Coagulation combined with ultraviolet irradiation activated sodium percarbonate as pretreatment prior to ultrafiltration: Analysis of free radical oxidation mechanism and membrane fouling control

被引:29
作者
Chang, Xinqiang [1 ,2 ,3 ]
Lin, Tao [1 ,2 ]
Mo, Jiachen [1 ,2 ]
Xu, Hang [1 ,2 ]
Tao, Hui [1 ,2 ]
Liu, Wei [1 ,2 ]
机构
[1] Hohai Univ, Minist Educ, Key Lab Integrated Regulat & Resource Dev Shallow, Nanjing 210098, Peoples R China
[2] Hohai Univ, Coll Environm, Nanjing 210098, Peoples R China
[3] Southwest Forestry Univ, Coll Civil Engn, Kunming 650224, Yunnan, Peoples R China
基金
中国国家自然科学基金;
关键词
Drinking water; Coagulation; UV; Sodium percarbonate (UV; SPC); Natural organic matter; Ultrafiltration membrane fouling; NATURAL ORGANIC-MATTER; DRINKING-WATER SOURCES; NOM; DEGRADATION; REMOVAL;
D O I
10.1016/j.chemosphere.2021.132049
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Novel pre-coagulation-sedimentation integrated with ultraviolet activated sodium percarbonate (SPC) (Fe(III)-UV/SPC) processes are promising methods for ultrafiltration (UF) pretreatment to ensure the safety of rural drinking water and mitigate UF membrane fouling. The process of surface water purification using the integrated coagulation-advanced oxidation processes (AOPs)-UF system relies on the idea that pre-coagulation can remove hydrophobic macromolecular organic compounds, thus facilitating the oxidation of hydrophilic molecules or medium-sized macromolecules to improve the utilization efficiency of free radicals in AOPs. Compared with the UV/SPC process, the removal rates of UV254 and DOC in the Fe(III)-UV/SPC process (Fe(III) = 0.1 mM, SPC = 0.5 mM) were increased from 87.39 % to 41.45 %-93.56 % and 52.51 %, respectively. Furthermore, the dosage of SPC was reduced from 0.75 mM in UV/SPC process to 0.5 mM due to effects of pre-coagulation. The free radical quenching experiment showed that a significant radical sink of reactions with organic contaminants was formed by center dot OH and CO3 center dot- in the UV/SPC process, rather than a single specific radical. The destruction of the cake layer structure, reduction in contaminant concentration, and appearance of many permeable holes on the membrane surface were the main reasons for the alleviation of UF membrane fouling. Finally, the trans-membrane pressure and reversible membrane resistance decreased from 22.33 kPa to 3.68 x 1011 m- 1 to 18.28 kPa and 0.93 x 1011 m- 1, respectively. These results provide new insights into the behavior of membrane fouling control and offer technical references for the long-term stable operation of the UF process.
引用
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页数:11
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