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商业纳滤膜去除水中的微量污染物。

Removal of micropollutants from water by commercially available nanofiltration membranes.

机构信息

Institute of Environmental and Chemical Engineering, Faculty of Chemical Technology, University of Pardubice, Studentská 573, 532 10 Pardubice, Czech Republic.

Institute of Environmental and Chemical Engineering, Faculty of Chemical Technology, University of Pardubice, Studentská 573, 532 10 Pardubice, Czech Republic.

出版信息

Sci Total Environ. 2020 Jun 10;720:137474. doi: 10.1016/j.scitotenv.2020.137474. Epub 2020 Feb 20.

Abstract

The current work is focused on the use of nanofiltration in the removal of micropollutants, specially drugs (diclofenac and ibuprofen) and heavy metal (zinc sulphate and zinc nitrate) from wastewater. The commercially available nanofiltration (NF) membranes (AFC 80, AFC 40, AFC 30) were characterised by demineralised water and the ability of the membranes to reject drugs and zinc(II) was subsequently examined. The influence of the operating conditions on the rejection and the permeate flux was evaluated. The operating conditions tested included the transmembrane pressure (5-30 bar); the effect of the feed concentration on the heavy metals rejection (50-200 mg L); the effect of ionic strength on the diclofenac and ibuprofen rejection (0-10 g L NaCl) and the volumetric flow rate (5-15 L min). It has been shown that increasing the transmembrane pressure increases the intensity of the permeate flow and rejection. Drugs rejection also increases with increasing bulk feed flow rates; however, decreases with increasing ionic strength (NaCl concentration in feed). Experimental data indicated that concentration polarisation existed in the membrane separation process. The stable permeation flux and high rejection of drugs and heavy metals indicated the potential of NF for the recovery of drugs and zinc(II) from wastewater.

摘要

目前的工作集中在纳滤去除废水中的污染物上,特别是药物(双氯芬酸和布洛芬)和重金属(硫酸锌和硝酸锌)。商业化的纳滤(NF)膜(AFC80、AFC40、AFC30)用去离子水进行了表征,并随后检查了这些膜对药物和锌(II)的截留能力。评估了操作条件对截留率和渗透通量的影响。测试的操作条件包括跨膜压力(5-30 巴);重金属截留率对进料浓度的影响(50-200 毫克/升);离子强度对双氯芬酸和布洛芬截留率的影响(0-10 克/升氯化钠)和体积流速(5-15 升/分钟)。结果表明,增加跨膜压力会增加渗透通量和截留率。随着进料体积流速的增加,药物截留率也增加;然而,随着离子强度(进料中氯化钠浓度)的增加而降低。实验数据表明,在膜分离过程中存在浓差极化。稳定的渗透通量和高药物和重金属截留率表明纳滤具有从废水中回收药物和锌(II)的潜力。

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