dc.creator | CANTO, C. S. A. | |
dc.creator | RATUSZNEI, S. M. | |
dc.creator | RODRIGUES, J. A. D. | |
dc.creator | ZAIAT, M. | |
dc.creator | FORESTI, E. | |
dc.date.accessioned | 2012-03-26T01:53:45Z | |
dc.date.accessioned | 2018-07-04T13:53:54Z | |
dc.date.available | 2012-03-26T01:53:45Z | |
dc.date.available | 2018-07-04T13:53:54Z | |
dc.date.created | 2012-03-26T01:53:45Z | |
dc.date.issued | 2008 | |
dc.identifier | Brazilian Journal of Chemical Engineering, v.25, n.2, p.275-289, 2008 | |
dc.identifier | 0104-6632 | |
dc.identifier | http://producao.usp.br/handle/BDPI/4372 | |
dc.identifier | 10.1590/S0104-66322008000200007 | |
dc.identifier | http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322008000200007 | |
dc.identifier | http://www.scielo.br/pdf/bjce/v25n2/a07v25n2.pdf | |
dc.identifier.uri | http://repositorioslatinoamericanos.uchile.cl/handle/2250/1603173 | |
dc.description.abstract | The 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.language | eng | |
dc.publisher | Brazilian Society of Chemical Engineering | |
dc.relation | Brazilian Journal of Chemical Engineering | |
dc.rights | Copyright Brazilian Society of Chemical Engineering | |
dc.rights | openAccess | |
dc.subject | Nitrification and denitrification | |
dc.subject | Immobilized biomass | |
dc.subject | Sequencing batch biofilm reactor | |
dc.subject | Liquid-phase circulation | |
dc.title | Effect of ammonia load on efficiency of nitrogen removal in an SBBR with liquid-phase circulation | |
dc.type | Artículos de revistas | |