Ozonation combined with electrolysis of 1,4-dioxane using a two-compartment electrolytic flow cell with solid electrolyte

被引:59
作者
Kishimoto, Naoyuki [1 ]
Nakagawa, Takahiro [1 ]
Asano, Masamichi [2 ]
Abe, Makoto [3 ]
Yamada, Masato [3 ]
Ono, Yoshiro [4 ]
机构
[1] Ryukoku Univ, Fac Sci & Technol, Otsu, Shiga 5202194, Japan
[2] Mitsubishi Heavy Ind Co Ltd, Yokohama Res & Dev Ctr, Yokohama, Kanagawa 2368515, Japan
[3] Natl Inst Environm Studies, Res Ctr Mat Cycles & Waste Management, Tsukuba, Ibaraki 3058506, Japan
[4] Okayama Univ, Grad Sch Environm Sci, Okayama 7008530, Japan
关键词
ozonation; electrochemical treatment; advanced oxidation technology; hydroxyl radical; 1,4-dioxane; reverse osmosis; landfill leachate;
D O I
10.1016/j.watres.2007.07.029
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ozonation combined with electrolysis (ozone-electrolysis) is a new advanced oxidation process for water treatment. The advantages of ozone-electrolysis are (1) that reagents such as hydrogen peroxide or ferrous salts are unnecessary, (2) there is less influence from chromaticity, and (3) electric power is only required for operation. However, electrolysis has a serious limitation, in that it requires electrical conductivity (EC). This research is aimed at developing an ozone-electrolysis reactor that is applicable to wastewater with low EC using a cation exchange membrane as solid electrolyte. Moreover, experimental evidence of hydroxyl radical (. OH) generation via the cathodic reduction of ozone was obtained. Competitive kinetics analysis, based on the experimental data from the ozone-electrolysis of a mixed solution of 1,4-dioxane and tert-butyl alcohol, revealed that OH contributed to 1,4-dioxane degradation. The ozone-electrolysis reactor was successfully applicable to degradation of 1,4-dioxane in both 1,4-dioxane solution (EC: less than 0.30 mu S/cm) and a landfill leachate treated by a low-pressure reverse osmosis membrane (EC: 0.06mS/cm). The use of a solid electrolyte was also very effective in reducing the electric power required for electrolysis. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:379 / 385
页数:7
相关论文
共 32 条
[1]   Distribution of 1,4-dioxane in relation to possible sources in the water environment [J].
Abe, A .
SCIENCE OF THE TOTAL ENVIRONMENT, 1999, 227 (01) :41-47
[2]   OXIDATION AND BIODEGRADABILITY ENHANCEMENT OF 1,4-DIOXANE USING HYDROGEN-PEROXIDE AND OZONE [J].
ADAMS, CD ;
SCANLAN, PA ;
SECRIST, ND .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (11) :1812-1818
[3]   Advanced oxidation processes (AOP) for water purification and recovery [J].
Andreozzi, R ;
Caprio, V ;
Insola, A ;
Marotta, R .
CATALYSIS TODAY, 1999, 53 (01) :51-59
[4]  
Baker R.W., 2004, Membrane Technology and Applications, V2nd, DOI DOI 10.1002/0470020393
[5]   Enhanced sonochemical decomposition of 1,4-dioxane by ferrous iron [J].
Beckett, MA ;
Hua, I .
WATER RESEARCH, 2003, 37 (10) :2372-2376
[6]  
CLESCERI LS, 1998, STANDARD METHOD EXAM
[7]   Boron removal from landfill leachate by means of nanofiltration and reverse osmosis [J].
Dydo, P ;
Turek, M ;
Ciba, J ;
Trojanowska, J ;
Kluczka, J .
DESALINATION, 2005, 185 (1-3) :131-137
[8]  
GLAZE WH, 1987, OZONE-SCI ENG, V9, P335
[9]   KINETICS OF OZONE DECOMPOSITION - A DYNAMIC APPROACH [J].
GUROL, MD ;
SINGER, PC .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1982, 16 (07) :377-383
[10]   RATE CONSTANTS OF REACTIONS OF OZONE WITH ORGANIC AND INORGANIC-COMPOUNDS IN WATER .1. NON-DISSOCIATING ORGANIC-COMPOUNDS [J].
HOIGNE, J ;
BADER, H .
WATER RESEARCH, 1983, 17 (02) :173-183