Lou In Chio, de los Reyes Francis L
Department of Civil, Construction, and Environmental Engineering, North Carolina State University, Raleigh, North Carolina 27695, USA.
Biotechnol Bioeng. 2008 Oct 1;101(2):327-36. doi: 10.1002/bit.21886.
We hypothesized that the growth rates of filaments and floc formers in activated sludge are affected by the combination of kinetic selection (Lou and de los Reyes, Biotechnol Bioeng 92(6): 729-739, 2005b) and substrate diffusion limitation (Martins et al., Water Res 37:2555-2570, 2003). To clarify the influence of these factors in explaining filamentous bulking, a conceptual framework was developed in this study. The framework suggests the existence of three different regions corresponding to bulking, non-bulking, and intermediate regions, based on substrate concentration. In the bulking and non-bulking regions, kinetic growth differences control the competition process, and filaments or floc formers dominate, respectively. In the intermediate region, substrate diffusion limitation, determined by the floc size, plays the major role in causing bulking. To test this framework, sequencing batch reactors (SBRs) were operated with influent COD of 100, 300, 600, and 1,000 mg/L, and the sludge settleability was measured at various floc size distributions that were developed using different mixing strengths. The experimental data in the bulking and intermediate regions supported the proposed framework. A model integrating the two factors was developed to simulate the substrate concentrations at different depths and floc sizes under intermittently feeding conditions. The modeling results confirmed that substrate diffusion limitation occurs inside the flocs at a certain range of activated sludge floc sizes over the operation cycle, and provided additional support for the proposed framework.
我们假设活性污泥中丝状菌和絮体形成菌的生长速率受动力学选择(Lou和de los Reyes,《生物技术与生物工程》92(6): 729 - 739,2005b)和底物扩散限制(Martins等人,《水研究》37:2555 - 2570,2003)共同作用的影响。为阐明这些因素对丝状膨胀的影响,本研究构建了一个概念框架。该框架表明,基于底物浓度存在三个不同区域,分别对应膨胀区、非膨胀区和中间区。在膨胀区和非膨胀区,动力学生长差异控制竞争过程,丝状菌或絮体形成菌分别占主导。在中间区,由絮体大小决定的底物扩散限制是导致膨胀的主要因素。为验证该框架,对序批式反应器(SBR)进行了运行,进水化学需氧量(COD)分别为100、300、600和1000 mg/L,并在使用不同混合强度形成的各种絮体大小分布下测量污泥沉降性能。膨胀区和中间区的实验数据支持了所提出的框架。开发了一个整合这两个因素的模型,以模拟间歇进料条件下不同深度和絮体大小的底物浓度。建模结果证实,在运行周期内,在一定范围的活性污泥絮体大小下,絮体内会发生底物扩散限制,为所提出的框架提供了额外支持。