Smith Sanne J, Lewis Jeffrey, Wiberg Karin, Wall Erik, Ahrens Lutz
Department of Aquatic Sciences and Assessment, Swedish University of Agricultural Sciences (SLU), P.O. Box 7050, SE-750 07 Uppsala, Sweden.
ECT2, Lärlingsgatan 14b, SE-90422 Umeå, Sweden.
Sci Total Environ. 2023 May 1;871:162050. doi: 10.1016/j.scitotenv.2023.162050. Epub 2023 Feb 7.
Foam fractionation has recently attracted attention as a low-cost and environmentally benign treatment technology for water contaminated with per- and polyfluoroalkyl substances (PFAS). However, data on the mass balance over the foam fractionation process are scarce and when available, gaps in the mass balance are often identified. This study verified the high treatment efficiency of a pilot-scale foam fractionation system for removal of PFAS from industrial water contaminated with aqueous film-forming foam. ΣPFAS removal reached up to 84 % and the removal of perfluorooctane sulfonic acid (PFOS) up to 97 %, but the short-chain perfluorobutanoic acid (PFBA) was only removed with a mean efficiency of 1.5 %. In general, mobile short-chain PFAS were removed less efficiently when the perfluorocarbon chain length was below six for carboxylic acids and below five for sulfonic acids. Fluctuations in treatment efficiency due to natural variations in the chemistry of the influent water were minor, confirming the robustness of the technology, but significant positive correlations between PFAS removal and influent metal concentration and conductivity were observed. Over all experiments, the mass balance closure did not differ significantly from 100 %. Nonetheless, PFAS sorption to the walls of the reactor was measured, as well as high PFAS emissions by the air exiting the reactor. PFAS emissions in aerosols correlated positively with mass balance closure. The elevated aerial PFAS concentrations measured in the experimental facility have implications for worker safety and prevention of PFAS-emissions to the atmosphere, and demonstrate the importance of installing appropriate filters on the air outlet of foam fractionation systems.
泡沫分离法最近作为一种低成本且环境友好的处理技术受到关注,用于处理受全氟和多氟烷基物质(PFAS)污染的水。然而,关于泡沫分离过程中质量平衡的数据很少,即便有数据,也常常能发现质量平衡存在缺口。本研究验证了中试规模泡沫分离系统从受水成膜泡沫污染的工业水中去除PFAS的高效性。ΣPFAS去除率高达84%,全氟辛烷磺酸(PFOS)去除率高达97%,但短链全氟丁酸(PFBA)的去除平均效率仅为1.5%。一般来说,当羧酸的全氟碳链长度低于6且磺酸的全氟碳链长度低于5时,可移动短链PFAS的去除效率较低。进水化学性质的自然变化导致的处理效率波动较小,证实了该技术的稳健性,但观察到PFAS去除与进水金属浓度和电导率之间存在显著正相关。在所有实验中,质量平衡闭合与100%无显著差异。尽管如此,仍测量到PFAS吸附在反应器壁上,以及从反应器排出的空气中存在高PFAS排放。气溶胶中的PFAS排放与质量平衡闭合呈正相关。在实验设施中测得的空气中PFAS浓度升高对工人安全和防止PFAS排放到大气有影响,并证明了在泡沫分离系统的出气口安装合适过滤器的重要性。