Pretreatment of vinasse from the sugar refinery industry under non-sterile conditions by Trametes versicolor in a fluidized bed bioreactor and its effect when coupled to an UASB reactor
Autor: | Liliana Alzate-Gaviria, Blondy Canto-Canché, Jorge Domínguez-Maldonado, Xavier Font, Elda España-Gamboa, Teresa Vicent |
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Rok vydání: | 2017 |
Předmět: |
0106 biological sciences
Environmental Engineering Continuous operation Trametes versicolor Fluidized bed bioreactor Biomedical Engineering Vinasse 010501 environmental sciences 01 natural sciences Methane chemistry.chemical_compound 010608 biotechnology Ethanol fuel Recalcitrant compounds UASB Molecular Biology Effluent 0105 earth and related environmental sciences biology Waste management Cell Biology biology.organism_classification Anaerobic digestion chemistry Degradation (geology) Non-sterile conditions Hydrous ethanol vinasse |
Zdroj: | Dipòsit Digital de Documents de la UAB Universitat Autònoma de Barcelona |
ISSN: | 1754-1611 |
DOI: | 10.1186/s13036-016-0042-3 |
Popis: | During hydrous ethanol production from the sugar refinery industry in Mexico, vinasse is generated. Phenolic compounds and melanoidins contribute to its color and make degradation of the vinasse a difficult task. Although anaerobic digestion (AD) is feasible for vinasse treatment, the presence of recalcitrant compounds can be toxic or inhibitory for anaerobic microorganism. Therefore, this study presents new data on the coupled of the FBR (Fluidized Bed Bioreactor) to the UASB (Upflow Anaerobic Sludge Blanket) reactor under non-sterile conditions by T. versicolor. Nevertheless, for an industrial application, it is necessary to evaluate the performance in this kind of proposal system. Therefore, this study used a FBR for the removal of phenolic compounds (67%) and COD (38%) at non-sterile conditions. Continuous operation of the FBR was successfully for 26 days according to the literature. When the FBR was coupled to the UASB reactor, we obtained a better quality of effluent, furthermore methane content and yield were 74% and 0.18 m3 CH4/ kg CODremoval respectively. This study demonstrated the possibility of using for an industrial application the coupled of the FBR to the UASB reactor under non-sterile conditions. Continuous operation of the FBR was carried out successfully for 26 days, which is the highest value found in the literature. |
Databáze: | OpenAIRE |
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