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作 者:黄健[1] 汤利华[1] 唐玉朝[1] 伍昌年[1] 王健[1]
机构地区:[1]安徽建筑工业学院环境与能源工程学院,安徽合肥230601
出 处:《中国给水排水》2012年第3期94-97,101,共5页China Water & Wastewater
基 金:国家水体污染控制与治理科技重大专项(2008ZX07316-002);安徽省优秀青年科技基金资助项目(10040606Y29);安徽省教育厅自然科学重点科研项目(KJ2011Z052)
摘 要:为解决低碳源城市污水高效脱氮除磷及磷回收问题,开发了侧流A2O工艺,通过抽取不同量的厌氧池末端富磷上清液至化学除磷池,来研究系统的脱氮除磷效果及磷回收情况。结果表明,在无需增加额外碳源,进水COD为136~168 mg/L、NH3-N为32~40 mg/L、TN为36~45mg/L、TP为6~8 mg/L的条件下,当化学除磷比(富磷上清液抽取量与进水量之比)为10%~20%时,对TN和TP的平均去除率分别可达到95.7%、84%,其中,当化学除磷比为15%时,出水TP浓度可降至0.5 mg/L以下,出水水质达到《城镇污水处理厂污染物排放标准(》GB 18918—2002)的一级A标准;同时,回收磷量可达进水磷量的23%~29%,既实现了磷的可持续发展,又增加了污水厂的经济效益。Side-stream A20 process was developed to improve the ability of nitrogen and phosphorus removal from low carbon municipal wastewater and the phosphorus recovery. The nitrogen and phosphorus removal and phosphorus recovery were studied by pumping different amounts of phosphorus-rich supernatant in the end of anaerobic tank into chemical phosphorus removal tank. Under the conditions of the influent COD of 136 to 168 mg/L, NH3 - N of 32 to 40 mg/L, TN of 36 to 45 mg/L, TP of 6 to 8 mg/L and no additional carbon source, the removal rates of TN and TP were 95.7% and 84% when the chemical phosphorus removal ratio (ratio of phosphorus-rich supernatant amount to intluent amount) was 10% to 20%. The effluent TIP concentration was lower than 0.5 mg/L at the chemical phosphorus removal ratio of 15 %. The effluent quality could reach the first criteria class A specified in Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918 -2002). In addition, the amount of phosphorus recovery was 23% to 29% of the influent phosphorus, thus achieving phosphorus sustainable development and increasing the economic benefit of WWTP.
分 类 号:X703[环境科学与工程—环境工程]
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