EXPRESS CALCULATION OF OXYGEN REGIME IN WASTEWATER FACILITIES

M.M. Biliaiev, P. Mashykhina, L.H. Tatarko, A.O. Chirkov, M.V. Chyrva
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Abstract

Problem statement. The efficiency of biological water purification depends significantly on the concentration of dissolved oxygen in the volume of the bioreactor. But during the operation of bioreactors, the oxygen regime changes, so it is important to predict the oxygen concentration for different modes of operation of treatment plants. Simplified mathematical models are used to calculate the oxygen regime, but these models are designed for typical bioreactors. An important task is the development of effective multivariate numerical models for evaluating the oxygen regime in reactors of different geometric shapes, which differ from “classical” reactors. The purpose of the article. Development of a CFD model for operational evaluation of the oxygen regime in bioreactors. Methodology. For mathematical modeling of the oxygen regime in the bioreactor, a two-dimensional mass transfer equation is used, which takes into account the place of oxygen supply from the aerator located in the building, the hydrodynamics of the flow in the bioreactor, and the diffusion process. The potential motion model was used to solve the hydrodynamic problem. Numerical integration of modeling equations is carried out by using finite-difference splitting schemes. At each splitting step, the difference equations are solved using explicit schemes. This allows a simple computer implementation of the numerical model. Scientific novelty. A multifactor two-dimensional CFD model was developed, which allows for a quick assessment of the oxygen regime in a bioreactor used for wastewater treatment. Practical significance. The developed CFD model and computer code can be used at the stage of designing or re-engineering bioreactors in order to find the optimal location of aerators in the structure. Conclusions. The software implementation of the developed numerical model was carried out. The results of a computational experiment on the study of the wastewater treatment process in a sedimentation tank are presented.
污水处理设施中氧系统的快速计算
问题陈述。生物净水的效率在很大程度上取决于生物反应器容积中的溶解氧浓度。但在生物反应器的运行过程中,氧状态会发生变化,因此预测处理厂不同运行模式下的氧浓度非常重要。人们使用简化的数学模型来计算氧状态,但这些模型是针对典型的生物反应器设计的。一项重要任务是开发有效的多元数值模型,用于评估不同几何形状的反应器(不同于 "经典 "反应器)中的氧状态。本文的目的是开发一个 CFD 模型,用于对生物反应器中的氧状态进行操作评估。方法。为建立生物反应器中氧状态的数学模型,使用了二维传质方程,该方程考虑了位于建筑物内的曝气器的供氧位置、生物反应器中的流体力学以及扩散过程。采用势能运动模型来解决流体力学问题。模型方程的数值积分采用有限差分分割方案。在每个分割步骤中,差分方程都使用显式方案求解。这使得数值模型的计算机实施非常简单。科学新颖性。开发了一个多因素二维 CFD 模型,可快速评估用于废水处理的生物反应器中的氧气机制。实用意义。所开发的 CFD 模型和计算机代码可用于生物反应器的设计或改造阶段,以便找到曝气器在结构上的最佳位置。结论。对所开发的数值模型进行了软件实施。介绍了研究沉淀池废水处理过程的计算实验结果。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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