Effect of feeding strategy and COD/sulfate ratio on the removal of sulfate in an AnSBBR with recirculation of the liquid phase.
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 3.7 L, treated 2.0 L synthetic wastewater in 8-h cycles at 30+/-1 degrees 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 10 min with 2L 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 0.8L (containing only the carbon source) in 240 min. The COD/sulfate ratios assessed were 1 and 3. Based on these values and on the concentrations of organic matter (0.5-11.25 gCOD/L) and sulfate (0.5 and 2.5 gSO(4)(2-)/L), the sulfate and organic matter loading rates applied equaled 1.5 and 4.5 gSO(4)(2-)/Ld for sulfate and 1.5, 4.5 and 13.5 gCOD/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 4.5 gSO(4)(2-)/Ld for sulfate, and 1.5 and 4.5 gCOD/Ld for organic matter). When COD/sulfate ratio was 3 (loading rates of 1.5 and 4.5 gSO(4)(2-)/Ld for sulfate, and 4.5 and 13.5 gCOD/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.
Archilha
Natália C
NC
Escola de Engenharia Mauá - Instituto Mauá de Tecnologia, Praça Mauá 1, CEP 09.580-900, São Caetano do Sul - SP, Brazil.
Canto
Catarina S A
CS
Ratusznei
Suzana M
SM
Rodrigues
José A D
JA
Zaiat
Marcelo
M
Foresti
Eugenio
E
D000693:Anaerobiosis; D001673:Biodegradation, Environmental; D018533:Biomass; D019149:Bioreactors / Q000382:microbiology*; D002244:Carbon; D007220:Industrial Waste; D011140:Polyurethanes; D012722:Sewage; D013431:Sulfates / Q000302:isolation & purification / Q000378:metabolism*; D014865:Waste Disposal, Fluid / Q000295:instrumentation / Q000379:methods*
D007220:Industrial Waste; D011140:Polyurethanes; D012722:Sewage; D013431:Sulfates; D002244:Carbon; C028279:polyurethane foam