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机构地区:[1]石家庄铁路职业技术学院,石家庄050041 [2]北京工业大学环境与能源工程学院,北京100022
出 处:《环境工程学报》2014年第3期845-850,共6页Chinese Journal of Environmental Engineering
基 金:河北省高等学校科学技术研究青年基金项目(QN2013172);河北省科技厅科技支撑计划项目(12273611);国家自然科学基金资助项目(51008005)
摘 要:利用SBR,控制曝气量为60 L/h,利用在线pH曲线控制曝气时间,成功实现了短程生物脱氮过程,并考察了不同进水方式下SBR运行性能及N2O产量。结果表明,分段进水能够有效降低短程生物脱氮过程中外加碳源投加量。在原水进水碳氮比较低时,采用递增进水量的进水方式,能够有效降低生物脱氮过程中NO-2积累量,从而降低系统N2O产量。1次进水、2次等量进水和2次递增进水方式下,生物脱氮过程中N2O产量分别为11.1、8.86和5.04 mg/L。硝化过程中NO-2-N的积累是导致系统N2O产生的主要原因。部分氨氧化菌(AOB)在限氧条件下以NH+4-N作为电子供体,NO-2-N作为电子受体进行反硝化,最终产物是N2O。Using a lab-scale batch sequencing reactor( SBR),advanced nitrogen removal from municipal wastewater and stabilizing short-cut nitrification and denitrification,as well as N2O emission,were investigated by on-line pH controlling. The aeration rate was controlled at 60 L/h. It revealed that by step-feeing pattern,less N2O was emitted and less external carbon for denitrification was required. The increasing feeding mode was efficient for reducing the NO-2 accumulation and N2O emission when organic carbon in the influent was insufficient. The N2O-N emission were 11. 1,8. 86 and 5. 04 mg/L for one-time feeding,two equal feeding and two increasing feeding mode respectively. The accumulation of NO-2-N during nitrogen removal process contributed to the production of N2O. The denitrification process of AOB under low DO level might be the cause of N2O production in which NO-2 was used as electron acceptor and NH+4 as electron donor.
关 键 词:生活污水 短程生物脱氮 分段进水 N2O 好氧反硝化
分 类 号:X703[环境科学与工程—环境工程]
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