The working operations of a full-scale digester of a wastewater treatment plant for waste-mixed sludge (WMS) stabilization was reproduced using a pilot-scale apparatus. The effect of WMS co-digested with fruit and vegetable waste (FVW) was investigated at different organic loading rates (OLR), from 1.46 kg VS/m3day to 2.8 kg VS/m3day, and reduced hydraulic retention time, from 14days to about 10days. Methane production per unit of digester volume increased from about 140 NL/m3day to a maximum value of about 900 NL/m3day when OLR was increased from 1.46kgVS/m3day to 2.1 kg VS/m3day. Higher OLR caused an excessive HRT reduction, decreasing the percentage of volatile solids degradation without significantly affecting process stability. The maximum electrical energy producible from the full-scale anaerobic facility was about 3,500,000 kWh/year. In these conditions the electrical power output and the net efficiency of the co-generator were 470 kW and 37%, respectively.
Amount of energy recoverable from an existing sludge digester with the co-digestion with fruit and vegetable waste at reduced retention time
DI MARIA, Francesco
Conceptualization
;SORDI, ALESSIOFormal Analysis
;CIRULLI, GIUSEPPESoftware
;MICALE, CATERINAMethodology
2015
Abstract
The working operations of a full-scale digester of a wastewater treatment plant for waste-mixed sludge (WMS) stabilization was reproduced using a pilot-scale apparatus. The effect of WMS co-digested with fruit and vegetable waste (FVW) was investigated at different organic loading rates (OLR), from 1.46 kg VS/m3day to 2.8 kg VS/m3day, and reduced hydraulic retention time, from 14days to about 10days. Methane production per unit of digester volume increased from about 140 NL/m3day to a maximum value of about 900 NL/m3day when OLR was increased from 1.46kgVS/m3day to 2.1 kg VS/m3day. Higher OLR caused an excessive HRT reduction, decreasing the percentage of volatile solids degradation without significantly affecting process stability. The maximum electrical energy producible from the full-scale anaerobic facility was about 3,500,000 kWh/year. In these conditions the electrical power output and the net efficiency of the co-generator were 470 kW and 37%, respectively.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.