R. Borja et al., ANAEROBIC-DIGESTION OF WASH WATERS DERIVED FROM THE PURIFICATION OF VIRGIN OLIVE OIL USING A HYBRID REACTOR COMBINING A FILTER AND A SLUDGEBLANKET, Process biochemistry, 31(3), 1996, pp. 219-224
A laboratory-scale hybrid anaerobic reactor, the bottom third of which
was occupied by a sludge blanket, the upper two-thirds by submerged c
lay rings, was used for treatment of wash waters derived from the puri
fication of olive oil in a new manufacturing process. The reactor was
operated under mesophilic conditions at different influent substrate c
oncentrations. The hydraulic retention times (HRT) ranged from 0.20 to
1.02 days under normal operating conditions after the start-up. Chemi
cal oxygen demand (GOD) removal efficiencies of more than 89% were ach
ieved at an organic loading rate(OLR) of 8.0 kg COD/m(3) day. OLR was
gradually increased from 2.6 to 7.1 kg COD/m(3) day within 16 days but
the anaerobic reactor performances did not change significantly. The
reactor was operated under varying influent COD concentrations to test
the response of the system to both high and low strength wash waters.
The system can tolerate OLRs as high as 17.8 kg COD/m(3) day with an
average COD removal efficiency of 76.2%. Although the reactor was fed
by diluted influent, with an average COD of 1030 mg/litre, at very hig
h hydraulic loadings (HRT=4.8 h) COD removals over 75% were achieved.