Enhanced degradation of organic contaminants by thermally activated peroxymonosulfate in the presence of chloride ion

被引:23
|
作者
Qin, Yuyang [1 ]
Li, Hongjing [1 ]
Ma, Jun [2 ]
机构
[1] Fudan Univ, Dept Environm Sci & Engn, Shanghai 200433, Peoples R China
[2] Harbin Inst Technol, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
基金
中国国家自然科学基金;
关键词
Thermally activated peroxymonosulfate; Chlorine ion; Organic contaminants; Reactive species; Chlorinated by-products; ADVANCED OXIDATION PROCESSES; SITU CHEMICAL OXIDATION; ACID ORANGE 7; BISPHENOL-A; PERSULFATE OXIDATION; PHENOLIC-COMPOUNDS; HYDROXYL RADICALS; PULSE-RADIOLYSIS; RATE CONSTANTS; WATER;
D O I
10.1016/j.cej.2022.138814
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The effect of chloride ion (Cl-) on the degradation of organic contaminants (OCs) by thermally activated peroxymonosulfate (TAP) was assessed in this study. P-aminobenzoic acid (PABA), sulfadiazine (SDZ), bisphenol A (BPA), and chloramphenicol (CAP) were employed as model OCs with different structure. The degradation efficiencies of PABA, SDZ, BPA, and CAP were respectively 76.4 %, 90.8 %, 10.1 %, and 14.5 % by TAP (70 degrees C) after 60 mM treatment, further raised to 97.6 %, 97.4 %, 55.2 %, and 30.5 % in the presence of Cl- (1 mM). When Cl- concentration increased to 10 mM, PABA and SDZ were completely degraded respectively after 7 min and 10 min, 97.1 % of BPA and 59.5 % of CAP were removed within 60 mM. In TAP system, PABA and SDZ were primarily degraded by direct peroxymonosulfate (PMS) oxidation, while BPA and CAP were mostly removed by hydroxyl radical and sulfate radical oxidation. In Cl-/TAP mixtures, the degradation of PABA and BPA was mainly attributed to hypochlorous acid oxidation, SDZ was chiefly removed via direct PMS oxidation, and CAP was principally oxidized by radicals. Furthermore, the intermediate products of OCs degradation during Cl-/TAP oxidation were identified, and primary degradation pathways were proposed. The removal efficiencies of total organic carbon were markedly improved from 19.3 % to 25.3 % by TAP to 52.6 %-69.0 % in Cl-/TAP system. The concentrations of typical chlorinated by-products after OCs oxidation were 17.2 mu g/L-86.3 mu g/L in Cl-/TAP system. Considering the complexity of actual wastewater, 51.3 %-100 % removal efficiencies of OCs by TAP oxidation were achieved in Cl--containing secondary effluent. Understanding the role of Cl(- )in OCs degradation is essential for the practical application of Cl-/TAP oxidation in advanced wastewater treatment.
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页数:10
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