van Dongen U, Jetten M S, van Loosdrecht M C
Department of Biotechnology, Faculty of Applied Sciences, Delft Univ. of Technology, Julianalaan 67, NL 2828 BC Delft.
Water Sci Technol. 2001;44(1):153-60.
The treatment of ammonium rich wastewater, like sludge digester effluent, can be significantly improved when new biotechnological processes are introduced. In this paper, the combination of a partial nitrification process (SHARON) and anoxic ammonium oxidation (Anammox) process for the treatment of ammonia rich influents is evaluated. Herein the combined process has been studied with sludge recycle liquor from the WWTP Rotterdam-Dokhaven. The SHARON process was operated stably for more than 2 years in a 10ICSTR under continuous aeration with a HRT of 1 day. The ammonia in the sludge liquor was converted by 53% to nitrite only. During the test period no formation of nitrate was observed. The effluent of the SHARON process was ideally suited as influent for the Anammox reactor. The Anammox process was operated as a granular sludge SBR-process. More than 80% of the ammonia was converted into dinitrogen gas at a load of 1.2 kgN/m3 per day. Planctomycete-like bacteria dominated the mixed community of the Anammox reactor, and only a small percentage of the population consisted of aerobic ammonium-oxidizing bacteria. This showed that the ammonium-oxidizers in the effluent of the SHARON process did not accumulate in the SBR. The test period showed that the combined SHARON-Anammox system can work stably over long periods and the process is ready for full-scale implementation.
当引入新的生物技术工艺时,富含铵的废水(如污泥消化池出水)的处理效果可得到显著改善。本文评估了部分硝化工艺(SHARON)和厌氧氨氧化(Anammox)工艺相结合处理高氨进水的效果。在此,采用鹿特丹 - 多哈芬污水处理厂的污泥循环液对该联合工艺进行了研究。SHARON工艺在一个10ICSTR中连续曝气、水力停留时间为1天的条件下稳定运行了两年多。污泥液中的氨仅53%转化为亚硝酸盐。在测试期间未观察到硝酸盐的形成。SHARON工艺的出水非常适合作为厌氧氨氧化反应器的进水。厌氧氨氧化工艺作为颗粒污泥SBR工艺运行。在每天1.2 kgN/m³的负荷下,超过80%的氨转化为氮气。厌氧氨氧化反应器的混合菌群以类浮霉菌为主,只有一小部分是好氧氨氧化细菌。这表明SHARON工艺出水中的氨氧化菌没有在SBR中积累。测试期间表明,SHARON - 厌氧氨氧化联合系统能够长期稳定运行,该工艺已具备全面实施的条件。