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亚硝化—厌氧氨氧化处理垃圾渗滤液一级厌氧出水的研究
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摘要
本文以人工合成高含氮废水启动了亚硝化和厌氧氨氧化工艺,并在二者达到稳定运行后改用垃圾渗滤液一级厌氧出水作为进水,探讨亚硝化-厌氧氨氧化工艺该废水的可行性。结果表明,串联工艺处理垃圾渗滤液一级厌氧出水时,进水总无机氮负荷达1.0kg/(m3.d),系统氨氮去除率大于93%;并在此基础之上开发了“一步式”全自养生物脱氮工艺,在限氧条件下实现氨氮的“一步脱除”,进水氨氮负荷达0.35kg/(m3.d),氨氮去除率达90%,建立了厌氧氨氧化菌的生长动力学方程,根据亚硝化菌、厌氧氨氧化菌及硝化细菌基质降解速率与生长速率之间的关系,得出上述三种微生物的浓度关系后,分析了三种微生物的共生竞争机制;此外,研究了亚硝化污泥颗粒化过程,并对其形成机理进行了分析。
A short-cut nitrification process (SN) and the anaerobic ammonium oxidation (ANAMMOX) process were started up with the synthetic ammonium-rich wastewater. After they both the two reactors reached stable running, the feasibility of the two processes treating the effluent of an UASB reactor fed by landfill leachate (raw wastewater) was studied. The results show that, when treating raw wastewater, the loading rate of SN-ANAMMOX process reached 1.0 kg/(m3.d), with the ammonium removal efficiency of 93%; "one-step" autotrophic nitrogen removal process was developed under the condition of limited oxygen, the ammonium loading rate reached 0.35kg/(m3.d), with the ammonium removal efficiency of 90%, and an dynamic kinetics equation was established describing the growth of ANAMMOX bacteria, according to the relationship between substrate degrading rate and growth rate, the concentration of SN bacteria, ANAMMOX bacteria and nitrification bacteria was obtained, and the mechanism of the bacteria. Furthermore, the process and mechanism of SN sludge granulation was studied.
引文
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