The operation performance of a single and two (in series) laboratory UASB r
eactors (working volume of 2.71, recycle ratio varied from 1:1 to 1:18) tre
ating diluted wine vinasse was investigated under psychrophilic conditions
(4-10 degreesC). For a single UASB reactor seeded with granular sludge, the
average organic loading rates (OLR) applied were 4.7, 3.7 and 1.7 g COD/l/
d (hydraulic retention times (HRTs) were around 1 d) at 9-11, 6-7 and 4-5 d
egreesC, respectively. The average total COD removal for preacidified vinas
se wastewater was around 60% for all the temperature regimes tested. For tw
o UASB reactors in series, the average total COD removal for treatment of n
on-preacidified wastewater exceeded 70% (the average OLRs for a whole syste
m were 2.2, 1.8 and 1.3 g COD/l/d under HRTs of 2 days at 10, 7 and 4 degre
esC, respectively). In situ determinations of kinetic sludge characteristic
s (V-m and K-m) revealed the existence of substantial mass-transfer limitat
ions for the soluble substrates inside the reactor sludge bed. Therefore an
application of higher recycle rations is essential for enhancement of UASB
pre-treatment under psychrophilic conditions. The produced anaerobic efflu
ents were shown to be efficiently post-treated aerobically - final effluent
COD concentrations were around 0.1 g/l.