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作 者:彭党聪[1] 金奇庭[1] 郭风伟 温晓玫[1] 诸竹君[1]
机构地区:[1]西安冶金建筑学院环境工程系
出 处:《西安冶金建筑学院学报》1994年第1期36-41,共6页
摘 要:以硝化菌增长的Haldane模式为基础,通过理论分析证明,完全混合式活性污泥反应器是碳氧化(COD降解)和NH3—N硝化合并处理工艺的最佳反应器,给出了曝气池NH3—N的最佳浓度(7.4mg/L).在此基础上,采用单级活性污泥法处理同时含有COD350—400mg几和NH3—N150mg/L的树脂生产废水,结果表明:当控制水力停留时间(HRT)为8h时,NH3—N的硝化率和COD去除率分别为90%和65%,将HRT延长至10h,NH3—N可完全硝化,而COD的去除率并不降低。On the basis of Haldane nitrifier growth model,it is confirmed theoritically that the completely-mixed activated sludge reactor can be the optimum one for simultaneous carbonaceous oxidation (COD degradation ) and ammonium nitrification. The optimum NH3-N concentration (7.4 mg/L) in the aeration tank is also given. A laboratory scale experiment using synthetic resin production wastewater which 350-400 mg/L COD and 180 mg/L NH3-N are contained is conducted. The results show that ammonium nitrification rate and COD removal efficiency can reach 90% and 65% respectively, in a single activated sludge process when hydraulic retention time (HRT) is controlled at 8h. Ammonium can be completely nitrified with HRT 10h. whereas COD removal efficiency can be maintained unchanging.
分 类 号:X783.03[环境科学与工程—环境工程]
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