采用厌氧/缺氧/好氧与生物接触氧化工艺组成的双污泥系统(A2/O-BCO)处理实际生活污水.通过投加乙酸钠调节进水碳氮比(C/N=2.44~8.85),考察了系统的反硝化除磷特性.试验结果表明:进水有机物主要是通过改变硝化性能(即缺氧段反硝化负荷)以及聚-β-羟基链烷酸脂(PHA)的贮存和利用,进而影响系统的脱氮除磷效果.当进水C/N为4~5时,COD、TN和PO43--P去除率分别达到88%,80%和96%,实现了有机物、氮和磷的同步高效去除.碳平衡分析表明,A2/O反应器去除的COD占去除总量的71.86%~77.28%,BCO反应器去除的COD仅占2%~12%,碳源的高效利用是A2/O-BCO工艺在低C/N条件下实现深度脱氮除磷的重要原因.此外,通过进水C/N与曝气量、硝化液回流比、厌/缺氧反应时间等相关性的分析,提出了系统的优化运行策略.%A two-sludge system combined anaerobic/anoxic/oxic with biological contact oxidation process (A2/O-BCO) was used to treat domestic wastewater. By adding sodium acetate to adjust influent carbonitrogen ratio (C/N=2.44 ~ 8.85), the denitrifying phosphorus removal characteristics of the system were investigated. The results showed that nitrification performance (anoxic denitrifying loading) and poly-β-hydroxyalkanoates (PHA) storage and utilization were mainly influenced by organic matter, which further effected the nitrogen and phosphorus removals. When the influent C/N ratio was 4 ~ 5, COD, TN and PO43--P removals reached to 88%, 80% and 96% respectively, which achieved high-efficiency removal of organic matter, nitrogen and phosphorus simultaneously. The material balance analysis of carbon revealed that COD removal in the A2/O reactor was 71.86% ~ 77.28% of the total COD removal, and COD removal in the BCO reactor only accounted for 2% ~ 12%, where the efficient utilization of carbon source in the A2/O- BCO process was the main reason to achieve deep denitrification and phosphorus removal under the condition of low C/N. In addition, through the correlation analysis of C/N with aeration rate, nitrate recycling ratio and anaerobic/anoxic reaction time, the optimal operation strategy of the A2/O-BCO process was proposed.
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