Gibbs B M, Shephard L R, Third K A, Cord-Ruwisch R
School of Biological Sciences and Biotechnology, Murdoch University, Murdoch, Western Australia 6150, Australia.
Water Sci Technol. 2004;50(10):181-8.
For economic and efficient nitrogen removal from wastewater treatment plants via simultaneous nitrification and denitrification the nitrification process should stop at the level of nitrite such that nitrite rather than nitrate becomes the substrate for denitrification. This study aims to contribute to the understanding of the conditions that are necessary to improve nitrite reduction over nitrite oxidation. Laboratory sequencing batch reactors (SBRs) were operated with synthetic wastewater containing acetate as COD and ammonium as the nitrogen source. Computer controlled operation of the reactors allowed reproducible simultaneous nitrification and denitrification (SND). The oxygen supply was kept precisely at a low level of 0.5 mgL(-1) and bacterial PHB was the only electron donor available for denitrification. During SND little nitrite or nitrate accumulated (< 20% total N), indicating that the reducing processes were almost as fast as the production of nitrite and nitrate from nitrification. Nitrite spiking tests were performed to investigate the fate of nitrite under different oxidation (0.1-1.5 mgL(-1) of dissolved oxygen) and reduction conditions. High levels of reducing power were provided by allowing the cells to build up to 2.5 mM of PHB. Nitrite added was preferentially oxidised to nitrate rather than reduced even when dissolved oxygen was low and reducing power (PHB) was excessively high. However, the presence of ammonium enabled significant reduction of nitrite under low oxygen conditions. This is consistent with previous observations in SBR where aerobic nitrite and nitrate reduction occurred only as long as ammonium was present. As soon as ammonium was depleted, the rate of denitrification decreased significantly. The significance of the observed strongly stimulating effect of ammonium on nitrite reduction under SND conditions is discussed and potential consequences for SBR operation are suggested.
为了通过同步硝化反硝化作用从污水处理厂中经济高效地去除氮,硝化过程应在亚硝酸盐水平停止,使亚硝酸盐而非硝酸盐成为反硝化的底物。本研究旨在有助于理解改善亚硝酸盐还原而非亚硝酸盐氧化所需的条件。实验室序批式反应器(SBR)以含有乙酸盐作为化学需氧量(COD)和铵作为氮源的合成废水运行。反应器的计算机控制操作实现了可重复的同步硝化反硝化(SND)。氧气供应精确保持在0.5 mgL(-1)的低水平,细菌聚-β-羟基丁酸酯(PHB)是唯一可用于反硝化的电子供体。在SND过程中,几乎没有亚硝酸盐或硝酸盐积累(<总氮的20%),表明还原过程几乎与硝化作用产生亚硝酸盐和硝酸盐的速度一样快。进行了亚硝酸盐加标试验,以研究在不同氧化(0.1 - 1.5 mgL(-1)溶解氧)和还原条件下亚硝酸盐的去向。通过使细胞积累至2.5 mM的PHB提供了高水平的还原能力。即使溶解氧低且还原能力(PHB)过高,添加的亚硝酸盐也优先被氧化为硝酸盐而非被还原。然而,铵的存在使得在低氧条件下亚硝酸盐能够显著还原。这与之前在SBR中的观察结果一致,即在有铵存在时才会发生好氧亚硝酸盐和硝酸盐还原。一旦铵耗尽,反硝化速率显著下降。讨论了在SND条件下观察到铵对亚硝酸盐还原的强烈刺激作用的意义,并提出了对SBR运行可能产生的后果。