TY - JOUR
T1 - Comparison of phosphorus removal efficiency between reversed and conventional A2/O processes
AU - Jin, Pengkang
AU - Zheng, Weiyuan
AU - Wang, Xianbao
AU - Zhang, Yu
AU - Wang, Xiaochang
AU - Sun, Hongfang
N1 - Publisher Copyright:
©, 2015, Science Press. All right reserved.
PY - 2015/2/5
Y1 - 2015/2/5
N2 - Through the monitoring and analysis on the whole reversed A2/O process in a sewage treatment plant in Xi'an, the adverse factors for poor phosphorus removal were ascertained. The study shows that the denitrification is incomplete in the anoxic tank so that lots of nitrate flows into the anaerobic tank and inhibits phosphorus release, which leads to the poor phosphorus removal. The phosphorus release was inhibited gradually with the increase of nitrate when the nitrate concentration was between 1 mg/L and 4 mg/L. When nitrate concentration was above 4 mg/L, phosphorus release was inhibited significantly. In order to avoid the adverse effect of nitrate on phosphorus accumulating bacteria for phosphorus release, nitrate concentration in the anaerobic tank should be below 1 mg/L. The adverse effect of nitrate on phosphorus accumulating bacteria indicates that carbon source is required for phosphorus release. Therefore, the effect of nitrate on phosphorus release was studied by using sodium acetate and raw water as carbon source sampled from the wastewater treatment plant. The study shows that the easily biodegradable organic matter was more beneficial for phosphorus release in anaerobic tank. Because of the anoxic tank set as the first step in reversed A2/O process, a large amount of easily biodegradable organic matter is consumed first for denitrification in the anoxic tank, which lead to the poor effect of phosphorus release in anaerobic tank due to lack of easily biodegradable organic matter. In response to this study, a reconstruction scheme that the reversed A2/O process shall be adjusted to a conventional A2/O process was put forward. After the reconstruction project, the concentration of nitrate in anaerobic tank decreases from a previous one of 3.57 mg/L to the current one of 0.89 mg/L with the amount of phosphorus release increased by 1.8 times. The total phosphorus in the effluent is 0.66 mg/L which is 0.21 mg/L lower than that of the reversed A2/O process.
AB - Through the monitoring and analysis on the whole reversed A2/O process in a sewage treatment plant in Xi'an, the adverse factors for poor phosphorus removal were ascertained. The study shows that the denitrification is incomplete in the anoxic tank so that lots of nitrate flows into the anaerobic tank and inhibits phosphorus release, which leads to the poor phosphorus removal. The phosphorus release was inhibited gradually with the increase of nitrate when the nitrate concentration was between 1 mg/L and 4 mg/L. When nitrate concentration was above 4 mg/L, phosphorus release was inhibited significantly. In order to avoid the adverse effect of nitrate on phosphorus accumulating bacteria for phosphorus release, nitrate concentration in the anaerobic tank should be below 1 mg/L. The adverse effect of nitrate on phosphorus accumulating bacteria indicates that carbon source is required for phosphorus release. Therefore, the effect of nitrate on phosphorus release was studied by using sodium acetate and raw water as carbon source sampled from the wastewater treatment plant. The study shows that the easily biodegradable organic matter was more beneficial for phosphorus release in anaerobic tank. Because of the anoxic tank set as the first step in reversed A2/O process, a large amount of easily biodegradable organic matter is consumed first for denitrification in the anoxic tank, which lead to the poor effect of phosphorus release in anaerobic tank due to lack of easily biodegradable organic matter. In response to this study, a reconstruction scheme that the reversed A2/O process shall be adjusted to a conventional A2/O process was put forward. After the reconstruction project, the concentration of nitrate in anaerobic tank decreases from a previous one of 3.57 mg/L to the current one of 0.89 mg/L with the amount of phosphorus release increased by 1.8 times. The total phosphorus in the effluent is 0.66 mg/L which is 0.21 mg/L lower than that of the reversed A2/O process.
KW - Carbon competition
KW - Conventional A/O process
KW - Nitrate
KW - Phosphorus release amount
KW - Reversed A/O process
UR - https://www.scopus.com/pages/publications/84923781054
M3 - 文章
AN - SCOPUS:84923781054
SN - 1673-9108
VL - 9
SP - 501
EP - 505
JO - Chinese Journal of Environmental Engineering
JF - Chinese Journal of Environmental Engineering
IS - 2
ER -