Haaksman V A, Schouteren M, van Loosdrecht M C M, Pronk M
Department of Biotechnology, Faculty of Applied Sciences, Delft University of Technology, Van der Maasweg 9, Delft, 2629 HZ, The Netherlands.
Department of Biotechnology, Faculty of Applied Sciences, Delft University of Technology, Van der Maasweg 9, Delft, 2629 HZ, The Netherlands.
Water Res. 2023 Apr 15;233:119803. doi: 10.1016/j.watres.2023.119803. Epub 2023 Feb 27.
There is a growing interest to implement aerobic granular sludge (AGS) in existing conventional activated sludge (CAS) systems with a continuous flow-through configuration. The mode of anaerobic contact of raw sewage with the sludge is an important aspect in the adaptation of CAS systems to accommodate AGS. It remains unclear how the distribution of substrate over the sludge by a conventional anaerobic selector compares to the distribution via bottom-feeding applied in sequencing batch reactors (SBRs). This study investigated the effect of the anaerobic contact mode on the substrate (and storage) distribution by operating two lab-scale SBRs; one with the traditional bottom-feeding through a settled sludge bed similar to full-scale AGS systems, and one where the synthetic wastewater was fed as a pulse at the start of the anaerobic phase while the reactor was mixed through sparging of nitrogen gas (mimicking a plug-flow anaerobic selector in continuous flow-through systems). The distribution of the substrate over the sludge particle population was quantified via PHA analysis, combined with the obtained granule size distribution. Bottom-feeding was found to primarily direct substrate towards the large granular size classes (i.e. large volume and close to the bottom), while completely mixed pulse-feeding gives a more equal distribution of substrate over all granule sizes (i.e. surface area dependant). The anaerobic contact mode directly controls the substrate distribution over the different granule sizes, irrespective of the solids retention time of a granule as an entity. Preferential feeding of the larger granules will enhance and stabilise the granulation compared to pulse-feeding, certainly under less advantageous conditions imposed by real sewage.
在现有的具有连续流通配置的传统活性污泥(CAS)系统中采用好氧颗粒污泥(AGS)的兴趣日益浓厚。原污水与污泥的厌氧接触方式是使CAS系统适应AGS的一个重要方面。传统厌氧选择器中底物在污泥上的分布与序批式反应器(SBR)中采用底部进料的底物分布相比,情况仍不清楚。本研究通过运行两个实验室规模的SBR,研究了厌氧接触方式对底物(和储存)分布的影响;一个采用传统的底部进料,通过类似于全尺寸AGS系统的沉淀污泥床,另一个在厌氧阶段开始时以脉冲形式进料合成废水,同时通过氮气曝气使反应器混合(模拟连续流通系统中的推流厌氧选择器)。通过PHA分析结合获得的颗粒尺寸分布,对底物在污泥颗粒群体上的分布进行了量化。发现底部进料主要将底物导向大颗粒尺寸类别(即大体积且靠近底部),而完全混合的脉冲进料使底物在所有颗粒尺寸上的分布更均匀(即取决于表面积)。厌氧接触方式直接控制底物在不同颗粒尺寸上的分布,而与颗粒作为一个整体的固体停留时间无关。与脉冲进料相比,优先向较大颗粒进料将增强并稳定颗粒化,特别是在实际污水施加的较不利条件下。