Tomaszek J A, Grabas M
Rzeszów University of Technology, Department of Environmental and Chemistry Engineering 2 W. Pola Street, 35-959 Rzeszów, Poland.
Environ Technol. 2007 May;28(5):555-63. doi: 10.1080/09593332808618815.
Experiments were carried out on a laboratory scale with four moving bed biofilm reactors (MBBRs) with step-feed. The first and third reactors were anoxic and the second and fourth aerobic. The aim of this experiment was to investigate the system's capacity for, and efficiency of organic carbon and nitrogen removal. Four tests examined the effect of the distribution between stages of raw stream wastewater, the recirculation ratio, and the effect of increasing nitrogen and organic carbon loads on nitrogen and carbon removal. It was concluded that in this system the proper selection of recirculation ratio R, and the parameters of the coefficient of raw wastewater stream distribution theta ensures greater efficiency of nitrogen removal than activated sludge systems.
在实验室规模下,使用四个具有分步进水的移动床生物膜反应器(MBBR)进行了实验。第一和第三个反应器为缺氧型,第二和第四个为好氧型。本实验的目的是研究该系统去除有机碳和氮的能力及效率。四项测试考察了原废水在各阶段的分配、回流比的影响,以及增加氮和有机碳负荷对氮和碳去除的影响。得出的结论是,在该系统中,正确选择回流比R以及原废水流分配系数θ的参数,可确保比活性污泥系统具有更高的氮去除效率。