This paper presents a numerical simulation and experimental validation of a
spray dryer using superheated steam instead of air as drying medium, model
ized with a computational fluid dynamics (CFD) code. The model describes mo
mentum, heat and mass transfer between two phases - a discrete phase of dro
plets and a continuous gas phase - through a finite volume method. For the
simulation, droplet size distribution is represented by 6 discrete classes
of diameter, fitting to the experimental distribution injected from the noz
zle orifice, taking into account their peculiar shrinkage during drying.
This model is able to predict the most important features of the dryer : fi
elds of gas temperature and gas velocity inside the chamber, droplets traje
ctories and eventual deposits on to the wall. The results of simulation are
compared to a pilot scale dryer, using water. In the absence of risk of po
wder ignition in steam, we have tested rather high steam inlet temperature
(973K), thus obtaining a high volumic efficiency. The model is validated by
comparison between experimental and predicted values of temperature inside
the chamber, verifying the coupling between the 3 different types of trans
fer without adjustment. This type of model can be used for chamber design,
or scale up. Using superheated steam instead of air in a spray dryer can al
low a high volumic evaporation rate (20 kg.h(-1).m(-3)), high energy recove
ry and better environment control.