Experiments carried out in an indirectly heated biomass gasifier successful
ly demonstrated that throughput and gas heating value could be increased by
using a latent heat ballast. A mathematical model describing heat transfer
and chemical reaction in the system was developed. The heat transfer submo
del is accurate to within 13 K for both ballasted and unballasted scenarios
. However, the chemical submodel, based on thermodynamic equilibrium calcul
ations, proved inadequate and underpredicted cooling times during the pyrol
ysis phase of the process by about 50%. Improvement was made by substitutin
g the measured product gas composition for the calculated gas composition.
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