Removal of micropollutants from water in a continuous-flow electrical discharge reactor

被引:65
|
作者
Wardenier, Niels [1 ,2 ]
Vanraes, Patrick [1 ,3 ]
Nikiforov, Anton [1 ]
Van Hulle, Stijn W. H. [2 ]
Leys, Christophe [1 ]
机构
[1] Univ Ghent, Dept Appl Phys, RUPT, Sint Pietersnieuwstr 41 B4, B-9000 Ghent, Belgium
[2] Univ Ghent, Dept Green Chem & Technol, LIWET, Graaf Karel Goedelaan 5, B-8500 Kortrijk, Belgium
[3] Univ Antwerp, PLASMANT, Dept Chem, Campus Drie Eiken,Univ Pl 1, B-2610 Antwerp, Belgium
关键词
Wastewater treatment; Advanced oxidation process; Non-thermal plasma; Micropollutants; Electrical energy per order; DIELECTRIC BARRIER DISCHARGE; PULSED CORONA DISCHARGE; ADVANCED OXIDATION PROCESSES; ATMOSPHERIC-PRESSURE PLASMA; WASTE-WATER; AQUEOUS-SOLUTIONS; ACTIVATED CARBON; INDUCED DEGRADATION; PRODUCT FORMATION; ATRAZINE;
D O I
10.1016/j.jhazmat.2018.08.095
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The emergence of micropollutants into our aquatic resources is regarded as an issue of increasing environmental concern. To protect the aquatic environment against further contamination with micropollutants, treatment with advanced oxidation processes (AOPs) is put forward as a promising technique. In this work, an innovative AOP based on electrical discharges in a continuous-flow pulsed dielectric barrier discharge (DBD) reactor with falling water film over activated carbon textile is examined for its potential application in water treatment. The effect of various operational parameters including feed gas type, gas flow rate, water flow rate and power on removal and energy efficiency has been studied. To this end, a synthetic micropollutant mixture containing five pesticides (atrazine, alachlor, diuron, dichlorvos and pentachlorophenol), two pharmaceuticals (carbamazepine and 1,7-alpha-ethinylestradiol), and 1 plasticizer (bisphenol A) is used. While working under optimal conditions, energy consumption was situated in the range 2.42-4.25 kW h/m(3), which is about two times lower than the economically viable energy cost of AOPs (5 kW h/m(3)). Hence, the application of non-thermal plasma could be regarded as a promising alternative AOP for (industrial) wastewater remediation.
引用
收藏
页码:238 / 245
页数:8
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