Commercial‐scale removal of short‐chain PFAS in a batch‐wise adsorptive bubble separation process by dosing with cationic co‐surfactant

IF 3 Q3 ENGINEERING, ENVIRONMENTAL
Paul Stevenson, Stoyan I. Karakashev
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Abstract

Abstract Studies performed by Burns et al. in 2021 and 2022 demonstrated that a three‐stage batch‐wise adsorptive bubble separation process, surface active foam fractionation (SAFF), is effective at removing most per‐ and polyfluoroalkyl substances (PFASs) from contaminated groundwaters and landfill leachates. However, PFAS species with very low adsorption coefficients to bubble surfaces are difficult to remove, which is parallel to the difficulties in removing short‐chain PFAS in granulated activated carbon beds and other solid media. It is well known that the adsorption coefficient to bubble surfaces improves in the presence of electrolytes in solution and it has previously been shown that this improves the removal of PFAS. By developing a correlation for the removal percentage of one species or another of PFAS due to SAFF in commercial‐scale processes as a function of the adsorption coefficient, it is possible to generally estimate the removal percentage of any PFAS. The addition of a cationic co‐surfactant, cetrimonium bromide, to the feed can significantly further improve the adsorption coefficient and, as a consequence, materially improve the removal of short‐chain PFAS due to SAFF. A method for estimating this improved performance is in qualitative agreement with plant trials of SAFF at a North American site with a history of groundwater contamination due to the use of aqueous film forming foams firefighting foams, but the precise improvements appear to be dependent upon the concentration of the added co‐surfactant. The required concentration of co‐surfactant is significantly larger than might be expected on charge equivalence considerations, and this may be due to its consumption by other species in the feed, including PFAS that have not been accounted for. It is noted that the SAFF process may not be true foam fractionation and may, instead, be a bubble fractionator, both of which can be collectively described by the term “adsorptive bubble separation processes.”
通过添加阳离子表面活性剂在间歇气泡吸附分离过程中去除短链PFAS的商业规模
Burns等人在2021年和2022年进行的研究表明,三阶段间歇式吸附气泡分离工艺,即表面活性泡沫分馏(SAFF),可以有效地从受污染的地下水和垃圾填埋场渗滤液中去除大多数单氟烷基和多氟烷基物质(PFASs)。然而,气泡表面吸附系数非常低的PFAS难以去除,这与在颗粒状活性炭床和其他固体介质中去除短链PFAS的困难相似。众所周知,在溶液中存在电解质时,气泡表面的吸附系数会提高,并且先前已经证明这可以提高PFAS的去除。通过建立商业规模工艺中由于SAFF导致的一种或另一种PFAS的去除率与吸附系数的关系,可以大致估计任何PFAS的去除率。在进料中加入一种阳离子表面活性剂——西曲溴铵,可以进一步显著提高吸附系数,从而大大提高由于SAFF引起的短链PFAS的去除效果。估计这种改进性能的方法与SAFF在北美的工厂试验在定性上是一致的,该工厂的地下水污染历史是由于使用水膜形成泡沫灭火泡沫造成的,但精确的改进似乎取决于添加的共表面活性剂的浓度。根据电荷等效的考虑,所需的共表面活性剂浓度比预期的要大得多,这可能是由于饲料中其他物种的消耗,包括未考虑到的PFAS。值得注意的是,SAFF过程可能不是真正的泡沫分馏,而可能是一个气泡分馏器,这两者都可以用术语“吸附气泡分离过程”来描述。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
3.50
自引率
21.10%
发文量
37
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