Huan Jing Ke Xue
September 2010
The cultivation of aerobic granules in a large pilot-scale SBR was investigated using domestic wastewater. After operation of 210 days, the granules with a diameter of 330 microm were successfully formed by seeding anaerobic digested sludge. Results showed that, during the first three months of operation under low organic load of influent, removal efficiencies of pollutants increased steadily including COD, NH(4+)-N, total nitrogen (TN) and total phosphorous (TP).
View Article and Find Full Text PDFIn this study, aerobic granular sludge was successfully developed in a pilot-scale sequencing batch reactor (SBR) installed on site to treat real wastewater using traditional activated sludge as inoculum. Compared with 1 or 2 months required by lab-scale reactor for aerobic granulation, it took about 400 days for activated sludge to transform into granule-dominant sludge in the pilot-scale SBR on site. Although the sludge in the reactor after 400-day operation was a mixture of flocs and granules with floc ratio ranged from 5 to 30%, sludge volume index with 5min settling (SVI5) always maintained at around 30mL/g.
View Article and Find Full Text PDFHuan Jing Ke Xue
March 2010
The formation process and morphological and physicochemical properties of aerobic granules were examined in a SBR system by a method of alternative feed loading. The results showed that the aerobic granules could be quickly and effectively cultivated using the alternative feeding COD 400, 800, 1200 mg/L [feed loading 0.96, 1.
View Article and Find Full Text PDFFilamentous overgrowth has been observed after aerobic granulation in shaking sequencing batch reactors (SSBR). The factors affecting the filamentous overgrowth in aerobic granules and its possible control methods were investigated. It was found that both the influent and sludge inoculation largely influenced the filamentous overgrowth in aerobic granules.
View Article and Find Full Text PDFComplete aerobic granulation could be achieved in shaking sequencing batch reactors (SSBR) with saline wastewater respectively inoculated conventional activated sludge and anaerobic granules. Pretty good specific TOC removal rates could be achieved without inoculating the halo-bacteria at the start-up time. When the salinity was less than 10 g/L NaCl with the synthetic glucose-rich wastewater as substitute, the TOC removal efficiency was in the range of 70.
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