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耐盐反硝化污泥与复合菌剂对高硫酸盐含氮废水的处理性能
引用本文:吴贵阳, 张泽梁, 田志娟, 李步, 俞柯吟, 叶斌杰, 汪金立, 阮文彬, 冯丽娟. 耐盐反硝化污泥与复合菌剂对高硫酸盐含氮废水的处理性能[J]. 环境工程学报, 2023, 17(2): 644-654. doi: 10.12030/j.cjee.202210148
作者姓名:吴贵阳  张泽梁  田志娟  李步  俞柯吟  叶斌杰  汪金立  阮文彬  冯丽娟
作者单位:1.浙江海洋大学海洋科学与技术学院,舟山 316022; 2.中国石油化工股份有限公司洛阳分公司,洛阳 471100; 3.浙江海洋大学,浙江省石油化工环境污染控制重点实验室,舟山 316022
基金项目:中石化洛阳分公司委托课题《耐盐复合菌剂制备及其在高盐高氮废水处理应用研究》(H21028007022)
摘    要:以耐盐反硝化污泥(DAS)和反硝化复合菌剂(DBA)为菌源,启动序批式生物膜系统(SBBRs)处理高硫酸盐含氮废水。结果表明,以相对低盐度(1%:12.5 g·L−1 SO42−和5 g·L−1 NaCl)启动系统,在不同菌源和载体条件下SBBRs启动时间均较短(6~11 d),其中以DAS为菌源、载体污泥浸制预处理均能缩短启动周期。提升SO42-质量浓度至25 g·L−1 (盐度2%)和37.5 g·L−1 (盐度3%)后,各装置的硝氮去除率均可维持90%以上,其中3%盐度下悬浮填料系统反硝化完全(>98%),显著高于生物绳系统(91.1±11.7)%。理论TOC/TN比为1.4~7,系统总氮去除率均稳定保持90%以上。优选TOC/TN值为2的实验室内处理石化厂高硫酸盐(2.7%)高氮(TN≈200 mg·L−1)废水,系统适应驯化后可获得稳定高效的总氮去除率,且悬浮填料去除率(>99%)与稳定性均优于生物绳(>90%)。系统硝酸盐还原途径以反硝化为主,且无显著硝酸盐异化还原为氨和硫酸盐还原作用。

关 键 词:耐盐复合菌   生物强化   硫酸盐   菌源   载体   C/N比
收稿时间:2022-10-29

Treatment performance of high-sulfate nitrogenous wastewater by salt-tolerant denitrifying activated sludge and compound bacteria agents
WU Guiyang, ZHANG Zeliang, TIAN Zhijuan, LI Bu, YU Keyin, YE Binjie, WANG Jinli, RUAN Wenbin, FENG Lijuan. Treatment performance of high-sulfate nitrogenous wastewater by salt-tolerant denitrifying activated sludge and compound bacteria agents[J]. Chinese Journal of Environmental Engineering, 2023, 17(2): 644-654. doi: 10.12030/j.cjee.202210148
Authors:WU Guiyang  ZHANG Zeliang  TIAN Zhijuan  LI Bu  YU Keyin  YE Binjie  WANG Jinli  RUAN Wenbin  FENG Lijuan
Affiliation:1.College of Marine Science and Technology, Zhejiang Ocean University, Zhoushan 316022, China; 2.SINOPEC Luoyang Petrochemical Company, Luoyang 471110, China; 3.Zhejiang Provincial Key Laboratory of Petrochemical Pollution Control, Zhejiang Ocean University, Zhoushan 316022, China
Abstract:In this study, salt-tolerant denitrifying activated sludge (DAS) and denitrifying bacterial agents (DBA) were used as inoculants to start sequential batch biofilm systems (SBBRs) treating high-sulfate nitrogenous wastewater. The results showed that the start-up period of SBBRs was short (6-11 d) with different sources of inoculants and carriers at salinity of 1% (12.5 g·L−1 SO42− and 5 g·L−1 NaCl), of which the start-up period of SBBRs was reduced with DAS as inoculants or carriers pretreatment via sludge leaching. After upgrading SO42− mass concentrations to 25 g·L−1 (salinity of 2%) and 37.5 g·L−1 (salinity of 3%), SBBRs were still able to maintain the nitrate reduction rates higher than 90%. The complete denitrification (>98%) occurred in SBBRs with suspended carrier at salinity of 3%, which was significantly higher than that (91.1±11.7)% of SBBR with biological rope carrier. The TN removal efficiency of SBBRs consistently maintained at >90% at the theoretical TOC/TN ratios of 1.4-7. SBBRs were further used to treat high sulfate (2.7%) and nitrogen rich (TN≈200 mg·L−1) wastewater at a TOC/TN ratio of 2, and stable and highly efficient TN removal occurred after the system adapted to acclimation, and higher reduction rates (>99%) and stability in the suspended carrier were also achieved than those in carrier biological rope (>90%). The nitrate reduction pathway in the system was dominated by denitrification without significant dissimilatory nitrate reduction to ammonium and sulfate reduction.
Keywords:salt-tolerant compound bacteria  bioaugmentation  sulfate  bacterial source  carrier  C  N ratio
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