Institute of Resource and Environment, Beijing Academy of Science and Technology, Beijing, China; School of Resources and Environmental Engineering, Shanghai Polytechnic University, Shanghai, China.
Institute of Resource and Environment, Beijing Academy of Science and Technology, Beijing, China; Beijing Key Lab of Industrial Land Contamination and Remediation, Beijing, China.
J Environ Manage. 2023 Jan 1;325(Pt B):116407. doi: 10.1016/j.jenvman.2022.116407. Epub 2022 Oct 24.
The proportion of activated persulfate (PS) oxidation technology in the remediation of domestic organic contaminated sites has increased every year, and the potential corrosion risk of site reuse caused by residual oxidants and by-products has also attracted the attention of researchers. In this work, the potential corrosion degree such as the mass reduction rate and surface crack width of standard iron flakes under different conditions, including with different PS dosages and release times, was monitored quantitatively over a long period, and the corresponding corrosion risk was quantitatively assessed. The results showed that when n (NaSO):n (PAHs) increased from 5:1 to 100:1, the higher the oxidizer dosage, the more severe the corrosion weight loss and surface crack width, indicating that the oxidizer dosage was positively correlated with the potential corrosion risk. In addition, the corrosion crack width of the standard iron flake had a significant positive correlation with the reaction time and a significant negative correlation with the mass change. According to the changes in the standard iron flake, the corrosion process could be divided into three stages, in which the corrosion risk from high to low followed the order of oxidant corrosion stage > oxidant and salt corrosion stage > salt and microbial corrosion stage. Therefore, the dosage of chemicals should be controlled, the molar ratio of oxidizer to contaminant should not exceed 25:1, and a natural recovery period of at least one year should be left post remediation. During the reuse of the remediation sites in the future, the potential corrosion risks should also be calculated based on the dosage and time, to avoid redevelopment and use of the restoration site in the high corrosion risk stage.
过硫酸盐活化氧化技术在国内有机污染场地修复中的比例逐年增加,而残留氧化剂和副产物对场地再利用造成的潜在腐蚀风险也引起了研究人员的关注。本工作定量监测了不同条件下(包括不同 PS 剂量和释放时间)标准铁片的质量减少率和表面裂纹宽度等潜在腐蚀程度,并对相应的腐蚀风险进行了定量评估。结果表明,当 n(NaSO):n(PAHs)从 5:1 增加到 100:1 时,氧化剂剂量越高,腐蚀失重和表面裂纹宽度越大,表明氧化剂剂量与潜在腐蚀风险呈正相关。此外,标准铁片的腐蚀裂纹宽度与反应时间呈显著正相关,与质量变化呈显著负相关。根据标准铁片的变化,可以将腐蚀过程分为三个阶段,其中从高到低的腐蚀风险顺序为氧化剂腐蚀阶段>氧化剂和盐腐蚀阶段>盐和微生物腐蚀阶段。因此,应控制化学品的用量,氧化剂与污染物的摩尔比不应超过 25:1,并在修复后至少留出一年的自然恢复期。在未来修复场地的再利用过程中,还应根据剂量和时间计算潜在的腐蚀风险,以避免在高腐蚀风险阶段重新开发和使用修复场地。