dc.creatorDAMIANOVIC, Marcia Helena Rissato Zamariolli
dc.creatorFORESTI, Eugenio
dc.date.accessioned2012-10-19T01:10:09Z
dc.date.accessioned2018-07-04T14:48:40Z
dc.date.available2012-10-19T01:10:09Z
dc.date.available2018-07-04T14:48:40Z
dc.date.created2012-10-19T01:10:09Z
dc.date.issued2009
dc.identifierPROCESS BIOCHEMISTRY, v.44, n.9, p.1050-1054, 2009
dc.identifier1359-5113
dc.identifierhttp://producao.usp.br/handle/BDPI/17963
dc.identifier10.1016/j.procbio.2009.04.027
dc.identifierhttp://dx.doi.org/10.1016/j.procbio.2009.04.027
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1614760
dc.description.abstractTwo bench-scale horizontal anaerobic fixed bed reactors were tested to remove both sulfate and organic matter from wastewater. First, the reactors (R1 and R2) were supplied with synthetic wastewater containing sulfate and a solution of ethanol and volatile fatty acids. Subsequently, RI and R2 were fed with only ethanol or acetate, respectively. The substitution to ethanol in R1 increased the sulfate reduction efficiency from 83% to nearly 100% for a chemical oxygen demand to sulfate (COD/sulfate) ratio of 3.0. In contrast, in R2, the switch in carbon source to acetate strongly decreased sulfidogenesis and the maximum sulfate reduction achieved was 47%. Process stability in long-term experiments and high removal efficiencies of both organic matter and sulfate were achieved with ethanol as the sole carbon source. The results allow concluding that syntrophism instead of competition between the sulfate reducing bacteria and acetoclastic methanogenic archaeal populations prevailed in the reactor. (C) 2009 Elsevier Ltd. All rights reserved.
dc.languageeng
dc.publisherELSEVIER SCI LTD
dc.relationProcess Biochemistry
dc.rightsCopyright ELSEVIER SCI LTD
dc.rightsrestrictedAccess
dc.subjectAcetogenesis
dc.subjectAnaerobic digestion
dc.subjectCOD/sulfate ratio
dc.subjectEthanol
dc.subjectHAIB reactor
dc.subjectMethanogenesis
dc.subjectSulfate reduction
dc.titleDynamics of sulfidogenesis associated to methanogenesis in horizontal-flow anaerobic immobilized biomass reactor
dc.typeArtículos de revistas


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