移动生化池中生物处理废水的模拟研究

M. Biliaiev, M. Lemesh, V. Zadoia, P. Mashykhina, L. Tatarko, Z. Yakubovska
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摘要

目的。本文的主要目的是建立一个数值模型,用于分析具有流动微生物病的反应器中生物废水处理过程。方法。采用非粘性无涡流的流体力学模型,对移动生物病反应器中生物废水处理过程进行了数学建模。在生物反应器表面、固体壁面和上表面计算了建模方程的边界条件;在入口边界处;在大楼的出口边界。为了计算活性污泥和底物在生物反应器中的运动过程,采用了考虑底物和活性污泥对流扩散运动的传质模型。在生物反应器中没有移动微生物载体的部分,生物净水过程将根据Monod模型进行计算。生物反应器中有移动载体部分的生物净水过程根据经验模型分三个阶段进行计算。第一阶段是使用Harremoes模型确定的。在第二阶段,计算生物膜中的底物“消耗”率。在第三阶段,由于对流运动、底物在水流中的扩散以及底物在载体上的生物膜中的破坏,决定了生物污染载体所在区域底物浓度的变化。利用抛物扩散方程对反应器中生物污染载体的混沌运动进行了建模。采用有限差分格式对模拟方程进行数值积分。发现。对所构建的数值模型进行了软件实现。通过计算实验确定了生物反应器不同部位的生物废水处理效率。创意。建立了一个有效的多因子数值模型,可以快速分析带有移动生物滤池的曝气池处理废水的效率。实用价值。所建立的二维数值模型可用于污水生物处理系统设计阶段的串联计算和不同运行条件下生物反应器效率的分析。
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Simulation of Biological Wastewater Treatment in Aerotanks with Moving Biocenosis
Purpose. The main purpose of the article is to develop a numerical model for the analysis of the process of biological wastewater treatment in a reactor with a mobile biocenosis. Methodology. For mathematical modeling of the process of biological wastewater treatment in a reactor with a moving biocenosis, a hydrodynamic model of a non-viscous vortex-free flow is used. We calculated the boundary conditions for the modeling equation on the surfaces of the bioreactor, solid walls, and the upper surface; at the inlet boundary; at the outlet boundary from the building. To calculate the process of movement of activated sludge and substrate in the bioreactor, a mass transfer model is used, which takes into account the convective-diffusion movement of the substrate and activated sludge. The process of biological water purification in that part of the bioreactor where there are no mobile biocenosis carriers will be calculated based on the Monod model. The process of biological water purification in the part of the bioreactor where there are mobile carriers is calculated on the basis of an empirical model in three stages. The first stage is determined using the Harremoes model. At the second stage, the rate of substrate «consumption» in the biofilm is calculated. At the third stage, the change in the substrate concentration in the zone where the biocenosis carriers are located is determined due to convective movement, substrate diffusion in the flow and its destruction in the biofilm on the carriers. The chaotic motion of biocenosis carriers in the reactor is modeled based on the parabolic diffusion equation. Finite-difference schemes are used for numerical integration of modeling equations. Findings. The software implementation of the constructed numerical model is carried out. A computational experiment to determine the efficiency of biological wastewater treatment in different parts of the bioreactor was conducted. Originality. An effective multifactorial numerical model has been created, which allows quick analysis of the efficiency of biological wastewater treatment in an aeration tank with mobile biocenosis carriers. Practical value. The created two-dimensional numerical model can be used for serial calculations at the stage of designing biological wastewater treatment systems and analysis of the efficiency of bioreactors under different operating conditions.
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