Department of Bioenvironmental Systems Engineering, National Taiwan University, No. 1, Sec. 4, Roosevelt Rd, Da-An District, Taipei, 106, Taiwan.
Formosa Chemicals and Fiber Corporation, No. 359, Sec. 3, Zhongshan Rd, Changhua County, 500, Taiwan.
Water Res. 2017 Sep 15;121:329-337. doi: 10.1016/j.watres.2017.05.050. Epub 2017 May 29.
The present study aimed to derive an analytical formula to quantify the diffusion of organic contaminant in a biofilm. The experiments were conducted to investigate the BOD degradation under the conditions of influent COD concentration from 50 to 300 mg/L, COD:N:P ratios of 100:5:1 and 100:15:3, with and without auxiliary aeration. The BOD removal rate was around 73% for non-aerated influent COD of 50 mg/L with 1-h hydraulic retention time. The BOD removal rate increased as the influent loading and hydraulic retention time increased while the influent COD was no more than 150 mg/L. Without aeration, the removal rate dropped significantly when influent COD increased to the range no less than 200 mg/L, due to the fact that the BOD diffusive flux driven by the biomass uptake was not further enhanced by higher ambient organic loading. The diffusion coefficient was calculated to be 1.12 × 10 m/d with influent COD of 50 mg/L at COD:N:P ratio of 100:5:1 and 1 h hydraulic retention time and aeration, and the coefficient increased to 3.35 × 10 m/d as the influent COD concentration increased to 300 mg/L. The diffusion coefficient decreased to 4.09 × 10 m/d as the retention time increased to 3 h. The overall diffusion coefficients showed an increasing trend as the influent organic loading increased. The difference in diffusion coefficients between 1 and 2 h was apparently greater than that between 2 and 3 h, indicating a smaller overall diffusive flux due to a longer retention time. Further analysis revealed that BOD diffusion activity exhibited a declining trend as the wastewater travelled through the system. An analytical diffusion-reaction model was developed to characterize the diffusion behaviour, and applied to estimating the treatment efficiency for real domestic sewage. The result showed that the estimated effluent BOD concentrations were quite comparable to those from experimental measurements.
本研究旨在推导一个分析公式,以量化生物膜中有机污染物的扩散。实验在进水 COD 浓度为 50 至 300mg/L、COD:N:P 比为 100:5:1 和 100:15:3、有或没有辅助曝气的条件下进行,以研究 BOD 降解情况。无曝气时,水力停留时间为 1 小时,进水 COD 为 50mg/L 时,BOD 去除率约为 73%。当进水负荷和水力停留时间增加,而进水 COD 不超过 150mg/L 时,BOD 去除率会增加。在没有曝气的情况下,当进水 COD 增加到不低于 200mg/L 时,去除率会显著下降,这是因为生物量摄取所驱动的 BOD 扩散通量不会因更高的环境有机负荷而进一步增强。在 COD:N:P 比为 100:5:1 和水力停留时间为 1 小时且曝气的条件下,进水 COD 为 50mg/L 时,扩散系数计算为 1.12×10−5m/d,当进水 COD 增加到 300mg/L 时,扩散系数增加到 3.35×10−5m/d。当停留时间增加到 3 小时时,扩散系数降至 4.09×10−5m/d。随着进水有机负荷的增加,总的扩散系数呈上升趋势。1 小时和 2 小时之间的扩散系数差异明显大于 2 小时和 3 小时之间的差异,这表明由于停留时间较长,总的扩散通量较小。进一步分析表明,BOD 扩散活性随着废水在系统中的流动而呈现下降趋势。建立了一个分析扩散-反应模型来描述扩散行为,并将其应用于估计实际生活污水的处理效率。结果表明,估算的出水 BOD 浓度与实验测量值非常接近。