Electrochemical degradation of polycyclic aromatic hydrocarbons in creosote solution using ruthenium oxide on titanium expanded mesh anode

被引:91
作者
Tran, Lan-Huong [1 ]
Drogui, Patrick [1 ]
Mercier, Guy [1 ]
Blais, Jean-Francois [1 ]
机构
[1] Univ Quebec, Inst Natl Rech Sci, Ctr Eau Terre & Environm, Quebec City, PQ G1K 9A9, Canada
关键词
Creosote; Polycyclic aromatic hydrocarbon; Electro-oxidation; Electrochemical degradation; Ruthenium oxide electrode; WASTE-WATER TREATMENT; ORGANIC POLLUTANTS; CONTAMINATED SEDIMENTS; ADVANCED OXIDATION; REMOVAL; PHENOL; SLUDGE; BIOREMEDIATION; DETOXIFICATION; PHENANTHRENE;
D O I
10.1016/j.jhazmat.2008.09.012
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, expanded titanium (Ti) covered with ruthenium oxide (RuO2) electrode was used to anodically oxidize polycyclic aromatic hydrocarbons (PAH) in creosote solution. Synthetic creosote-oily solution (COS) was prepared with distilled water and a commercial creosote solution in the presence of an amphoteric surfactant; Cocamidopropylhydroxysultaine (CAS). Electrolysis was carried out using a parallelepipedic electrolytic 1.5-L cell containing five anodes (Ti/RuO2) and five cathodes (stainless steel, 316L) alternated in the electrode pack. The effects of initial pH, temperature, retention time, supporting electrolyte, current density and initial PAH concentration on the process performance were examined. Experimental results revealed that a current density of 9.23 mA cm(-2) was beneficial for PAH oxidation. The sum of PAH concentrations for 16 PAHs could be optimally diminished up to 80-82% while imposing a residence time in the electrolysis cell of 90 min. There was not a significant effect of the electrolyte (Na2SO4) concentration on oxidation efficiency in the investigated range of 500-4000 mg/L However, an addition of 500 mg Na2SO4 L-1 was required to reduce the energy consumption and the treatment cost. Besides, there was no effect of initial PAH concentration on oxidation efficiency in the investigated range of 270-540 mg PAH L-1. Alkaline media was not favourable for PAH oxidation, whereas high performance of PAH degradation could be recorded without initial pH adjustment (original pH around 6.0). Likewise, under optimal conditions, 84% of petroleum hydrocarbon (C-10-C-50) was removed, whereas removal yields of 69% and 62% have been measured for O&G and COD, respectively. Microtox and Daphnia biotests showed that electrochemical oxidation using Ti/RuO2 could be efficiently used to reduce more than 90% of the COS toxicity. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:1118 / 1129
页数:12
相关论文
共 49 条
[1]   Combined treatment of PAHs contaminated soils using the sequence extraction with surfactant-electrochemical degradation [J].
Alcantara, M. T. ;
Gomez, J. ;
Pazos, M. ;
Sanroman, M. A. .
CHEMOSPHERE, 2008, 70 (08) :1438-1444
[2]   Electrochemical remediation of phenanthrene from contaminated kaolinite [J].
Alcantara, T. ;
Pazos, M. ;
Cameselle, C. ;
Sanroman, M. A. .
ENVIRONMENTAL GEOCHEMISTRY AND HEALTH, 2008, 30 (02) :89-94
[3]  
[Anonymous], 1999, Standard Methods for Examination of Water and Waste Water
[4]   Leaching behaviour of wood treated with creosote [J].
Becker, L ;
Matuschek, G ;
Lenoir, D ;
Kettrup, A .
CHEMOSPHERE, 2001, 42 (03) :301-308
[5]   Fenton reagent advanced oxidation of polynuclear aromatic hydrocarbons in water [J].
Beltran, FJ ;
Gonzalez, M ;
Rivas, FJ ;
Alvarez, P .
WATER AIR AND SOIL POLLUTION, 1998, 105 (3-4) :685-700
[6]  
BETTS WD, 1990, P INT TAR C PAR FRAN
[7]   Anodic oxidation of Orange II on Ti/BDD electrode: Variable effects [J].
Chen, XM ;
Chen, GH .
SEPARATION AND PURIFICATION TECHNOLOGY, 2006, 48 (01) :45-49
[8]  
COMNINELLIS C, 1993, J APPL ELECTROCHEM, V23, P108
[9]  
COMNINELLIS C, 1992, PROCESS SAF ENVIRON, V70, P219
[10]   ELECTROCATALYSIS IN THE ELECTROCHEMICAL CONVERSION/COMBUSTION OF ORGANIC POLLUTANTS FOR WASTE-WATER TREATMENT [J].
COMNINELLIS, C .
ELECTROCHIMICA ACTA, 1994, 39 (11-12) :1857-1862