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Modeling of Activated Sludge Bioreactor for BOD degradation in Industrial Wastewater

机译:工业废水中BOD降解的活性污泥生物反应器建模

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A model for an activated sludge bioreactor, which describes the dynamic behavior of the substrate-Biological Oxygen Demand (BOD) utilization and biomass growth, is developed. The activated sludge was modeled as system of Continuous stirred tank bioreactor (CSTR) operating isothermally. The model was solved numerically by employing the fourth order Runge-Kutta algorithm and simulated using Matlab program. The model prediction of BOD degradation (31.35mg/l) as compared to plant data (30.0mg/l) showed a deviation of 4.5%. The model simulations reveal 16h as the optimum hydraulic retention time and a recycle ratio of 1.0 for an industrial wastewater treatment plant with MLVSS of 2400mg/l and BOD concentration of 250mg/l. These results, which are in good agreement with the plant design parameters, imply that the WWT plant could be described using system of CSTR configuration.
机译:建立了用于描述污泥基质动态行为的活性污泥生物反应器模型-生物需氧量(BOD)利用率和生物量增长。将活性污泥建模为等温运行的连续搅拌槽生物反应器(CSTR)系统。使用四阶Runge-Kutta算法对模型进行数值求解,并使用Matlab程序进行仿真。与工厂数据(30.0mg / l)相比,BOD降解(31.35mg / l)的模型预测显示偏差为4.5%。模型仿真显示,对于MLVSS为2400mg / l和BOD浓度为250mg / l的工业废水处理厂,最佳水力停留时间为16h,循环比为1.0。这些结果与电厂设计参数非常吻合,表明可以使用CSTR配置系统描述WWT电厂。

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