Fluidized bed and rotary dryers are two popular types of dryers utiliz
ed in almost every area of drying. In this study, both dryers are anal
ysed regarding their design and operational performance, so that they
could be compared in a straightforward way. The mathematical models de
scribing the convective drying process were evaluated for both types o
f dryers. Design procedures aiming at the determination of optimum siz
ing and operational characteristics for each type involved were carrie
d out by appropriately optimizing the total annual cost of each struct
ure for a given production capacity. Both dryer types were compared ex
plicitely by evaluating optimum configurations for a wide range of pro
duction capacity values. Once the dryer sizing parameters are defined,
its operational performance can be evaluated by comparing the optimum
operational cost versus production capacity for predefined optimum de
signed structures. Rotary dryers rum out to be rather expensive compar
ed to fluidized bed dryers, regarding design. On operational grounds,
however, it is the other way around, due to the understandably favored
heat transfer achieved in rotary dryers. Characteristic examples cove
ring a wide range of materials - from food products to inorganic miner
als - are included in order to demonstrate the performance of each pro
cess as well as the effectiveness of the proposed approach.