Optimization of phosphorus removal in uniFed SBR system for domestic wastewater treatment

被引:4
|
作者
Tang, Xuguang [1 ]
Wang, Shuying [1 ]
Peng, Yongzhen [1 ]
机构
[1] Beijing Univ Technol, Key Lab Beijing Water Qual Sci & Water Environm R, Beijing 100124, Peoples R China
关键词
UniFed sequencing batch reactor (SBR); phosphorus removal; volumetric exchange ratio (VER); alternation of anoxic-aerobic (A/O); domestic wastewater; NUTRIENT REMOVAL; SCALE;
D O I
10.1007/s11783-010-0244-8
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The characteristic of phosphorus removal and appropriate change of the traditional operation modes were investigated in UniFed sequencing batch reactor (SBR) laboratory-scale apparatus (40 L), treating actual domestic wastewater with low ratios of C/N (2.57) and C/P (30.18), providing theoretical basis for actual application of wastewater treatment plant. UniFed SBR system with its unique operation mode had the distinct superiority of phosphorus removal. On this occasion, the effect of volumetric exchange ratio (VER) and the method of influent introduction for phosphorus removal were studied. When the carbon source became the limiting factor to phosphorus release, the higher the VER, the lower the phosphorus concentration in the effluent. Three different influent patterns, including one-time filling, four-time filling, and continuous filling with the same quantity of wastewater could increase the release rate of anaerobic phosphorus from 0.082 to 0.143 mg center dot P center dot(L center dot min)(-1). Appropriate change of the traditional operation modes could optimize the efficiency of phosphorus removal. When the feed/ decant time was extended from 2 h to 4 h, the phosphorous removal efficiency increased from 59.93% to 88.45% without any external carbon source. In the mode of alternation of anoxic-aerobic (A/O) condition, phosphorous removal efficiency increased from 55.07% to 72.27% clearly. The carbon source in the influent can be used adequately, and denitrifying phosphorus removal was carried out in anoxic stage 2 (A2). This mode was optimal for the treatment of actual domestic wastewater with low C/N and C/P ratios.
引用
收藏
页码:475 / 481
页数:7
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