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采用高比表面积合成介质填充的紧凑淹没式好氧固定膜(SAFF)反应器处理低浓度废水。

Treatment of low strength wastewater using compact submerged aerobic fixed film (SAFF) reactor filled with high specific surface area synthetic media.

机构信息

Department of Civil and Applied Mechanics, Shri. Govindram Seksaria Institute of Technology and Science, Indore 452003, India.

CSIR-National Environmental Engineering Research Institute (NEERI), Nehru Marg, Nagpur, 440 020, India E-mail:

出版信息

Water Sci Technol. 2019 Aug;80(4):737-746. doi: 10.2166/wst.2019.316.

Abstract

Studies on laboratory-scale submerged aerobic fixed film reactor (SAFF) packed with synthetic media having specific surface area of 165 m/m with a void volume of 89% were carried out to assess its performance under various organic loading rates (OLR) and hydraulic retention times (HRT). Synthetic wastewater having chemical oxygen demand (COD) and biochemical oxygen demand (BOD) of 400 ± 10% and 210 ± 10% mg/L respectively was fed and the reactor was subjected to OLRs ranging from 0.37 to 1.26 kg COD/m.d. It was observed that steady sloughing of biofilm occurs within the SAFF reactor all the times and average concentration of sloughed biomass in the effluent was 26 mg/L. The COD and BOD removal efficiencies varied between 85 and 89% and 86 to 94%, respectively. The kinetic studies demonstrated that SAFF reactor followed Stover-Kincannon and Grau models, with high correlation coefficients (R) of 0.9977 and 0.9916, respectively. Thus, the values of kinetic coefficients such as maximum substrate utilization rate, U = 64.1 g/(Ld); saturation value constant, K = 72.31 g/(L.d) and Grau second-order substrate removal rate constant, Ks = 2.44 day can be useful to develop and design large scale SAFF reactors. Finally, the study reveals that the optimum range for OLR can vary within 0.68-0.94 kg COD/m.d.

摘要

采用比表面积为 165 m/m、空隙率为 89%的合成介质,在实验室规模的浸没式好氧固定膜生物反应器(SAFF)中进行了研究,以评估其在不同有机负荷率(OLR)和水力停留时间(HRT)下的性能。采用化学需氧量(COD)和生化需氧量(BOD)分别为 400 ± 10%和 210 ± 10% mg/L 的合成废水进行进料,反应器的 OLR 范围为 0.37 至 1.26 kg COD/m.d。结果表明,SAFF 反应器内的生物膜始终稳定脱落,出水中脱落生物量的平均浓度为 26 mg/L。COD 和 BOD 的去除效率分别在 85%至 89%和 86%至 94%之间变化。动力学研究表明,SAFF 反应器遵循 Stover-Kincannon 和 Grau 模型,相关系数(R)分别高达 0.9977 和 0.9916。因此,最大基质利用速率 U = 64.1 g/(Ld)、饱和值常数 K = 72.31 g/(L.d)和 Grau 二级基质去除速率常数 Ks = 2.44 天等动力学系数的值可用于开发和设计大型 SAFF 反应器。最后,研究表明,OLR 的最佳范围可以在 0.68-0.94 kg COD/m.d 之间变化。

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