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Development of pre-coagulation and bio-filtration process for advanced treatment of sewage

机译:开发用于污水深度处理的预混凝和生物过滤工艺

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摘要

A pre-coagulation and bio-filtration process for advanced treatment of sewage is developed and experimentally discussed with a pilot plant. The bio-filtration unit consists of a denitrification filter, a nitrification filter with side stream to the denitrification filter, and a polishing filter with anoxic and aerobic parts. Concentrations of SS, T-COD_(Cr), T-C-BOD, T-N and T-P in the effluent were stably kept at less than 3 mg/L, 20 mg/L, 5 mg/L, 2 mg N/L and 0.2 mg P/L, respectively, and transparency at higher than 100 cm, under total hydraulic retention time (HRT) of 3.2 h in the bio-filtration parts. S-COD_(Cr)/NO_x~- -N ratio of higher than 12 mg COD/mg N is required to keep the remaining NOx~- -N concentrations less than 1 mg N/L in the effluent from the denitrification filter. Methanol addition rate of higher than 4.5 mg COD/mg N is necessary to accomplish denitrification with the remaining NO_x~- -N of less than 0.5 mg N/L in the effluent from the polishing filter. Backwashing in each filter as well as methanol addition and aeration in the polishing filter were able to be operated successfully by the automatic control systems. Therefore this process is proved to be applicable to advanced treatment of sewage with easy maintenance.
机译:开发了用于污水深度处理的预混凝和生物过滤工艺,并与中试工厂进行了实验讨论。生物过滤单元包括反硝化过滤器,带反硝化过滤器侧流的硝化过滤器以及带有缺氧和好氧部分的抛光过滤器。废水中SS,T-COD_(Cr),TC-BOD,TN和TP的浓度稳定保持在3 mg / L,20 mg / L,5 mg / L,2 mg N / L和0.2 mg生物过滤部件的总水力停留时间(HRT)为3.2 h时,P / L和透明性均高于100 cm。需要S-COD_(Cr)/ NO_x-N比率高于12 mg COD / mg N,以使反硝化过滤器流出物中的剩余NOx-N浓度小于1 mg N / L。甲醇脱除率必须高于4.5 mg COD / mg N,才能完成反硝化作用,而抛光过滤器流出物中的残留NO_x --- N小于0.5 mg N / L。每个过滤器中的反洗以及抛光过滤器中的甲醇添加和通气都可以通过自动控制系统成功运行。因此,该方法被证明适用于污水的深度处理且易于维护。

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