Eawag, Swiss Federal Institute of Aquatic Science and Technology, 8600 Dübendorf, Switzerland.
Water Res. 2015 Jan 1;68:127-39. doi: 10.1016/j.watres.2014.09.036.
Nitrogen (N) removal from high-strength wastewater can be accomplished in single-stage combined nitritation-anammox reactors with suspended growth biomass composed of floccular sludge, granular sludge, or of any mix of these 2 different sludge fractions. To date, the influence of floccular biomass on granular sludge reactor performance and stability has not been investigated experimentally or numerically. To address this knowledge gap, two 1D multi-species models were developed in Aquasim to assess the importance of small levels of flocs in putatively granular sludge combined nitritation-anammox reactors for different bulk oxygen concentrations and organics loads. The models included the growth and decay of aerobic ammonium-oxidizing organism (AOO), nitrite-oxidizing organisms (NOO), heterotrophic organisms (OHO), and anammox organisms (AMO) in exclusively granular sludge reactors, and in granular sludge reactors with small levels (∼5% of total biomass) of flocs. While maximum N removal efficiencies were similar for both model structures, floc addition led to a lower optimal dissolved oxygen concentration (DO) as well as a narrower maximum N removal peak, suggesting that small levels of floccular material may decrease process robustness to bulk oxygen changes. For some DO levels, this led to drastic efficiency drops. Furthermore, floc addition also led to substantial segregation in activity and microbial population distribution, with AOO, NOO and OHO concentrated in flocs and AMO concentrated in granules. Increased organic loading (COD:N = 4:3) improved maximum N removal efficiency in both model structures, but yielded substantially different predictions for optimal DO setpoint and process robustness to variations in DO. Taken together, our results indicate that even small levels of floccular biomass in biofilm reactors can have profound implications for reactor performance and optimization and for segregation of linked microbial processes, and suggest that the common practice of neglecting small levels of floccular material in biofilm models and in practice may lead to erroneous predictions.
从高强度废水中去除氮(N)可以在悬浮生长生物量的单级组合亚硝化-厌氧氨氧化反应器中完成,悬浮生长生物量由絮状污泥、颗粒污泥或这两种不同污泥部分的任何混合物组成。迄今为止,絮状生物量对颗粒污泥反应器性能和稳定性的影响尚未通过实验或数值进行研究。为了弥补这一知识空白,在 Aquasim 中开发了两个 1D 多物种模型,以评估在不同的总氧浓度和有机物负荷下,少量絮体在假定的颗粒污泥组合亚硝化-厌氧氨氧化反应器中对颗粒污泥反应器性能和稳定性的重要性。这些模型包括专用于颗粒污泥反应器中以及含有少量(总生物量的∼5%)絮体的颗粒污泥反应器中好氧氨氧化菌(AOO)、亚硝酸盐氧化菌(NOO)、异养菌(OHO)和厌氧氨氧化菌(AMO)的生长和衰减。虽然两种模型结构的最大 N 去除效率相似,但絮体的添加导致最佳溶解氧浓度(DO)降低,最大 N 去除峰值变窄,这表明少量絮体物质可能会降低工艺对总氧变化的鲁棒性。对于某些 DO 水平,这会导致效率急剧下降。此外,絮体的添加还导致活性和微生物种群分布的显著分离,AOO、NOO 和 OHO 集中在絮体中,而 AMO 集中在颗粒中。增加有机负荷(COD:N=4:3)提高了两种模型结构的最大 N 去除效率,但对最佳 DO 设定值和 DO 变化的工艺鲁棒性产生了截然不同的预测。总的来说,我们的结果表明,即使在生物膜反应器中存在少量的絮状生物质,也会对反应器性能和优化以及相关微生物过程的分离产生深远的影响,并表明在生物膜模型和实践中忽略少量絮状物质的常见做法可能会导致错误的预测。