Anaerobic co-digestion of winery wastewater.
The operational performance of anaerobic batch reactors treating winery wastewater (WW) combined with waste activated sludge (WAS) in different proportions was investigated under mesophilic conditions. In these experiments it was shown that for anaerobic digestion of WW alone, methane production rate was lower than the rates achieved when WW and WAS were treated together. When WW was mixed with WAS at a concentration of 50% WW resulted in the highest methane production rates. A simplified anaerobic model was used to determine the main kinetic parameters; maximum COD reduction rate (q(DA)) and maximum methane generation rate (k(max)). The maximum values of q(DA) and k(max) were 16.50 kgCOD COD(-1) d(-1) and 14.34 kgCOD kgCOD(-1) d(-1), respectively.
Rodríguez
L
L
University of Castilla-La Mancha, Chemical Engineering Department (ITQUIMA), Avenida Camilo José Cela S/N. 13071 Ciudad Real, Spain. Lourdes.Rodriguez@uclm.es
Villaseñor
J
J
Fernández
F J
FJ
Buendía
I M
IM
D000693:Anaerobiosis; D001673:Biodegradation, Environmental; D019149:Bioreactors; D007220:Industrial Waste / Q000517:prevention & control; D007700:Kinetics; D008697:Methane / Q000378:metabolism; D010100:Oxygen / Q000378:metabolism; D012722:Sewage / Q000382:microbiology*; D014865:Waste Disposal, Fluid / Q000295:instrumentation / Q000379:methods*; D014920:Wine
D007220:Industrial Waste; D012722:Sewage; D008697:Methane; D010100:Oxygen