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    Effect of feeding strategy and COD/sulfate ratio on the removal of sulfate in an AnSBBR with recirculation of the liquid phase

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    Artigo de Periódico
    Date
    2010
    Author
    Archilha, Natália Couto
    Canto, Catarina Simone Andrade do
    Ratusznei, Suzana Maria
    Rodrigues, José Alberto Domingues
    Zaiat, Marcelo
    Foresti, Eugênio
    xmlui.dri2xhtml.METS-1.0.item-sponsorship
    FAPESP
    Metadata
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    Abstract
    The objective of this work was to analyze the effect of the interaction between feeding strategy and COD/sulfate ratio on the removal efficiency of sulfate and organic matter from a synthetic wastewater. An anaerobic sequencing batch reactor with recirculation of the liquid phase and containing immobilized biomass on polyurethane foam (AnSBBR) was used. The AnSBBR with a total volume of 3.7L, treated 2.0L synthetic wastewater in 8-h cycles at 30±1°C and was inoculated with anaerobic biomass from a UASB. Two feeding strategies were assessed: (a) batch and (b) batch followed by fed-batch. In strategy (a) the reactor was fed in 10min with 2L wastewater containing sulfate and carbon sources. In strategy (b) 1.2L wastewater (containing only the sulfate source) was fed during the first 10min of the cycle and the remaining 0.8L (containing only the carbon source) in 240min. The COD/sulfate ratios assessed were 1 and 3. Based on these values and on the concentrations of organic matter (0.5-11.25gCOD/L) and sulfate (0.5 and 2.5gSO42-/L), the sulfate and organic matter loading rates applied equaled 1.5 and 4.5gSO42-/Ld for sulfate and 1.5, 4.5 and 13.5gCOD/Ld for organic matter. After stabilization of the system time profiles were run of monitored parameters (COD, sulfate, sulfide and sulfite). In general, the reactor showed to be robust for use in the anaerobic treatment of wastewaters containing sulfate. Gradual feeding (strategy b) of the carbon source favored sulfate reduction, resulting in sulfate removal efficiencies of 84-98% and organic matter removal efficiencies of 48-95%. The best results were observed under COD/sulfate ratio equal to 1 (loading rates of 1.5 and 4.5gSO42-/Ld for sulfate, and 1.5 and 4.5gCOD/Ld for organic matter). When COD/sulfate ratio was 3 (loading rates of 1.5and 4.5gSO42-/Ld for sulfate, and 4.5 and 13.5gCOD/Ld for organic matter) the effect of feed mode became less significant. These results show that the strategy batch followed by fed-batch is more advantageous for COD/sulfate ratios near the stoichiometric value (0.67) and higher organic matter and sulfate concentrations. © 2010 Elsevier Ltd.
    1. AnSBBR
    2. Batch and fed-batch
    3. COD/sulfate ratio
    4. Sulfate removal
    5. Batch reactors
    6. Biogeochemistry
    7. Biological materials
    8. Biological water treatment
    9. Biomass
    10. Chemicals removal (water treatment)
    11. Efficiency
    12. Feeding
    13. Loading
    14. Organic compounds
    15. Reduction
    16. Wastewater treatment
    17. carbon
    18. organic matter
    19. polyurethan foam
    20. sulfate
    21. sulfide
    22. sulfite
    23. Batch and feed-batch
    24. Carbon source
    25. COD/sulphate ratio
    26. Fed batches
    27. Feeding strategies
    28. Loading rate
    29. Recirculations
    30. Sulfate ratio
    31. anoxic conditions
    32. chemical oxygen demand
    33. stoichiometry
    34. wastewater
    35. article
    36. biofilm reactor
    37. biomass
    38. carbon source
    39. chemical interaction
    40. concentration (parameters)
    41. controlled study
    42. liquid
    43. sequencing batch reactor
    44. waste component removal
    45. waste water management
    46. Sulfur compounds
    URI
    https://www.scopus.com/inward/record.uri?eid=2-s2.0-77953292733&doi=10.1016%2fj.jenvman.2010.03.016&partnerID=40&md5=375b636f33e65b713fb12041e1650e12
    https://repositorio.maua.br/handle/MAUA/1213
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