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不同COD浓度下低基质厌氧氨氧化的启动特征
摘要点击 1785  全文点击 516  投稿时间:2018-08-06  修订日期:2018-12-03
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中文关键词  厌氧序批式反应器(ASBR)  化学需氧量 (COD)  厌氧氨氧化 (ANAMMOX)  启动  脱氮性能  贡献率
英文关键词  Anaerobic sequencing batch reactor(ASBR)  chemical oxygen demand(COD)  anaerobic ammonia oxidation (ANAMMOX)  start-up  nitrogen removal efficiency  contribution rate
作者单位E-mail
马艳红 兰州交通大学环境与市政工程学院, 兰州 730070 1606944231@qq.com 
赵智超 兰州交通大学环境与市政工程学院, 兰州 730070  
安芳娇 兰州交通大学环境与市政工程学院, 兰州 730070  
黄利 兰州铁道设计院有限公司, 兰州 730000  
师晓娟 兰州交通大学环境与市政工程学院, 兰州 730070  
慕浩 兰州交通大学环境与市政工程学院, 兰州 730070  
陈永志 兰州交通大学环境与市政工程学院, 兰州 730070 476411589@qq.com 
中文摘要
      采用厌氧序批式反应器(ASBR)处理NH4+-N和NO2--N浓度分别为(25.00±0.40)mg·L-1和(33.00±0.60)mg·L-1的模拟废水,在温度为30℃时,投加乙酸钠控制COD浓度分别为5.00、15.00、30.00和50.00mg·L-1,研究对厌氧氨氧化启动的影响.结果表明:①4种COD浓度下分别经过74、94、106和129 d均能成功启动厌氧氨氧化.COD浓度为15.00 mg·L-1和30.00mg·L-1时,反应器脱氮性能较好,稳定运行后,平均出水NH4+-N浓度分别为1.98 mg·L-1和1.89mg·L-1,平均出水NO2--N浓度低于0.62mg·L-1,平均出水TN浓度分别为2.37、2.28mg·L-1;②启动过程中反硝化对脱氮的平均贡献率逐渐降低至4.78%、9.59%、10.21%和36.50%,厌氧氨氧化对脱氮的平均贡献率逐渐上升至95.22%、90.41%、89.79%和63.50%;③厌氧氨氧化活性分别在第44、76、86和114 d时超过反硝化活性,最后分别达到0.700、0.690、0.670和0.510 mg·(g·h)-1,反硝化活性分别为0.110、0.130、0.240和0.410 mg·(g·h)-1.该研究结果可为厌氧氨氧化技术在实际工程中的应用提供参考.
英文摘要
      An anaerobic sequencing batch reactor(ASBR)was used to treat low-substrate simulated wastewater with NH4+-N and NO2--N concentrations of (25.00±0.40) mg·L-1 and (33.00±0.60) mg·L-1, respectively. The COD concentrations were controlled at 5.00, 15.00, 30.00, and 50.00 mg·L-1 by adding sodium acetate, and its effects on start-up of anaerobic ammonia oxidation (ANAMMOX) were investigated under the temperature of 30℃. The results showed that ① The start-up of ANAMMOX could be achieved successfully after 74, 94, 106, and 129 days. The nitrogen removal efficiency was optimum when the COD concentration was between 15.00 and 30.00 mg·L-1. In the steady phase, the average effluent concentrations of NH4+-N were 1.98 and 1.89 mg·L-1, the average effluent concentrations of NO2--N were below 0.62 mg·L-1, and the average effluent concentrations of TN were 2.37 and 2.28 mg·L-1. ② The average contribution of heterotrophic denitrification to nitrogen removal decreased to 4.78%, 9.59%, 10.21%, and 36.50%, respectively, during start-up process. The average contribution of ANAMMOX to nitrogen removal gradually increased to 95.22%, 90.41%, 89.79%, and 63.50%, respectively. ③ The activities of ANAMMOX exceeded denitrification activities at 44, 76, 86, and 114 days, respectively, which finally reached 0.700, 0.690, 0.670, and 0.510 mg·(g·h)-1, and the denitrification activities were 0.110, 0.130, 0.240 and 0.410 mg·(g·h)-1, respectively. Thus, the research results have provided references for the application of ANAMMOX to engineering.

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