A yeast reactor was proposed to treat highly concentrated acidified ef
fluents of the food industry. The strain Candida utilis was selected a
nd operated in batch or continuously in a perfectly mixed reactor with
acetic acid, propionic acid or butyric acid as the sole carbon source
while the pH was maintained at 3.5 to prevent most bacterial contamin
ation. The obtained 97% TOC abatement through the continuous reactor w
as independent of inlet concentration and space-time if the space-time
is higher than a critical wash-out value. Such large loading rates as
30 kg TOC/m(3) . day could be treated. The reaction rate was inhibite
d by the substrate concentration which explained a steady outlet TOC c
oncentration when the reactor was operated under the critical space-ti
me value. The sludge production was of the same order of magnitude as
in a conventional activated sludge reactor. The solids were easily flo
cculated and settled after neutralizing the suspension. Copyright (C)
1996 Elsevier Science Ltd