Department of Chemical and Biomolecular Engineering, University of Cantabria, Av. de Los Castros s/n, 39005 Santander, Spain.
Department of Chemical and Biomolecular Engineering, University of Cantabria, Av. de Los Castros s/n, 39005 Santander, Spain.
Water Res. 2017 Apr 1;112:147-156. doi: 10.1016/j.watres.2017.01.043. Epub 2017 Jan 25.
The present study was aimed at the development of a strategy for removing and degrading perfluorohexanoic acid (PFHxA) from industrial process waters at concentrations in the range 60-200 mg L. The treatment train consisted of nanofiltration (NF) separation followed by electrochemical degradation of the NF concentrate. Using a laboratory-scale system and working in the total recirculation mode, the DowFilm NF270 membrane provided PFHxA rejections that varied in the range 96.6-99.4% as the operating pressure was increased from 2.5 to 20 bar. The NF operation in concentration mode enabled a volume reduction factor of 5 and increased the PFHxA concentration in the retentate to 870 mg L. Results showed that the increase in PFHxA concentration and the presence of calcium sulfate salts did not induce irreversible membrane fouling. The NF retentate was treated in a commercial undivided electrochemical cell provided with two parallel flow-by compartments separated by bipolar boron doped diamond (BDD) electrode, BDD counter anode, and counter cathode. Current densities ranging from 20 to 100 A m were examined. The electrochemical degradation rate of PFHxA reached 98% and was accompanied by its efficient mineralization, as the reduction of total organic carbon was higher than 95%. Energy consumption, which was 15.2 kWh m of treated NF concentrate, was minimized by selecting operation at 50 A m. While most of the previous research on the treatment of perfluoroalkyl substances (PFASs) focused on the removal of perfluorooctanoic acid (PFOA) and perfluorooctane sulfonate (PFOS), these compounds have been phased out by chemical manufacturers. Our findings are relevant for the treatment of PFHxA, which appears to be one of the present alternatives to long-chain PFASs thanks to its lower bioaccumulative potential than PFOA and PFOS. However, PFHxA also behaves as a persistent pollutant. Moreover, our results highlight the potential of combining membrane separation and electrochemical oxidation for the efficient treatment of PFAS-impacted waters.
本研究旨在开发一种策略,从浓度为 60-200mg/L 的工业工艺水中去除和降解全氟己酸(PFHxA)。处理链由纳滤(NF)分离和 NF 浓缩物的电化学降解组成。使用实验室规模的系统并在全循环模式下工作,DowFilm NF270 膜提供的 PFHxA 截留率在操作压力从 2.5 增加到 20bar 时变化范围为 96.6-99.4%。NF 浓缩模式下的操作可实现 5 倍的体积减少因子,并将截留物中 PFHxA 的浓度增加到 870mg/L。结果表明,PFHxA 浓度的增加和硫酸钙盐的存在并没有引起不可逆的膜污染。NF 浓缩物在带有两个平行流动室的商业不分隔电化学电池中进行处理,两个流动室由双极掺硼金刚石(BDD)电极、BDD 对电极和对阴极隔开。考察了 20-100A/m 的电流密度。PFHxA 的电化学降解率达到 98%,同时伴随着高效的矿化,因为总有机碳的减少率高于 95%。通过选择在 50A/m 下操作,将处理的 NF 浓缩物的能耗降至 15.2kWh/m。虽然之前关于全氟烷基物质(PFASs)处理的大部分研究都集中在去除全氟辛酸(PFOA)和全氟辛烷磺酸(PFOS)上,但这些化合物已被化学制造商逐步淘汰。我们的发现与 PFHxA 的处理有关,由于其生物蓄积潜力低于 PFOA 和 PFOS,PFHxA 似乎是长链 PFASs 的替代品之一。然而,PFHxA 也表现为一种持久性污染物。此外,我们的结果强调了膜分离和电化学氧化相结合用于有效处理受 PFAS 影响的水的潜力。