The tar content of the product gases from gasification of biomass is one of
the major factors affecting the subsequent process stages. In this work, e
volution profiles of the main tar constituents, i.e. benzene, toluene, inde
ne, naphthalene and phenol were obtained during about 1 h gasification runs
of biomass and coal in a pressurised fluidised-bed at 700 and 900 degrees
C, 0.4 MPa. Sampling and analysis was achieved, using the solid-phase adsor
ption (SPA) method, previously developed in our laboratory. Our main object
ives were: (1) to illustrate the usefulness of the SPA method; (2) to shed
new light on the main factors governing tar evolution. It was found that te
mperature and the type of feedstock used mainly affected tar yields. For bo
th biomass and coal the concentration of tar products decreased with increa
sing run time at a rate that was fastest initially. This behaviour, which w
as much more pronounced for coal, provides evidence that char catalytically
affects tar evolution. Accordingly, char accumulates in the bed to a vario
us extent depending on fuel and gradually approaching steady state. Biomass
char, contrary to coal char, is readily oxidised during gasification, and
thus only small steady-state amounts are available to catalyse tar cracking
reactions. (C) 1999 Elsevier Science Ltd. All rights reserved.