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A kinetic analysis and experimental validation of an integrated system of anaerobic filter and biological aerated filter

机译:厌氧滤池和曝气生物滤池集成系统的动力学分析和实验验证

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An anaerobic/aerobic filter (AF/BAF) system was developed treating dairy wastewater. The influent was blended with recirculated effluent to allow for pre-denitrification in the AF followed by nitrification in the BAF. The recirculation ratio ranged 100-300%. The average chemical oxygen demand (COD) removal efficiency was 79.8-86.8% in the AF and the average total nitrogen removal efficiency was 50.5-80.8% in the AF/BAF system. Steady-state mass balances on the AF were used to analyze removal kinetics in the AF. The kinetic model values for effluent COD in the AF were overestimated as compared with experimental data. The integrated suspended and attached biomass growth rates in the AF were estimated. The specific growth rate of the integrated biomass at each recirculation ratios was 0.6213, 0.6647, and 1.2083. 1/day, respectively. The increase in specific growth rate corresponded to increases in biomass sloughing as the recirculation ratio increased.
机译:开发了厌氧/好氧滤池(AF / BAF)系统来处理乳品废水。将进水与再循环废水混合,以允许在AF中进行预脱硝,然后在BAF中进行硝化。再循环率在100-300%的范围内。 AF中平均化学需氧量(COD)去除效率为79.8-86.8%,AF / BAF系统中平均总氮去除率为50.5-80.8%。 AF上的稳态质量平衡用于分析AF中的去除动力学。与实验数据相比,AF中出水COD的动力学模型值被高估了。估计了AF中悬浮和附着生物量的综合增长率。在每个再循环比率下,整合的生物质的比生长速率分别为0.6213、0.6647和1.2083。 1 /天。随着再循环率的增加,比生长速率的增加对应于生物质脱落的增加。

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