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Anaerobic ammonium oxidation of ammonium-rich waste streams in fixed-bed reactors

机译:固定床反应器中富铵废水的厌氧铵氧化

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The feasibility of anaerobic ammonium oxidation (Anammox) in fixed-bed reactors was evaluated on laboratory and pilot scales. Using synthetic wastewater, the specific nitrogen removal rate was increased from 0.05-0.1 kgNm~(-3)_(reactor)d~(-1) to 0.35-0.38 kgNm~(-3)_(reactor)d~(-1) within ayear (T= 22-27℃) in all applications. However, the anammox activity was seriously and repeatedly inhibited at prolonged high nitrite concentrations (e.g. six days at 30-50 gNO_2-Nm~(-3)) and recovery was always a lengthy process. But even at a moderate nitrite concentration (11 ± 10 gNO_2-Nm~(-3)), the observed specific growth rate was only 0.018 d~1 at 26.4 ± 0.8℃, which corresponds to approximately 0.025 d~(-1) at 30℃ (doubling time: 28 days). In a second experimental period for another 250 days, one of the laboratory reactors was fed with partially nitrified sludge liquors from a domestic wastewater treatment plant (WWTP). In this case, the specific elimination rate was as high as 3.5 kgNm~(-3)_(reactor)d~(-1)at 26-27℃. Independently of the feed, the average nitrogen elimination rate lay between 80-85% in all applications. An appropriate hydraulic design is essential to prevent clogging and local nitrite inhibition in fixed-bed reactors.
机译:在实验室和中试规模上评估了固定床反应器中厌氧铵氧化(Anammox)的可行性。使用合成废水,比氮去除率从0.05-0.1 kgNm〜(-3)_(反应器)d〜(-1)增加到0.35-0.38 kgNm〜(-3)_(反应器)d〜(-1) )一年内(T = 22-27℃)进行所有应用。然而,在长时间的高亚硝酸盐浓度下(例如在30-50 gNO_2-Nm〜(-3)下六天),厌氧氨氧化活性受到严重和反复的抑制,恢复始终是一个漫长的过程。但是即使在适度的亚硝酸盐浓度下(11±10 gNO_2-Nm〜(-3)),在26.4±0.8℃下观察到的比生长速率也仅为0.018 d〜1,相当于在0.06 d〜(-1)时。 30℃(倍增时间:28天)。在又一个250天的第二个实验期内,向其中一个实验室反应器供入了来自生活废水处理厂(WWTP)的部分硝化的污泥液。在这种情况下,在26-27℃时比清除率高达3.5 kgNm〜(-3)_(反应器)d〜(-1)。与进料无关,在所有应用中,平均氮消除率在80%至85%之间。适当的水力设计对于防止固定床反应器中的堵塞和局部亚硝酸盐抑制至关重要。

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