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在一个大规模的厌氧/缺氧/好氧工艺与膜生物反应器相结合的城市污水再生系统中,选定的微有机污染物的去除和归宿。

Elimination and fate of selected micro-organic pollutants in a full-scale anaerobic/anoxic/aerobic process combined with membrane bioreactor for municipal wastewater reclamation.

机构信息

State Key Joint Laboratory of Environmental Simulation and Pollution Control, Department of Environmental Science and Engineering, Tsinghua University, Beijing 100084, China.

出版信息

Water Res. 2010 Dec;44(20):5999-6010. doi: 10.1016/j.watres.2010.07.052. Epub 2010 Jul 27.

Abstract

The occurrence and elimination of 19 micro-organic pollutants including endocrine disrupting chemicals (EDCs) and pharmaceuticals and personal care products (PPCPs) in a full-scale anaerobic/anoxic/aerobic-membrane bioreactor process was investigated. The investigated process achieved over 70% removal of the target EDCs and 50%-100% removal of most of the PPCPs, with influent concentration ranging from ng/L to μg/L. Three PPCPs, carbamazepine, diclofenac and sulpiride were not well removed, with the removal efficiency below 20%. A rough mass balance suggests that the targets were eliminated through sludge-adsorption and/or biodegradation, the former of which was particularly significant for the removal of hydrophobic compounds. The two-phase fate model was employed to describe the kinetics of sludge-adsorption and biodegradation. It was found that the fast sludge adsorption (indicated by mass-transfer rates greater than 10 for most compounds) is responsible for the rapid decline of the aqueous concentration of the targets in the first compartment of the treatment process (i.e. in the anaerobic tank). In contrast, the slow biodegradation proved to be the rate-determining step for the entire degradation process, and the rates are generally positively related to the dissolved oxygen level. On the other hand, this study showed that the removal rates of most targets can reach a quasi-plateau in 5 h under aerobic conditions, indicating that hydraulic retention time of ca. 5 h in aerobic tanks should be sufficient for the elimination of most targets.

摘要

本研究考察了全规模厌氧/缺氧/好氧-膜生物反应器工艺中 19 种微污染物(包括内分泌干扰物(EDCs)和药品及个人护理产品(PPCPs))的产生和消除情况。所研究的工艺对目标 EDCs 的去除率超过 70%,对大多数 PPCPs 的去除率为 50%-100%,进水浓度范围为 ng/L 至 μg/L。三种 PPCPs(卡马西平、双氯芬酸和舒必利)的去除效果不佳,去除效率低于 20%。粗略的质量平衡表明,这些目标是通过污泥吸附和/或生物降解去除的,前者对疏水性化合物的去除特别重要。采用两相分配模型描述了污泥吸附和生物降解动力学。结果表明,快速的污泥吸附(对于大多数化合物,传质速率大于 10)是处理过程第一阶段(即厌氧池)中目标物水溶液浓度迅速下降的原因。相比之下,缓慢的生物降解被证明是整个降解过程的限速步骤,且速率通常与溶解氧水平呈正相关。另一方面,本研究表明,在好氧条件下,大多数目标物的去除率在 5 小时内可达到准稳定状态,表明好氧池的水力停留时间约为 5 小时应足以消除大多数目标物。

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