Quantitative monitoring and potential mechanism of the secondary corrosion risk of PAH-contaminated soil remediated by persulfate oxidation

被引:6
|
作者
Wang, Zhenxia [1 ,2 ]
Song, Jiuhao [1 ,3 ]
Yuan, Wenyi [2 ]
Li, Yi [1 ,3 ]
Wu, Naijin [1 ,3 ]
Li, Xiang [1 ,3 ]
Rong, Liming [1 ,3 ]
Wang, Haijian [1 ,3 ]
Zhang, Ji [1 ,3 ]
Wei, Wenxia [1 ,3 ]
Li, Peizhong [1 ,3 ]
机构
[1] Beijing Acad Sci & Technol, Inst Resource & Environm, Beijing, Peoples R China
[2] Shanghai Polytech Univ, Sch Resources & Environm Engn, Shanghai, Peoples R China
[3] Beijing Key Lab Ind Land Contaminat & Remediat, Beijing, Peoples R China
基金
中国国家自然科学基金;
关键词
Soil; Chemical oxidation; Persulfate; Corrosion risk; Contaminated site remediation; PIPELINE STEEL; CARBON-STEEL; DEGRADATION; CONCRETE; REMOVAL;
D O I
10.1016/j.jenvman.2022.116407
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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 (Na2S2O8):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.
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页数:9
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