污水厂生物处理单元工艺状态下曝气性能测定与评价
Determination and evaluation of biological treatment unit aeration performance under process state in sewage treatment plant
-
摘要: 以上海竹园第二污水处理厂2号生物好氧处理单元为研究对象,采用工艺状态曝气充氧性能测定仪对曝气器性能进行现场测定,通过核算氧利用率、曝气均匀性指数、曝气效率综合影响因子等指标,评价该厂曝气器日常运行状态,分析曝气系统在控制上的不足,并针对性地提出优化方案。结果表明,工艺状态下曝气器氧利用率与清水条件下相比下降19.22%~23.78%,曝气均匀性指数在0.80~1.34的范围内,曝气效率综合影响因子偏低,充分表明2号生物好氧处理单元部分曝气器存在污染或老化的问题。该厂的曝气系统具有较大的优化潜力,性能评价结果可以为曝气器科学管理维护及水厂的运行优化提供指导。
-
关键词:
- 曝气充氧性能测定仪 /
- 氧利用率 /
- 曝气均匀性指数 /
- 曝气效率综合影响因子
Abstract: Taking the No.2 biological aerobic treatment unit of the Shanghai Zhuyuan Sewage Treatment Plant No.2 as the research object in this study, the aerator performance was measured using the process state aeration oxygenation performance tester. By calculating the oxygen transfer efficiency, aeration uniformity index and comprehensive impact factor of aeration efficiency, the daily operating status of the aerator was valuated, to analyze the shortage of aeration system in control and propose the targeted optimization program. Results showed that the oxygen transfer efficiency of the aerator in process state decreased from 19.22% to 23.78% compared to that in fresh water. The aeration uniformity index was in the range of 0.80 to 1.34,and the comprehensive impact factor of aeration efficiency is relatively low, which fully indicated that some aerators in the No.2 biological aerobic treatment unit have problems of contamination or aging. The aeration system has a large potential for optimization, moreover, the performance evaluation results can provide guidance for the management and maintenance of the aerator and the optimal running of the sewage treatment plant. -
[1] 高廷耀,顾国维主编.水污染控制工程[M].1版.北京:高等教育出版社,1989 [2] 顾国维.水污染治理技术研究[M].1版.上海:同济大学出版社,1997 [3] BERNARD J, DAVIA P.Energy autonomy in the wastewater treatment process[J].Journal,1980,2(3):587-596 [4] FERRER J, RODRIGO M A, SECO A, et al.Energy saving in the aeration process by fuzzy logic control[J].Water Science & Technology,1998,8(3):209-217 [5] XUE Y M, WANG B, ZHU J G, et al.Improvement of cleaning scheme of microporous aerator and its execution effect[J].China Water & Wastewater,2011,7(10):98-100 [6] 中华人民共和国住房和城乡建设部.曝气器清水充氧性能测定:CJ/T 475-2015[S].北京:中国标准出版社, 2015 [7] LARSON L,ROSSO D,LEU S Y B, et al.Energy-conservation in fine pore diffuser installations in activated sludge processes[D].Los Angeles(US):University of California-Los Angeles, 2007 [8] REDMON D.Oxygen transfer efficiency measurements in mixed liquor using off-gas techniques[J].Journal Water Pollution Control Federation,1983,5(11):1338-1347 [9] MICHAEL K.Aeration theory and aeration device[R].Los Angeles:University of California,2010 [10] GARRIDO-BASERBA M, SOBHANI R, ASVAPATHANAGUL P, et al.Modelling the link amongst fine-pore diffuser fouling, oxygen transfer efficiency, and aeration energy intensity[J].Water Research,2017,1:127-139 [11] American Society of Civil Engineers.Standard Guidelines for In-Process Oxygen Transfer Testing[M].New York:American Society of Civil Engineers, 1997 [12] ROSSO D, LIBRA J A, WIEHE W, et al.Membrane properties change in fine-pore aeration diffusers: Full-scale variations of transfer efficiency and headloss[J].Water Research,2008,2(10/11):2640-2648 [13] 崔玉川.城市污水厂处理设施设计计算[M].2版.北京:化学工业出版社, 2011 [14] 李小冬,齐鲁,刘国华,等.通气量对微孔曝气器充氧性能影响的中试研究[J].中国给水排水,2014,30(5):81-84 [15] 李宾祥.污水处理系统曝气设备氧转移能力及α值影响因素研究[D].青岛:青岛理工大学,2016
计量
- 文章访问数: 2785
- HTML全文浏览数: 2378
- PDF下载数: 551
- 施引文献: 0