In a previous study, a unified approach to the calculation of the size and
energy consumption of well-mixed fluidized bed dryers was developed. A comp
uter code was written and a parametric study undertaken to determine the ef
fects of the principal operating variables. The results were shown to depen
d on the form of the drying kinetics. The present paper describes the formu
lation of an analytical model of a well-mixed fluidized bed dryer, which ap
plies for materials that exhibit linear falling-rate drying. These material
s are typified by small hygroscopic particles, which are frequently dried i
n such equipment. Equations are presented that enable the drying time, spec
ific energy consumption, heater duty and bed area to be calculated. The pre
dictions of these equations agreed well with previously published experimen
tal findings and with the results of computer simulations for a typical sol
id (ion exchange resin) exhibiting the required drying characteristics.