A mathematical model of a novel industrial-scale biofilm reactor - TUR
BOFLO - was developed. The reactor is an internal circulating airlift
with rectangular cross-section. High density polyethylene granules wit
h a density of less than 1 g/cm(3) were used to support bacterial grow
th. The reactor was used for several months for nitrification of secon
dary effluent. The mathematical model consisted of three differential
mass balance equations for ammonia, dissolved oxygen (DO) and biomass.
Description of gas-liquid mass transfer was the critical part of the
model. The most successful approach was based on Higbie's penetration
theory and Kolmogorov's isotropic turbulence. (C) 1998 IAWQ. Published
by Elsevier Science Ltd.