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超滤和复合微滤生物催化膜在环境相关浓度下的活性及类固醇激素微污染物降解

Ultrafiltration and composite microfiltration biocatalytic membrane activity and steroid hormone micropollutant degradation at environmentally relevant concentrations.

作者信息

Imbrogno Alessandra, Schmidt Martin, Schulze Agnes, Moreira María Teresa, Schäfer Andrea I

机构信息

Institute for Advanced Membrane Technology (IAMT), Karlsruhe Institute of Technology (KIT), Hermann-von-Helmholtz-Platz 1, 76344 Eggenstein-Leopoldshafen, Germany.

Leibniz Institute of Surface Engineering (IOM), Leipzig, Germany.

出版信息

Water Res. 2025 Mar 15;272:122902. doi: 10.1016/j.watres.2024.122902. Epub 2024 Dec 2.

Abstract

Biocatalytic degradation of micropollutants has been extensively explored in both batch and membrane reactors in µg/L to mg/L concentrations and variable water compositions. The degradation of micropollutants by biocatalytic membranes at environmentally relevant concentrations of ng/L range found in natural surface water matrices has not yet been investigated, presumably because of the challenging concentration analysis. This study investigated the limitations of biocatalytic degradation of estradiol (E2) micropollutant at environmentally relevant concentrations by a biocatalytic membrane. The contributions of solute flux, hydraulic residence time (HRT) and water matrix composition on reaction kinetics, the apparent rate of disappearance (or reaction rate) and enzyme activity were examined. Two biocatalytic membranes were used: i) laccase entrapped in an ultrafiltration (UF) membrane support (namely UF-SNPs) and, ii) laccase covalently bound to the nanofiber matrix of a composite microfiltration (MF) membrane. The three main findings are reported. Firstly, the apparent rate of E2 disappearance decreases significantly by four orders of magnitude at a low micropollutant concentration of 0.1 µg/L, resulting in undetectable degradation during filtration, irrespective of the biocatalytic membrane. Secondly, the solute mass transfer and HRT control the biocatalytic degradation through the membranes resulting in different E2 removal. For the UF-SNPs membrane, a removal of 31 % is achieved only by increasing the concentration to 3000 µg/L and at a flux of 60 L/m².h (HRT of 4.5 s) due to an increase in solute flux by an order of magnitude similar to the apparent rate of disappearance. In contrast, the nano-MF membrane is ineffective in achieving biocatalytic degradation regardless of E2 concentration, as the HRT is approximately seven times lower (0.6 s) than that of the UF-SNPs, and thus insufficient for E2 to reach the catalytic site. Thirdly, the composition of the aqueous matrix plays a crucial role in the control of laccase activity irrespective of the membrane. Indeed, laccase is inactivated predominantly by chloride ions in synthetic carbonate buffer, since the typical NaCl concentration is about two orders of magnitude higher than E2 concentration. This study highlights that the slower kinetics achieved in the biocatalytic UF-SNPs and MF membranes are ineffective in removing steroid hormone micropollutants at realistic concentrations in surface water matrices. Further research is suggested to accelerate the reaction kinetics at such low concentrations and prolong the residence time within the membrane.

摘要

在微克/升至毫克/升浓度范围以及不同水质组成的条件下,微污染物的生物催化降解已在间歇式反应器和膜反应器中得到广泛研究。然而,对于生物催化膜在天然地表水基质中纳克/升浓度范围内环境相关浓度下对微污染物的降解,尚未进行研究,推测这是由于浓度分析具有挑战性。本研究调查了生物催化膜在环境相关浓度下对雌二醇(E2)微污染物进行生物催化降解的局限性。研究了溶质通量、水力停留时间(HRT)和水基质组成对反应动力学、表观消失速率(或反应速率)和酶活性的影响。使用了两种生物催化膜:i)固定在超滤(UF)膜载体中的漆酶(即UF-SNPs),以及ii)共价结合到复合微滤(MF)膜纳米纤维基质上的漆酶。报告了三个主要发现。首先,在0.1微克/升的低微污染物浓度下,E2的表观消失速率显著降低四个数量级,导致在过滤过程中无法检测到降解,无论使用哪种生物催化膜。其次,溶质传质和HRT通过膜控制生物催化降解,从而导致不同的E2去除率。对于UF-SNPs膜,仅通过将浓度提高到3000微克/升并在通量为60升/平方米·小时(HRT为4.5秒)的条件下,由于溶质通量增加了一个与表观消失速率相似的数量级,实现了31%的去除率。相比之下,纳米MF膜无论E2浓度如何,都无法有效实现生物催化降解,因为其HRT比UF-SNPs低约七倍(0.6秒),因此不足以使E2到达催化位点。第三,无论使用何种膜,水基质的组成在控制漆酶活性方面都起着关键作用。实际上,在合成碳酸盐缓冲液中,漆酶主要被氯离子灭活,因为典型的NaCl浓度比E2浓度高约两个数量级。本研究强调,生物催化UF-SNPs和MF膜中实现的较慢动力学在去除地表水基质中实际浓度的类固醇激素微污染物方面是无效的。建议进一步研究以加速如此低浓度下的反应动力学并延长膜内的停留时间。

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