gasification step.
A broadly linear relationship has been observed between conversions f
rom a pilot plant reactor and direct CO2-gasification in the bench-sca
le high-pressure wire-mesh reactor. Despite differences between operat
ing parameters in the two reactors, the results suggest that data from
the wire-mesh reactor may be successfully used to compare relative co
al reactivities under pilot-plant,gasification conditions. (C) 1998 El
sevier Science Ltd. All rights reserved.