Yin Wenjun, Wang Kai, Xu Jingtao, Wu Daoji, Zhao Congcong
School of Municipal and Environmental Engineering, Shandong Jianzhu University Jinan 250101 China
College of Geography and Environment, Collaborative Innovation Center of Human-Nature and Green Development in Universities of Shandong, Shandong Normal University Jinan 250014 P. R. China.
RSC Adv. 2018 Dec 19;8(74):42329-42336. doi: 10.1039/c8ra07839d.
A modified sequencing batch biofilm reactor (SBBR, adding a pre-anoxic phase before the aeration phase) was used to treat landfill leachate. The overall SBBR operation period was divided into a load-increasing period I (69 days) and a steady operation period II (41 days). In period I, the influent total nitrogen (TN) and chemical oxygen demand (COD) concentrations increased from approximately 60 and 400 mg L to 1000 and 6500 mg L, respectively, and these were kept for period II. In period II, the COD and TN removal rates were 83-88% and 95-98%, with effluent COD and TN concentrations of less than 500-600 and 10-20 mg L, respectively. The end of pre-anoxic phase PHA (polyhydroxyalkanoate) content increased from 0.11 Cmol (start of period I) to 0.22 Cmol (end of period II). The contributions from simultaneous nitrification and denitrification (SND) and endogenous denitrification to the TN removal rate were approximately 60% and 40%, respectively. The mechanisms of carbon transformation and nitrogen removal were: (1) the synthesis of PHAs in the pre-anoxic phase; (2) short-range nitrification; (3) simultaneous nitrification and denitrification (SND); and (4) endogenous denitrification. Microbial diversity analysis revealed that and accounted for 89.66% of the total bacteria. Ammonia-oxidizing bacteria (AOB, ) and denitrifying bacteria with the ability to transform organic matter into PHAs ( and ) are the dominant bacterial communities.
采用改良序批式生物膜反应器(SBBR,在曝气阶段前增加一个预缺氧阶段)处理垃圾渗滤液。SBBR的整个运行期分为负荷增加期I(69天)和稳定运行期II(41天)。在阶段I,进水总氮(TN)和化学需氧量(COD)浓度分别从约60和400mg/L增加到1000和6500mg/L,并在阶段II保持该浓度。在阶段II,COD和TN去除率分别为83 - 88%和95 - 98%,出水COD和TN浓度分别小于500 - 600mg/L和10 - 20mg/L。预缺氧阶段结束时聚羟基脂肪酸酯(PHA)含量从0.11Cmol(阶段I开始时)增加到0.22Cmol(阶段II结束时)。同步硝化反硝化(SND)和内源反硝化对TN去除率的贡献分别约为60%和40%。碳转化和氮去除的机制为:(1)预缺氧阶段PHA的合成;(2)短程硝化;(3)同步硝化反硝化(SND);(4)内源反硝化。微生物多样性分析表明, 和 占细菌总数的89.66%。氨氧化细菌(AOB, )和具有将有机物转化为PHA能力的反硝化细菌( 和 )是主要细菌群落。