Author_Institution :
Dept. of Environ. Eng., Taiyuan Univ., Taiyuan, China
Abstract :
Notice of Retraction
After careful and considered review of the content of this paper by a duly constituted expert committee, this paper has been found to be in violation of IEEE´s Publication Principles.
We hereby retract the content of this paper. Reasonable effort should be made to remove all past references to this paper.
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To determine if anaerobic microniches are created in granular sludge exposed to oxygen where the refractory organics reduction in coking wastewater could occur and to assay the feasibility of the highly efficiently and stable operation of the micro-aerobic EGSB reactor for simultaneous removal of COD and NH3-N treating actual coking wastewater at 25-30°C, both anaerobic and microaerobic operations of the EGSB reactor were considered. And the granular characteristic of activity, settling, and size was also investigated in this paper. By controlling the oxygenation rate in the aeration column, different concentrations of dissolved O2 were generated in the circulating fluid which supplied dissolved O2 to the granule sludge bed in the EGSB reactor and to generate micro-aerobic environments. The results showed that, at 25-30°C, treating actual coking wastewater with 1280-2024mg·L-1 COD concentration, 50-112mg·L-1 NH3-N concentration, the anaerobic EGSB reactor could only have 40.1%, 56.7% average COD removal efficiencies and 8.3% average NH3-N removal efficiencies (the negative NH3-N removal was usually appeared and even low to -77.8%) with 1.3L.-1, 0.6L-1 influent flow and 9.2h, 20h HRT, respectively. But the microaerobic EGSB reactor could have average COD and NH3-N removal efficiencies of 83.0% and 67.1%, respectively. Supplement dose of Oxygen for the microaerobic EGSB react- r was controlled by redox potential (ORP), and the ORP in the inlet of the micro-aerobic EGSB reactor should be kept at about +35mV. Oxygenation could shift the population distribution to smaller or larger particles compared to the anaerobic EGSB reactor and decreased the settled velocity of the granules (low to 12m.h-1), but without any sludge washout. And the micro-aerobic EGSB reactor could keep about 38.0gMLSS.L-1 sludge concentra- ion and 0.65 MLVSS/MLSS. The methanogenic activity of the granular sludge in the micro-aerobic was not decreased, and even higher than in the strictly anaerobic EGSB reactor.
Keywords :
bioreactors; coke; microorganisms; oxidation; reduction (chemical); refractories; wastewater treatment; EGSB reactor; aeration column; anaerobic operation; coking wastewater treatment; methanogenic activity; microaerobic operation; oxygenation; redox potential; refractory organics; temperature 25 C to 30 C; time 9.2 h; Biodegradation; Bioreactors; Educational institutions; Inductors; Microorganisms; Organic compounds; Protection; Recycling; Sludge treatment; Wastewater treatment;
