Rittstieg K, Robra K H, Somitsch W
Institute for Environmental Biotechnology, Graz, Austria.
Appl Microbiol Biotechnol. 2001 Sep;56(5-6):820-5. doi: 10.1007/s002530100696.
An industrial wastewater containing a total Kjeldahl nitrogen (TKN) of 12.80 g l(-1) was treated in a continuously fed activated sludge reactor. The main contaminant was urea (21.52 g l(-1)), together with minor amounts of the nitrification inhibitor dicyandiamide (0.46 g l(-1)) and free ammonia (0.56 g l(-1)). The wastewater was diluted 1:1 with water and treated under alkaline conditions (pH 9.4), enabling the simultaneous hydrolysis of urea and stripping of free ammonia in one aerobic reactor. Experiments were conducted to eliminate the remaining ammonia in a separate treatment unit by nitrification/denitrification. An adapted nitrifying bacterial population was isolated which was able to nitrify at a rate of 0.1 g nitrogen l(-1) day(-1) at a dicyandiamide concentration of 0.22 g l(-1). However, this was found to be too slow for an industrial-scale operation. Therefore, separate stripping with air or steam after pH adjustment to > or =10.5 is proposed. The diluted wastewater was treated with a hydraulic retention time of 6 days, corresponding to a volumetric nitrogen loading rate of 1.1 g nitrogen l(-1) day(-1) with an overall TKN reduction of 78.0%.
一种总凯氏氮(TKN)含量为12.80 g l⁻¹的工业废水在连续进料的活性污泥反应器中进行处理。主要污染物是尿素(21.52 g l⁻¹),还有少量的硝化抑制剂双氰胺(0.46 g l⁻¹)和游离氨(0.56 g l⁻¹)。该废水与水按1:1稀释,并在碱性条件(pH 9.4)下处理,使得尿素能在一个好氧反应器中同时水解以及游离氨能被汽提。通过硝化/反硝化在一个单独的处理单元中进行实验以去除剩余的氨。分离出了一种适应性硝化细菌群体,其在双氰胺浓度为0.22 g l⁻¹时能够以0.1 g氮l⁻¹天⁻¹的速率进行硝化。然而,发现这对于工业规模操作来说太慢了。因此,建议在将pH调节至≥10.5后用空气或蒸汽进行单独汽提。稀释后的废水以6天的水力停留时间进行处理,这对应于1.1 g氮l⁻¹天⁻¹的体积氮负荷率,总凯氏氮的去除率为78.0%。