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dc.contributor.authorFlores-Valle, Sergio Odín
dc.contributor.authorRíos-Bernÿ, Omar
dc.contributor.authorChanona-Pérez, Jorge
dc.contributor.authorFregoso-Aguilar, Tomas
dc.contributor.authorMorales-González, Ángel
dc.contributor.authorPrado Rubianes, Óscar Jesús
dc.contributor.authorHerrera-Bucio, Rafael
dc.contributor.authorLópez-Albarán, Pablo
dc.contributor.authorMorales-González, Ángel
dc.contributor.authorGaribay-Febles, Vicente
dc.contributor.authorGodínez Domínguez, Enrique
dc.contributor.authorKennes, Christian
dc.contributor.authorVeiga, María Carmen
dc.contributor.authorMendoza-Pérez, Jorge Alberto
dc.date.accessioned2014-10-30T12:37:59Z
dc.date.available2014-10-30T12:37:59Z
dc.date.issued2011-08
dc.identifier.citationFlores-Valle SO, Ríos-Bernÿ O, Chanona-Pérez J, Fregoso-Aguilar T, Morales-González JA, Prado-Rubianes OJ, et al. A comparative study of physical and chemical processes for removal of biomass in biofilters. Molecules. 2011;16(8):6927-49es_ES
dc.identifier.otherdoi:10.3390/molecules16086927
dc.identifier.urihttp://hdl.handle.net/2183/13751
dc.description.abstractAfter 6 months of operation a long-term biofilter was stopped for two weeks and then it was started up again for a second experimental period of almost 1.3 years, with high toluene loads and submitted to several physical and chemical treatments in order to remove excess biomass that could affect the reactor’s performance due to clogging, whose main effect is a high pressure drop. Elimination capacity and removal efficiency were determined after each treatment. The methods applied were: filling with water and draining, backwashing, and air sparging. Different flows and temperatures (20, 30, 45 and 60 °C) were applied, either with distilled water or with different chemicals in aqueous solutions. Treatments with chemicals caused a decrease of the biofilter performance, requiring periods of 1 to 2 weeks to recover previous values. The results indicate that air sparging with pure distilled water as well as with solutions of NaOH (0.01% w/v) and NaOCl (0.01% w/v) were the treatments that removed more biomass, working either at 20, 30 or 45 °C and at relatively low flow rates (below 320 L h−1), but with a high biodegradation inhibition after the treatments. Dry biomass (g VS) content was determined at three different heights of the biofilter in order to carry out each experiment under the same conditions. The same amount of dry biomass when applying a treatment was established so it could be considered that the biofilm conditions were identical. Wet biomass was used as a control of the biofilter’s water content during treatments. Several batch assays were performed to support and quantify the observed inhibitory effects of the different chemicals and temperatures applied.es_ES
dc.language.isoenges_ES
dc.publisherMDPIes_ES
dc.relation.urihttp://dx.doi.org/10.3390/molecules16086927es_ES
dc.subjectDownward flowes_ES
dc.subjectBiofilteres_ES
dc.subjectBackwashinges_ES
dc.subjectAir sparginges_ES
dc.subjectBiofilmes_ES
dc.subjectClogginges_ES
dc.subjectBatch assayes_ES
dc.subjectFilter bedes_ES
dc.subjectBiomass controles_ES
dc.titleA Comparative Study of Physical and Chemical Processes for Removal of Biomass in Biofilterses_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.accessinfo:eu-repo/semantics/openAccesses_ES


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