dc.creatorCOSTABILE, Augusto L. O.
dc.creatorCANTO, Catarina S. A.
dc.creatorRATUSZNEI, Suzana M.
dc.creatorRODRIGUES, Jose A. D.
dc.creatorZAIAT, Marcelo
dc.creatorFORESTI, Eugenio
dc.date.accessioned2012-10-19T01:10:13Z
dc.date.accessioned2018-07-04T14:48:43Z
dc.date.available2012-10-19T01:10:13Z
dc.date.available2018-07-04T14:48:43Z
dc.date.created2012-10-19T01:10:13Z
dc.date.issued2011
dc.identifierJOURNAL OF ENVIRONMENTAL MANAGEMENT, v.92, n.7, p.1714-1723, 2011
dc.identifier0301-4797
dc.identifierhttp://producao.usp.br/handle/BDPI/17978
dc.identifier10.1016/j.jenvman.2011.02.001
dc.identifierhttp://dx.doi.org/10.1016/j.jenvman.2011.02.001
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1614775
dc.description.abstractThe objective of this work was to analyze the interaction effects between temperature, feed strategy and COD/[SO(4)(2-)] levels, maintaining the same ratio, on sulfate and organic matter removal efficiency from a synthetic wastewater. This work is thus a continuation of Archilha et al. (2010) who studied the effect of feed strategy at 30 degrees C using different COD/[SO] ratios and levels. A 3.7-L anaerobic sequencing batch reactor with recirculation of the liquid phase and which contained immobilized biomass on polyurethane foam (AnSBBR) was used to treat 2.0 L synthetic wastewater in 8 h cycles. The temperatures of 15, 22.5 and 30 degrees C with two feed strategies were assessed: (a) batch and (b) batch followed by fed-batch. In strategy (a) the reactor was fed in 10 min with 2 L wastewater containing sulfate and carbon sources. In strategy (b) 1.2 L wastewater (containing only the sulfate source) was fed during the first 10 min of the cycle and the remaining 0.8 L (containing only the carbon source) in 240 min. Based on COD/[SO(4)(2-)] = 1 and on the organic matter (0.5 and 1.5 gCOD/L) and sulfate (0.5 and 1.5 gSO(4)(2-)/L) concentrations, the sulfate and organic matter loading rates applied were 1.5 and 4.5 g/L.d, i.e., same COD/[SO(4)(2-)] ratio (=1) but different levels (1.5/1.5 and 4.5/4.5 gCOD/gSO(4)(2-)). When reactor feed was 1.5 gCOD/L.d and 1.5 gSO(4)(2-)/L.d, gradual feeding (strategy b) showed to favor sulfate and organic matter removal in the investigated temperature range, indicating improved utilization of the electron donor for sulfate reduction. Sulfate removal efficiencies were 87.9; 86.3 and 84.4%, and organic matter removal efficiencies 95.2; 86.5 and 80.8% at operation temperatures of 30; 22.5 and 15 degrees C, respectively. On the other hand, when feeding was 4.5 gCOD/L.d and 4.5 gSO(4)(2-)/L.d, gradual feeding did not favor sulfate removal, indicating that gradual feeding of the electron donor did not improve sulfate reduction. (C) 2011 Elsevier Ltd. All rights reserved.
dc.languageeng
dc.publisherACADEMIC PRESS LTD- ELSEVIER SCIENCE LTD
dc.relationJournal of Environmental Management
dc.rightsCopyright ACADEMIC PRESS LTD- ELSEVIER SCIENCE LTD
dc.rightsrestrictedAccess
dc.subjectAnSBBR
dc.subjectSulfate removal
dc.subjectBatch and fed-batch
dc.subjectTemperature
dc.titleTemperature and feed strategy effects on sulfate and organic matter removal in an AnSBB
dc.typeArtículos de revistas


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