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Simulation of tertiary denitrification with methanol in an upflow biofilter

机译:上流式生物滤池中甲醇三次脱氮的模拟

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A biofilm model for the simulation of denitrification with methanol in a 3 m high upflow biofilter is presented. This model considers mass transfer at the bulklbiofilm interface, mass transport in the liquid phase of the biofilter and mass transport and substrate utilization in the biofilm. The biofilter was run with different filtration rates between 11 and 29 m/h. The methanol dosage ranged between 2.6 and 3.8 g CH3OH/g NO3-N. The denitrification rate ranged between 1 and 4.8 kg/m(3)d and depended mainly on the filtration rate and the methanol dosage. To carry out a simulation, the biofilter was divided into five segments. Each segment was simulated as a totally mixed reactor tank. The experimental results were used to fit the maximum growth rate of the denitrifying bacteria and the yield coefficient for the process growth in the simulation. The simulation of nitrate and COD concentration in the effluent matches very well the experimental results even when the filtration rate changed. It was also possible to simulate the measured concentration profiles in the biofilter with the presented model. [References: 9]
机译:提出了一个生物膜模型,用于模拟3 m高上流生物滤池中甲醇的反硝化作用。该模型考虑了在大块生物膜界面的传质,生物滤池液相的质量传递以及生物膜的质量传递和底物​​利用率。生物滤池以11至29 m / h的不同过滤速率运行。甲醇的剂量范围为2.6至3.8 g CH3OH / g NO3-N。反硝化速率介于1和4.8 kg / m(3)d之间,并且主要取决于过滤速率和甲醇用量。为了进行模拟,将生物滤池分为五个部分。将每个段模拟为完全混合的反应罐。实验结果用于拟合反硝化细菌的最大生长速率和模拟过程生长的产量系数。即使过滤速度发生变化,废水中硝酸盐和COD浓度的模拟结果也与实验结果非常吻合。也可以使用提出的模型来模拟生物滤池中测得的浓度分布。 [参考:9]

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