A process model based on the ASPEN PLUS process simulator has been develope
d for a novel Compartmented Fluidised Bed Coal Gasifier (CFBCG) process. A
distinctive feature of the model is that a number of user-written models ha
ve been incorporated within the ASPEN Frame to describe processes of hydrod
ynamics, coal combustion and gasification, solid circulation, entrainment a
nd elutriation, and particle size distribution in the CFBCG and energy loss
to the environment from the reactor. In general, most of the predictions o
f the model is in a reasonable agreement with the experimental results. How
ever, some unmeasurable operating parameters at hot state in the experiment
s lead to some difficulties to verify the model in these instances against
real data. Uncertainty related to volatile combustion mechanisms in fluidis
ed beds in the literature also influences the model accuracy. Nevertheless
the ASPEN based model provides a convenient vehicle for the further develop
ment of this new process, by allowing the physical insights into mechanisms
, which would be difficult and expensive to investigate experimentally. The
simulations indicate that the CFBCG concept is sound and further developme
nt is needed to improve the operatibility of the process before practical i
mplementation to produce high quality synthesis gas from the CFBCG might be
considered.