New applications of expanded perlite in the building industry lead to a gro
wing demand For process optimization for the expansion of perlite. Perlite
expanders aim to adapt their furnaces and/or furnace operation conditions i
n order to attain more flexibility to produce different expanded perlite qu
alities. A way to examine the possibilities of an existing installation is
the numerical simulation of the perlite expansion process in that installat
ion. The two-phase flow field and combustion in the furnace can be modelled
by using currently available Computational Fluid Dynamics (CFD) codes. The
only problem is the modelling of the expansion process. which changes the
particle size and thus influences the two-phase flow calculations.
In this paper the authors propose a physical model for the simulation of th
e expansion of perlite. This model is based on the results of fundamental s
tudies concerning the expansion phenomenon. It relies on the calculation of
particle temperature and viscosity and thus takes into account the must in
fluential parameters For perlite expansion. It allows the calculation of th
e perlite particle size as a function of time or of the particle's trajecto
ry inside a furnace. Particle size statistics of the expanded product can b
e determined in that way. The model has been validated by comparison with e
xperimental results from laboratory and industrial measurements.