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Treatment of phenolic wastes in an aerated submerged fixed-film (ASFF) bioreactor
Affiliation:1. Bordeaux INP - EA 4592 – ENSEGID, Institut Carnot/ISIFOR, 1 Allée F. Daguin, 33607 Pessac, France;2. Aix Marseille Univ, CNRS UMR 7376, Laboratoire Chimie Environnement, 3 Place Victor Hugo, F-13331 Marseille, France;1. Department of Computer Science & Technology, Tsinghua University, Beijing, China;2. Graduate School at Shenzhen, Tsinghua University, Shenzhen, Guangdong, China;3. Department of Computer Science at the University of Minnesota Duluth, MN, USA;1. University of Natural Resources and Life Sciences Vienna (BOKU), Department IFA-Tulln, Institute for Environmental Biotechnology, Konrad Lorenz Strasse 20, 3430 Tulln, Austria;2. University of Plymouth, Petroleum and Environmental Geochemistry Group, Biogeochemistry Research Centre, Drake Circus, Plymouth, Devon PL4 8AA, UK;3. Government of Upper Austria, Directorate for Environment and Water Management, Division for Environmental Protection, Kärntner Strasse 10-12, 4021 Linz, Austria;4. GUT Gruppe Umwelt und Technik GmbH, Ingenieurbüro für Technischen Umweltschutz, Plesching 15, 4040 Linz, Austria
Abstract:The biological removal of phenol was studied in a multi-stage fixed-film reactor at phenol concentrations in the range of 190–900 mg l−1, hydraulic loadings of 0.02–0.22 m3 m−2 day−1 and temperatures of 20–35°C. Phenol removals up to 99.9% were obtained at 20°C but the efficiency decreased as the loading rate or phenol concentration was increased. The reactor coped with organic overloads better than with hydraulic overloads. Removal efficiencies increased as temperature was increased. Reactor performance was stable under extreme loadings and the reactor was capable of handling a ten-fold increase in loading with less than 20% loss in phenol removal efficiency. A large amount of attached biomass was retained in the reactor and was mostly present in the first stage where the majority of organic removal occurred.
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