Key Laboratory of Membrane Separation of Shaanxi Province, Key Laboratory of Northwest Water Resources, Key Laboratory of Environmental Engineering of Shaanxi Province, Xi'an University of Architecture and Technology, Yan Ta Road No. 13, Xi'an 710055, China; Research Institute of Membrane Separation Technology of Shaanxi Province, Xi'an University of Architecture and Technology, Yan Ta Road No. 13, Xi'an 710055, China.
Key Laboratory of Membrane Separation of Shaanxi Province, Key Laboratory of Northwest Water Resources, Key Laboratory of Environmental Engineering of Shaanxi Province, Xi'an University of Architecture and Technology, Yan Ta Road No. 13, Xi'an 710055, China.
Water Res. 2024 Jul 1;258:121752. doi: 10.1016/j.watres.2024.121752. Epub 2024 May 8.
The homogeneous Fenton process involves both coagulation and oxidation, but it requires added acidity, so it is rarely used to control membrane fouling. This work found that the pH of neutral simulated wastewater sharply declined to 4.1 after pre-treatment with 0.1 mM Fenton reagent (Fe:HO=1:1) without added acidity. This occurred mainly because the trace homogeneous Fenton reagent induced in situ acid production by organic matter in the wastewater, which supplied the acidic conditions required for the Fenton reaction and ensured that the reaction could proceed continuously. Then, oxidation during the pre-Fenton process enhanced the electrostatic repulsion forces and effectively weakened the hydrogen bonds of organic matter at the membrane surface by altering the net charge and hydroxyl content of organic matter, while coagulation caused the foulants to gather and form large aggregates. These changes diminished the deposition of foulants onto the membrane surface and resulted in a looser fouling layer, which eventually caused the membrane fouling rate to decline from 83 % to 24 % and the flux recovery rate to increase from 44 % to 98 % during 2 h of filtration. This membrane fouling mitigation ability is much superior to that of pre-HO, pre-Fe or pre-Fe processes with equivalent doses.
均相 Fenton 工艺同时涉及混凝和氧化,但需要额外添加酸,因此很少用于控制膜污染。本工作发现,在中性模拟废水中添加 0.1mM Fenton 试剂(Fe:H2O2=1:1)预处理后,无需额外添加酸,废水的 pH 值就会急剧下降至 4.1。这主要是因为痕量均相 Fenton 试剂诱导废水中有机物原位产酸,提供 Fenton 反应所需的酸性条件,并确保反应能持续进行。然后,预 Fenton 过程中的氧化作用通过改变有机物的净电荷和羟基含量,增强静电斥力,有效削弱有机物在膜表面的氢键,同时混凝作用使污染物聚集并形成大的聚集体。这些变化减少了污染物在膜表面的沉积,导致过滤 2 小时后,膜污染速率从 83%降低至 24%,通量恢复率从 44%提高至 98%。这种膜污染缓解能力远优于同等剂量的预 HO、预 Fe 或预 Fe 工艺。