Startup of reactors for anoxic ammonium oxidation: Experiences from the first full-scale anammox reactor in Rotterdam

被引:1041
作者
van der Star, Wouter R. L.
Abma, Wiebe R.
Blommers, Dennis
Mulder, Jan-Willem
Tokutomi, Takaaki
Strous, Marc
Picioreanu, Cristian
Van Loosdrecht, Mark C. M.
机构
[1] Delft Univ Technol, Dept Biotechnol, NL-2628 BC Delft, Netherlands
[2] Paques BV, NL-8561 EL Balk, Netherlands
[3] Waterschap Hollandse Delta, NL-3300 AL Dordrecht, Netherlands
[4] Kurita Water Ind Ltd, Nogimachi, Tochigi 3290105, Japan
[5] Radboud Univ Nijmegen, Dept Microbiol, NL-6525 ED Nijmegen, Netherlands
关键词
nitrogen removal; reject water treatment; anammox; anaerobic ammonium oxidation; brocadia anammoxidans; reactor scale-up; quantitative PCR; real-time PCR;
D O I
10.1016/j.watres.2007.03.044
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The first full-scale anammox reactor in the world was started in Rotterdam (NL). The reactor was scaled-up directly from laboratory-scale to full-scale and treats up to 750 kg-N/d. In the initial phase of the startup, anammox conversions could not be identified by traditional methods, but quantitative PCR proved to be a reliable indicator for growth of the anammox population, indicating an anammox doubling time of 10-12 days. The experience gained during this first startup in combination with the availability of seed sludge from this reactor, will lead to a faster startup of anammox reactors in the future. The anammox reactor type employed in Rotterdam was compared to other reactor types for the anammox process. Reactors with a high specific surface area like the granular sludge reactor employed in Rotterdam provide the highest volumetric loading rates. Mass transfer of nitrite into the biofilm is limiting the conversion of those reactor types that have a lower specific surface area. Now the first full-scale commercial anammox reactor is in operation, a consistent and descriptive nomenclature is suggested for reactors in which the anammox process is employed. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4149 / 4163
页数:15
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