[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