A mathematical model for the activated sludge process with a sludge disintegration unit

IF 1 Q4 ENGINEERING, CHEMICAL Chemical Product and Process Modeling Pub Date : 2022-05-03 DOI:10.1515/cppm-2021-0064
Salman S. Alsaeed, M. Nelson, M. Edwards, A. Msmali
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Abstract

Abstract We develop and investigate a model for sludge production in the activated sludge process when a biological reactor is coupled to a sludge disintegration unit (SDU). The model for the biological reactor is a slimmed down version of the activated sludge model 1 in which only processes related to carbon are retained. Consequently, the death-regeneration concept is included in our model which is an improvement on almost all previous models. This provides an improved representation of the total suspended solids in the biological reactor, which is the key parameter of interest. We investigate the steady-state behaviour of this system as a function of the residence time within the biological reactor and as a function of parameters associated with the operation of the SDU. A key parameter is the sludge disintegration factor. As this parameter is increased the concentration of total suspended solids within the biological reactor decreases at the expense increasing the chemical oxygen demand in the effluent stream. The existence of a maximum acceptable chemical oxygen demand in the effluent stream therefore imposes a maximum achievable reduction in the total suspended solids. This paper improves our theoretical understanding of the utility of sludge disintegration as a means to reduce excess sludge formation. As an aside to the main thrust of our paper we investigate the common assumption that the sludge disintegration processes occur on a much shorter timescale than the biological processes. We show that the disintegration processes must be exceptional slow before the inclusion of the biological processes becomes important.
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具有污泥分解装置的活性污泥过程的数学模型
摘要我们开发并研究了一个生物反应器与污泥分解装置(SDU)耦合时活性污泥过程中污泥产生的模型。生物反应器的模型是活性污泥模型1的精简版本,其中仅保留与碳有关的过程。因此,死亡再生概念包含在我们的模型中,这是对几乎所有先前模型的改进。这提供了生物反应器中总悬浮固体的改进表示,这是感兴趣的关键参数。我们研究了该系统的稳态行为,它是生物反应器内停留时间的函数,也是与SDU操作相关的参数的函数。一个关键参数是污泥崩解因子。随着该参数的增加,生物反应器内总悬浮固体的浓度以增加流出物流中的化学需氧量为代价而降低。因此,在流出物流中存在最大可接受的化学需氧量使得总悬浮固体的可实现的最大减少。本文提高了我们对污泥分解作为减少过量污泥形成的一种手段的效用的理论理解。除了我们论文的主旨之外,我们还研究了一个常见的假设,即污泥分解过程发生的时间比生物过程短得多。我们表明,在纳入生物过程变得重要之前,分解过程必须非常缓慢。
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来源期刊
Chemical Product and Process Modeling
Chemical Product and Process Modeling ENGINEERING, CHEMICAL-
CiteScore
2.10
自引率
11.10%
发文量
27
期刊介绍: Chemical Product and Process Modeling (CPPM) is a quarterly journal that publishes theoretical and applied research on product and process design modeling, simulation and optimization. Thanks to its international editorial board, the journal assembles the best papers from around the world on to cover the gap between product and process. The journal brings together chemical and process engineering researchers, practitioners, and software developers in a new forum for the international modeling and simulation community. Topics: equation oriented and modular simulation optimization technology for process and materials design, new modeling techniques shortcut modeling and design approaches performance of commercial and in-house simulation and optimization tools challenges faced in industrial product and process simulation and optimization computational fluid dynamics environmental process, food and pharmaceutical modeling topics drawn from the substantial areas of overlap between modeling and mathematics applied to chemical products and processes.
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