Long term operation of a thermophilic anaerobic reactor
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 indicator...
| Authors: | , , |
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| Format: | article |
| Publication Date: | 2009 |
| Country: | España |
| Institution: | Universitat Autònoma de Barcelona |
| Repository: | Dipòsit Digital de Documents de la UAB |
| Language: | English |
| OAI Identifier: | oai:ddd.uab.cat:163067 |
| Online Access: | https://ddd.uab.cat/record/163067 https://dx.doi.org/urn:doi:10.1016/j.biortech.2009.12.006 |
| Access Level: | Open access |
| Keyword: | Biogas Biosolids Dewaterability Hygienisation Wastewater |
| Summary: | 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 °C. Methane production rate was increased (from 0.2 to 0.4-0.6 m³CH₄ m⁻³reactor 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⁻³reactor 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 COD L⁻¹), acetate (0.6 g L⁻¹), acetate/propionate (0.5), intermediate alkalinity (1.8 g CaCO₃ L⁻¹), intermediate/partial alkalinity (0.9), intermediate/total alkalinity (0.5), CH₄ in biogas (55%). |
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