Chemical Engineering Department, Universidad Autónoma de Madrid, Ctra. Colmenar Km 15, 28049, Madrid, Spain.
Environ Sci Pollut Res Int. 2024 Apr;31(20):29148-29161. doi: 10.1007/s11356-024-33065-8. Epub 2024 Apr 3.
The global occurrence of micropollutants in water bodies has raised concerns about potential negative effects on aquatic ecosystems and human health. EU regulations to mitigate such widespread pollution have already been implemented and are expected to become increasingly stringent in the next few years. Catalytic wet peroxide oxidation (CWPO) has proved to be a promising alternative for micropollutant removal from water, but most studies were performed in batch mode, often involving complex, expensive, and hardly recoverable catalysts, that are prone to deactivation. This work aims to demonstrate the feasibility of a fixed-bed reactor (FBR) packed with natural magnetite powder for the removal of a representative mixture of azole pesticides, recently listed in the EU Watch Lists. The performance of the system was evaluated by analyzing the impact of HO dose (3.6-13.4 mg L), magnetite load (2-8 g), inlet flow rate (0.25-1 mL min), and initial micropollutant concentration (100-1000 µg L) over 300 h of continuous operation. Azole pesticide conversion values above 80% were achieved under selected operating conditions (W = 8 g, [HO] = 6.7 mg L, flow rate = 0.5 mL min, pH = 5, T = 25 °C). Notably, the catalytic system showed a high stability upon 500 h in operation, with limited iron leaching (< 0.1 mg L). As a proof of concept, the feasibility of the system was confirmed using a real wastewater treatment plant (WWTP) effluent spiked with the mixture of azole pesticides. These results represent a clear advance for the application of CWPO as a tertiary treatment in WWTPs and open the door for the scale-up of FBR packed with natural magnetite.
水体中微污染物的全球性出现引起了人们对其对水生生态系统和人类健康产生潜在负面影响的关注。欧盟已经实施了减轻此类广泛污染的法规,预计在未来几年内将变得更加严格。催化湿式过氧化物氧化 (CWPO) 已被证明是从水中去除微污染物的一种很有前途的替代方法,但大多数研究都是在批处理模式下进行的,通常涉及复杂、昂贵且难以回收的催化剂,这些催化剂容易失活。本工作旨在展示用天然磁铁矿粉末填充的固定床反应器 (FBR) 去除最近被列入欧盟观察名单的唑类农药的代表性混合物的可行性。通过分析 HO 剂量(3.6-13.4 mg L)、磁铁矿负载(2-8 g)、入口流速(0.25-1 mL min)和初始微污染物浓度(100-1000 µg L)对 300 h 连续运行的影响来评估系统的性能。在选定的操作条件下(W = 8 g,[HO] = 6.7 mg L,流速 = 0.5 mL min,pH = 5,T = 25°C),唑类农药转化率超过 80%。值得注意的是,在 500 h 的运行过程中,催化系统表现出较高的稳定性,铁浸出量有限(< 0.1 mg L)。作为概念验证,使用添加了唑类农药混合物的实际污水处理厂 (WWTP) 出水证实了该系统的可行性。这些结果代表了 CWPO 作为 WWTP 三级处理的应用的明显进展,并为填充天然磁铁矿的 FBR 的放大铺平了道路。