dc.creatorCANTO, C. S. A.
dc.creatorRATUSZNEI, S. M.
dc.creatorRODRIGUES, J. A. D.
dc.creatorZAIAT, M.
dc.creatorFORESTI, E.
dc.date.accessioned2012-03-26T01:53:45Z
dc.date.accessioned2018-07-04T13:53:54Z
dc.date.available2012-03-26T01:53:45Z
dc.date.available2018-07-04T13:53:54Z
dc.date.created2012-03-26T01:53:45Z
dc.date.issued2008
dc.identifierBrazilian Journal of Chemical Engineering, v.25, n.2, p.275-289, 2008
dc.identifier0104-6632
dc.identifierhttp://producao.usp.br/handle/BDPI/4372
dc.identifier10.1590/S0104-66322008000200007
dc.identifierhttp://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322008000200007
dc.identifierhttp://www.scielo.br/pdf/bjce/v25n2/a07v25n2.pdf
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1603173
dc.description.abstractThe removal of biological nitrogen from a synthetic wastewater with different ammonium nitrogen concentrations (50 and 100 mgN-NH4+/L) by a nitrification and denitrification process using a sequencing batch biofilm reactor (SBBR) with liquid-phase circulation was studied. The system with a total working volume of 4.6 L (3.7 L in the reactor and 0.9 L in the reservoir) treated 2.1 L of synthetic wastewater in 12-h cycles. As inoculum two types of biomass were used: an anaerobic/anoxic one from an up-flow anaerobic sludge blanket reactor (UASB) and an aerobic one from a prolonged aeration activated sludge system. The system, maintained at 30 ± 1 ºC, operated in batch mode followed by fed-batch mode and was aerated intermittently. During fed-batch operation the reactor was fed with an external carbon source as electron donor in the denitrifying step and with no aeration. When the reactor was fed with 50 mgN-NH4+/L, efficiencies of removal of ammonium nitrogen and total nitrogen from the effluent were 93.8 and 72.2%, respectively, and nitrite, nitrate and organic nitrogen concentrations were 0.07, 6.4 and 0.5 mg/L, respectively. On the other hand, when the influent ammonium nitrogen concentration was 100 mgN-NH4+/L, residual nitrite and nitrate were 0.17 and 20.4, respectively, and no N-Org was found in the effluent. It should be mentioned that residual nitrate remained unaltered at the different C/N ratios used. Consequently, efficiency of total nitrogen removal was reduced to 66.7%, despite efficiency of ammonium nitrogen removal exceeding 90%. These results show the potential of the proposed system in removing ammonium nitrogen from liquid effluents with a moderate ammonium nitrogen concentration.
dc.languageeng
dc.publisherBrazilian Society of Chemical Engineering
dc.relationBrazilian Journal of Chemical Engineering
dc.rightsCopyright Brazilian Society of Chemical Engineering
dc.rightsopenAccess
dc.subjectNitrification and denitrification
dc.subjectImmobilized biomass
dc.subjectSequencing batch biofilm reactor
dc.subjectLiquid-phase circulation
dc.titleEffect of ammonia load on efficiency of nitrogen removal in an SBBR with liquid-phase circulation
dc.typeArtículos de revistas


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