Department of Chemical Engineering, The University of Melbourne, Building 165, Chemical Engineering 1, Parkville VIC 3010, Australia; Australian Laboratory for Emerging Contaminants, School of Chemistry, The University of Melbourne, Victoria 3010, Australia.
Department of Chemical Engineering, The University of Melbourne, Building 165, Chemical Engineering 1, Parkville VIC 3010, Australia.
Water Res. 2024 Nov 15;266:122397. doi: 10.1016/j.watres.2024.122397. Epub 2024 Sep 16.
The concept of incorporating foam fractionation in aerated bioreactors at wastewater treatment plants (WWTPs) for the removal of per- and polyfluoroalkyl substances (PFAS) has recently been proposed. The extent of PFAS enrichment in aerated bioreactors' foams, as indicated by enrichment factors (EFs), has been observed to vary widely. Laboratory evidence has shown that factors affecting PFAS enrichment in foams include conductivity, surfactant concentrations and initial PFAS concentrations. However, real wastewaters are complex heterogenous matrices with physical, chemical and biological characteristics potentially contributing to the phenomenon of PFAS partitioning into foams. In this study, we characterised mixed liquor suspensions, including conductivity, filament content, aqueous PFAS concentrations, surface tension and total suspended solids concentrations (TSS) as well as foams, including bubble size and half-life. We used statistical tools - linear mixed-effects model - to establish relationships between PFAS enrichment in aerated bioreactor foams and the examined characteristics. We found that some of the examined characteristics, specifically filament content, surface tension and TSS concentrations measured in mixed liquor suspension and foam half-life, are negatively and significantly associated with the enrichment of longer chain PFAS (with perfluorinated carbon number ≥ 6). Of these, filament content is the important determinant of PFAS enrichment, potentially leading to an increase in, for example, perfluorooctanoic acid (PFOA) EF from 3 to 100 between typical filamentous and non-filamentous suspended biomass. However, enrichment of shorter chain PFAS (with perfluorinated carbon number ≤ 5) is negligible and is not affected by the characteristics that were measured. The findings of our study may serve as valuable information for the implementation of foam fractionation at WWTPs by elucidating the drivers that contribute to the enrichment of longer chain PFAS, under conditions typically found at WWTPs.
将泡沫浮选纳入污水处理厂(WWTP)充气生物反应器中以去除全氟和多氟烷基物质(PFAS)的概念最近被提出。充气生物反应器泡沫中 PFAS 的富集程度(通过富集因子 (EF) 表示)差异很大。实验室证据表明,影响 PFAS 在泡沫中富集的因素包括电导率、表面活性剂浓度和初始 PFAS 浓度。然而,实际废水是复杂的多相基质,具有物理、化学和生物特性,可能导致 PFAS 分配到泡沫中的现象。在这项研究中,我们对混合液悬浮液进行了表征,包括电导率、丝状内容物、水溶液中的 PFAS 浓度、表面张力和总悬浮固体浓度(TSS),以及泡沫,包括气泡大小和半衰期。我们使用统计工具——线性混合效应模型——来建立充气生物反应器泡沫中 PFAS 富集与所检查特性之间的关系。我们发现,一些被检查的特性,特别是丝状内容物、表面张力和混合液悬浮液中的 TSS 浓度以及泡沫半衰期,与长链 PFAS(全氟碳数≥6)的富集呈负相关且具有统计学意义。在这些特性中,丝状内容物是 PFAS 富集的重要决定因素,可能会导致例如,在典型的丝状和非丝状悬浮生物量之间,全氟辛酸 (PFOA) 的 EF 从 3 增加到 100。然而,短链 PFAS(全氟碳数≤5)的富集可以忽略不计,并且不受所测量特性的影响。我们研究的结果可以为 WWTP 中泡沫分离的实施提供有价值的信息,阐明了在 WWTP 中通常存在的条件下导致长链 PFAS 富集的驱动因素。