Larrea L, Abad A, Gayarre J
CEIT, Environmental Engineering Section, 20018, San Sebastian, Spain.
Water Sci Technol. 2003;48(11-12):419-28.
The effect on NH4-N removal rates in nitrification biofilters of filtered biodegradable COD and particulate COD leaving predenitrification biofilters was studied in a lab scale plant configured with the separated system of biofilters for secondary nitrogen removal from urban wastewaters. Applying a typical COD load of 11 kg/m3 x day to the predenitrification biofilter and maximizing its COD removal by adding nitrates or by operating an improved control of the internal recycle, only 60% removal of filtered biodegradable COD was found. This value corresponds to the complete removal of the readily biodegradable substrate (30% of influent filtered COD) and 36% of filtered slowly biodegradable substrate (50% of influent COD). The remaining 64% of the latter entered the nitrification biofilter, causing competition between heterotrophs and nitrifiers for dissolved oxygen in the inner layers of the biofilm. Consequently the nitrification rate had relatively low values (0.5 kgN/m3 x d) at 14 degrees C despite using dissolved oxygen levels of 6 mg/l. This behaviour may explain the lower nitrification rates obtained in some cases of nitrification biofilters compared to those in tertiary nitrification after activated sludge processes. The particulate COD entering the nitrification biofilter is associated with the suspended solids leaving the denitrification biofilter which are adsorbed by the external layers of the biofilm, increasing its thickness. The activity of the nitrifiers was affected because of a lack of oxygen when the thickness was left to grow considerably. Therefore no significant particulate COD effect is expected to occur as long as backwashing is carried out with the appropriate frequency.
在一个采用生物滤池分离系统进行城市污水二级脱氮的实验室规模装置中,研究了预脱硝生物滤池流出的过滤后可生物降解化学需氧量(COD)和颗粒状COD对硝化生物滤池中氨氮去除率的影响。向预脱硝生物滤池施加典型的COD负荷11 kg/m³·天,并通过添加硝酸盐或改进内部循环控制来最大化其COD去除率,结果发现仅去除了60%的过滤后可生物降解COD。该值对应于易生物降解底物(进水过滤后COD的30%)的完全去除以及36%的过滤后缓慢生物降解底物(进水COD的50%)的去除。后者剩余的64%进入硝化生物滤池,导致异养菌和硝化菌在生物膜内层争夺溶解氧。因此,尽管溶解氧水平为6 mg/l,但在14℃时硝化速率相对较低(0.5 kgN/m³·天)。这种行为可能解释了在某些硝化生物滤池情况下获得的硝化速率低于活性污泥法后三级硝化的情况。进入硝化生物滤池的颗粒状COD与离开反硝化生物滤池的悬浮固体相关,这些悬浮固体被生物膜外层吸附,增加了其厚度。当厚度大幅增加时,由于缺氧,硝化菌的活性受到影响。因此,只要以适当的频率进行反冲洗,预计不会出现明显的颗粒状COD影响。