Simultaneous sulfide and acetate oxidation under denitrifying conditions using an inverse fluidized bed reactor

BACKGROUND: Simultaneous removal of sulfur, nitrogen and carbon compounds from wastewaters is a commercially important biological process. The objective was to evaluate the influence of the CH₃COO⁻/NO₃⁻ molar ratio on the sulfide oxidation process using an inverse fluidized bed reactor (IFBR).RESULT...

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Veröffentlicht in:Journal of chemical technology and biotechnology (1986) 2008-09, Vol.83 (9), p.1197-1203
Hauptverfasser: Beristain-Cardoso, Ricardo, Texier, Anne-Claire, Sierra-Álvarez, Reyes, Field, Jim A, Razo-Flores, Elías, Gómez, Jorge
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Sprache:eng
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Zusammenfassung:BACKGROUND: Simultaneous removal of sulfur, nitrogen and carbon compounds from wastewaters is a commercially important biological process. The objective was to evaluate the influence of the CH₃COO⁻/NO₃⁻ molar ratio on the sulfide oxidation process using an inverse fluidized bed reactor (IFBR).RESULTS: Three molar ratios of CH₃COO⁻/NO₃⁻ (0.85, 0.72 and 0.62) with a constant S²⁻/NO₃⁻ molar ratio of 0.13 were evaluated. At a CH₃COO⁻/NO₃⁻ molar ratio of 0.85, the nitrate, acetate and sulfide removal efficiencies were approximately 100%. The N₂ yield (g N₂ g⁻¹ NO₃⁻-N consumed) was 0.81. Acetate was mineralized, resulting in a yield of 0.65 g inorganic-C g⁻¹ CH₃COO⁻-C consumed. Sulfide was partially oxidized to S⁰, and 71% of the S²⁻ consumed was recovered as elemental sulfur by a settler installed in the IFBR. At a CH₃COO⁻/NO₃⁻ molar ratio of 0.72, the efficiencies of nitrate, acetate and sulfide consumption were of 100%, with N₂ and inorganic-C yields of 0.84 and 0.69, respectively. The sulfide was recovered as sulfate instead of S⁰, with a yield of 0.92 g SO₄²⁻-S g⁻¹ S²⁻ consumed.CONCLUSIONS: The CH₃COO⁻/NO₃⁻ molar ratio was shown to be an important parameter that can be used to control the fate of sulfide oxidation to either S⁰ or sulfate. In this study, the potential of denitrification for the simultaneous removal of organic matter, sulfide and nitrate from wastewaters was demonstrated, obtaining CO₂, S⁰ and N₂ as the major end products. Copyright
ISSN:0268-2575
1097-4660
DOI:10.1002/jctb.1921