Rodgers Michael, Zhan Xin-Min
Department of Civil Engineering, National University of Ireland, Galway, Ireland.
Bioresour Technol. 2004 Jul;93(3):313-9. doi: 10.1016/j.biortech.2003.09.017.
In this study, a biological nitrogen removal process using a vertically moving biofilm system was used to treat synthetic wastewater. The process consisted of two pre-denitrification units, one combined carbonaceous removal/nitrification unit and three nitrification units. Each unit employed biofilm growth on a plastic module. In the anoxic units, the modules were vertically moved, while always submerged, in the bulk fluid; in the aerobic units, they were moved vertically up into the air and down into the wastewater. Three small-scale experiments, having different recirculation ratios and influent loadings, were conducted at a controlled temperature of 11 degrees C. In this system, the carbonaceous removal efficiency was in the range of 94-96% and the total nitrogen removal efficiency was 77-82%. In the anoxic units, the denitrification efficiency was 94-98% and the areal denitrification rates, based on the surface area of the biofilm modules, were 2.9-3.8 g NO3-N/(m2 x d). The nitrification efficiency occurring in the aerobic tanks was up to 95% and the maximum areal ammonium removal rates were 1.3-1.8 g NH4-N/(m2 x d).
在本研究中,采用垂直移动生物膜系统的生物脱氮工艺处理合成废水。该工艺由两个前置反硝化单元、一个碳质去除/硝化组合单元和三个硝化单元组成。每个单元均利用塑料模块上的生物膜生长。在缺氧单元中,模块在主体流体中垂直移动,且始终处于淹没状态;在好氧单元中,它们垂直向上移动到空气中,然后向下移动到废水中。在11摄氏度的控制温度下进行了三个不同回流比和进水负荷的小规模实验。在该系统中,碳质去除效率在94 - 96%范围内,总氮去除效率为77 - 82%。在缺氧单元中,反硝化效率为94 - 98%,基于生物膜模块表面积的面积反硝化速率为2.9 - 3.8 g NO3-N/(m2·d)。好氧池中发生的硝化效率高达95%,最大面积铵去除率为1.3 - 1.8 g NH4-N/(m2·d)。