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铁氮共掺杂活性炭混合基质膜的制备及其水处理性能

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传统膜分离过程存在选择性与渗透性的矛盾问题,无法有效去除尺寸小于膜孔的污染物。将铁氮共掺杂活性炭(FeNCs)填充入聚偏二氟乙烯(PVDF)基质中制得一种具有过硫酸氢盐(PMS)活化能力的混合基质膜(FeNCs@PVDF)。通过扫描电子显微镜、能谱分析、X射线衍射、拉曼等表征来测试膜的物理化学特性。以苯酚为目标污染物,考察了FeNCs@PVDF在PMS活化辅助下的水处理性能。结果表明,FeNCs@PVDF耦合PMS活化可以有效去除苯酚,且FeNCs填充度越高越有利于提高催化膜性能。FeNCs填充度为50%的FeNCs@PVDF对苯酚的去除率分别为单独PMS氧化以及单独膜分离的4。8和3。6倍。FeNCs@PVDF催化膜在较宽的pH范围(3~12)内均保持高性能。
Preparation of Fe and N co-doped activated carbon mixed matrix membranes for water treatment
The traditional membrane separation process suffers from the contradiction between membrane selectivity and permeability,which is hard to remove pollutants smaller than membrane pores.Fe and N co-doped activated carbons(FeNCs)were filled into poly(vinylidene fluoride)(PVDF)matrix to obtain mixed matrix membranes(FeNCs@PVDF)with peroxymonosulfate(PMS)activation ability.The physical and chemical properties of membranes were tested by scanning electron microscopy,energy dispersive spectroscopy,X ray diffraction and Raman spectroscopy.Employing phenol as the target pollutant,the water treatment performance of FeNCs@PVDF under PMS activation assistance was evaluated.Results showed the FeNCs@PVDF integrated with PMS activation exhibited effective phenol removal,and its performance was improved with increased filling of FeNCs.The phenol removal by FeNCs@PVDF with 50%FeNCs was 4.8 and 3.6 times higher than that of PMS oxidation alone and membrane filtration alone,respectively.The FeNCs@PVDF can maintain high performance in a wide pH range of 3-12.

Fe and N co-doped activated carbonmixed matrix membraneperoxymonosulfate activation

谭昕阳、王冠龙、张秀芳

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大连工业大学 轻工与化学工程学院,辽宁 大连 116034

铁氮共掺杂活性炭 混合基质膜 过硫酸氢盐活化

国家自然科学基金项目辽宁省教育厅高校基本科研项目

21906013LJKQZ2021116

2024

大连工业大学学报
大连工业大学

大连工业大学学报

影响因子:0.295
ISSN:1674-1404
年,卷(期):2024.43(1)
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