An investigation of the thermal drying of lignite has been carried out, by
using an indirect heat pilot rotary drum. The process aims at the productio
n of dry lignite and clean steam as part of a gasification procedure. Both
flighted and bare drum modes have been employed. Temperature profiles along
the dryer length, the amount of evaporation (moisture conversion) and the
solids residence time distribution (RTD) were measured. A non-isothermal mo
del was tested under three different regimes of solids flow. Model integrat
ion, by taking account of experimental amount of evaporation at dryer exit
and temperature profiles along the dryer length, has been utilized in the v
alidation of drying kinetics and heat transfer correlations. Model predicti
ons compare satisfactorily with the operating data of an indirect heat indu
strial lignite dryer. Overall heat transfer coefficients of the pilot rotar
y dryer were found to agree well with those reported for direct heat dryers
.