内循环SBR反应器无厌氧段实现同步脱氮除磷

研究了内循环SBR反应器在模拟城市生活污水处理中脱氮除磷的效果.结果表明,在曝气时间为4h,曝气开始时DO浓度为6mg·L-1,pH值7～8时,反应器对COD、NH4 -N、TP均有较好的去除效果,进水中COD浓度、NH4 -N浓度、TP浓度分别由170～260mg·L-1、20～30mg·L-1、8～20mg·L-1降到出水的4～48mg·L-1、0～2.0mg·L-1和0～1.4mg·L-1,COD、TIN(NH4 -N NO3--N N02--N)的去除率分别为89.7%±6.5%、70%左右,NH4 -N的转化率为97.4%±3.6%、TP的去除率为95.6%±4.4%.在本研究的实验过程中反应器进水后未经过传统除磷理论认为所必须的厌氧段而直接曝气,TP的去除效果仍然良好且运行稳定,这和传统的理论与研究有所区别.

Simultaneous Nitrogen and Phosphorus Removal in the Reactor of Inner Loop SBR Without Anaerobic Phase

The performance of simultaneous nitrogen and phosphorus removal with an inner loop sequencing batch reactor were investigated by simulated municipal wastewater. The experimental results showed that COD, NH4(+) -N, and TP can be removed efficiently after four hours aeration, during which dissolved oxygen concentration was at 6 mg/L at the beginning of aerobic phase and pH was in the rang of 7 - 8. The COD and NH4+ -N as well as TP concentration in the effluent were about at 4 - 48 mg x L(1), 0 - 2.0 mg x L(-1), and 0 - 1.4 mg x L(-1) respectively, which indicated the removal rate for each item were about 89.7% +/- 6.5%, 97.4% +/- 3.6%, 95.6% +/- 4.4% when the concentration of influent were about 170 - 260 mg x L(-1), 20 - 30 mg- L(-1), 8 - 20 mg L(-1), respectively. The removal rate of TIN( NH4 -N + NO3(-) -N + NO2(-) -N) was also reached about 70%. It was found during the research process that phosphorus removal can be achieved without anaerobic phase, which was conventionally considered as a key phase for phosphorus removal, and this phenomena can not be explained by traditional theory.