A two-region model of a spouted bed gasifier devised by the present au
thors has been further developed to include an enthalpy balance. As be
fore, the present model assumes first-order reaction kinetics for the
gasification reactions and the spout is treated as a plug flow reactor
of fixed diameter with cross Bow of gas into the annulus. The annulus
region is considered to be a single plug flow reactor. Solids move in
plug flow in both annulus and spout, independent of temperature and r
eaction. The model allows predictions of axial profiles of temperature
and gas in the spout and annulus as well as exit gas compositions and
overall carbon conversion. The exit gas compositions were compared wi
th those of the previous two-region and streamtube isothermal models.
The effect of hydrodynamic parameters on model predictions are illustr
ated and a comparison made with experimental temperature profiles obta
ined in a 0.30 m diameter gasifier. (C) 1998 Published by Elsevier Sci
ence Ltd. All rights reserved.