A dynamic mathematical model of prefermentation is presented. Prefermentati
on is becoming an increasingly popular unit operation in biological nutrien
t removal wastewater treatment plants. The aim of the prefermenter model is
to provide a tool for optimisation of prefermenter design and operation. M
odel assumptions. equations and parameters are detailed. The major specific
ation for the prefermenter model is that it is relatively simple, but can s
till describe the effects of the main design and operating parameters on vo
latile fatty acid (VFA) production in prefermenters. The model is verified
by comparing its prediction with experimental data presented in the literat
ure. Predicted and measured steady-state effluent VFA, soluble COD and ammo
nia-N concentrations are compared for varying hydraulic and solids residenc
e times. The correspondence between experimental data and model prediction
is good. (C) 1999 Elsevier Science Ltd. All rights reserved.