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Updated: Jun 17, 2026

Continuously-stirred Anaerobic Digester to Convert Organic Wastes into Biogas: System Setup and Basic Operation
Published on: July 13, 2012
Long term operation of a thermophilic anaerobic reactor: process stability and efficiency at decreasing sludge
Ivet Ferrer1, Felícitas Vázquez, Xavier Font
1Environmental Engineering Division, Department of Hydraulic, Maritime, and Environmental Engineering, Technical University of Catalonia (UPC), c/Jordi Girona 1-3, E-08034 Barcelona, Spain. ivet.ferrer@upc.edu
Abstract:
The aim of this study was to evaluate the performance of thermophilic sludge digestion at decreasing sludge retention time (SRT) and increasing organic loading rate (OLR), in terms of methane production, effluent stabilisation, hygienisation and dewaterability. Focus was put on determining indicators to help prevent process failure. To this end, a lab-scale reactor was operated for nearly 2 years at 55 degrees Celsius. Methane production rate was increased (from 0.2 to 0.4-0.6 m(3)((ch)(4)) m(-3)(reactor) d(-1)) by decreasing the SRT from 30 to 15-10 days, while increasing the OLR from 0.5 to 2.5-3.5 kg VS m(-3)(reactor) d(-1). Sludge dewaterability was worsened at SRT below 15 days; while pathogen destruction was always successful. The following concentrations might be used to prevent process failure: VFA C2-C5 (3.7 g CODL(-1)), acetate (0.6 g L(-1)), acetate/propionate (0.5), intermediate alkalinity (1.8 g CaCO(3) L(-1)), intermediate/partial alkalinity (0.9), intermediate/total alkalinity (0.5), CH(4) in biogas (55%).
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