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, ALESSIO
Formal Analysis
;
CIRULLI, GIUSEPPE
Software
;
MICALE, CATERINA
Methodology
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.
2015
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11391/1342987
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