Reduction of trihalomethane precursors of dissolved organic matter in the secondary effluent by advanced treatment processes

被引:30
|
作者
Wei, Liang-Liang [1 ]
Zhao, Qing-Liang [1 ,2 ]
Xue, Shuang [1 ,3 ]
Chang, Chein-Chi [4 ,5 ]
Tang, Feng [6 ]
Liang, Guan-Liang [1 ]
Jia, Ting [1 ]
机构
[1] Harbin Inst Technol, Sch Municipal & Environm Engn, Harbin 150090, Peoples R China
[2] HIT, SKLUWRE, Harbin 150090, Peoples R China
[3] Liaoning Univ, Sch Environm Sci, Shenyang 110036, Peoples R China
[4] Dist Columbia Water & Sewer Author, Washington, DC 20032 USA
[5] Univ Maryland, Dept Civil & Environm Engn, Baltimore, MD 21250 USA
[6] Guangzhou Devot Thermal Facil Co, Guangzhou 510760, Guangdong, Peoples R China
关键词
Advanced treatments; Dissolved organic matter; Fractionation; Trihalomethane formation potential; Specific trihalomethane formation potential; SOIL-AQUIFER TREATMENT; SUBSURFACE WETLAND TREATMENT; PREPARATIVE ISOLATION; ACTIVATED CARBON; REVERSE-OSMOSIS; NATURAL-WATERS; REMOVAL; TRANSFORMATION; FATE; DOC;
D O I
10.1016/j.jhazmat.2009.04.045
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Wastewater effluent collected from the Wenchang Wastewater Treatment Plant (Harbin, China) was used as source water for advanced treatment and reclamation. Since dissolved organic matter (DOM) in the secondary effluent contains a high concentration of trihalomethanes (THMs) precursors, several processes of advanced treatments including granular activated carbon (GAC) adsorption, sand column biodegradation, horizontal subsurface flow wetland (HSFW) treatment, laboratory-scale soil aquifer treatment (SAT) and GAC + SAT were used in this study to compare and differentiate the removal mechanisms of DOM. DOM in the secondary effluent and the treated effluents was fractionated into five classes using XAD resins: hydrophobic acid (HPO-A), hydrophobic neutral (HPO-N), transphilic acid (TPI-A), transphilic neutral (TPI-N), and hydrophilic fraction (HPI). Results showed that HPO-A and HPI were two main fractions of the DOM in the secondary effluent, accounting for 30.0% and 45.5% of the bulk DOM, respectively. HPO-A exhibited higher trihalomethane formation potential (THMFP) and specific THMFP (STHMFP) than HPI during the chlorination process. The order of the dissolved organic carbon (DOC) removal with respect to different advanced treatments was observed to be GAC + SAT > SAT > GAC > sand column > HSFW. As for the DOM removal mechanisms, the advanced treatment processes of GAC adsorption, SAT and GAC + SAT tended to adsorb more HPO-A, HPO-N and TPI-A and could reduce the aromaticity of those DOM fractions efficiently. Correspondingly, the advanced treatment processes of sand column, SAT, HSFW and GAC + SAT removed more HPI and TPI-N through biodegradation and each of the DOM fractions had an increased aromaticity. The removal order of the THMs precursor by the advanced treatment processes was GAC + SAT > GAC > SAT > sand column > HSFW. The adsorption reduced the STHMFP of the DOM fractions effectively, whereas the biodegradation mechanism of the treatments (sand column, SAT, GAC + SAT and HSFW) showed a converse trend. Moreover, the THMFP and STHMFP of the DOM in the HSFW effluent were obviously affected by the DOM derived from the leaves and roots. (c) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:1012 / 1021
页数:10
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