Continuous electrochemical decomposition of dichloromethane in aqueous solution using various column electrodes

Abstract Dichloromethane is one of the chlorohydrocarbons that contaminate the soil and groundwater. They are conventionally removed from water by the aeration method and aeration/activated carbon adsorption. These methods only remove the compounds from water into other phases, and therefore require a secondary treatment for decomposition of the pollutants. The electrochemical method is an appropriate method for the decomposition of halocarbons in water. However, dichloromethane is one of the most persistent halocarbons for electrochemical treatment. In this paper, we optimized the conditions for electrochemical decomposition of dichloromethane in water and attempted to continuously treat the dichloromethane solution using a flow cell. During batch electrolysis, a Cu wire electrode showed high electrocatalytic activity for the decomposition of dichloromethane and the optimum potential for the decomposition was −1.3 V vs. Ag/AgCl. During flow electrolysis, the conversion of dichloromethane was largely dependent on the packing material of the column electrodes. A Cu metal-powder column electrode showed higher activity than a Cu particle-impregnated carbon fiber electrode and activated carbon electrode. The Cu metal-powder column electrode decomposed 20 ppm dichloromethane in an aqueous solution with 100% conversion at a low flow rate. This result suggests that the structure of the Cu surface affects the adsorption of dichloromethane on the Cu electrodes.

[1]  D. Spath,et al.  Photodegradation of dichloromethane, tetrachloroethylene and 1,2-dibromo-3- chloropropane in aqueous suspensions of TiO2 with natural, concentrated and simulated sunlight , 1992 .

[2]  Rosy Muftikian,et al.  A method for the rapid dechlorination of low molecular weight chlorinated hydrocarbons in water , 1995 .

[3]  R. Rosal,et al.  Hydrodechlorination of dichloromethane, trichloroethane, trichloroethylene and tetrachloroethylene over a sulfided Ni/Mo–γ-alumina catalyst , 1999 .

[4]  Chuh‐Yung Chen,et al.  CH2Cl2 decomposition by using a radio-frequency plasma system , 1996 .

[5]  N. Sonoyama,et al.  Electrochemical Hydrogenation of CFC-13 Using Metal-Supported Gas Diffusion Electrodes , 1998 .

[6]  N. Sonoyama,et al.  Electrochemical continuous decomposition of chloroform and other volatile chlorinated hydrocarbons in water using a column type metal impregnated carbon fiber electrode , 1999 .

[7]  N. Sonoyama,et al.  Electrochemical Decomposition of CFC-12 Using Gas Diffusion Electrodes , 1998 .

[8]  Makiko Kato,et al.  Electrochemical reduction of CO2 on single crystal electrodes of silver Ag(111), Ag(100) and Ag(110) , 1997 .

[9]  P. M. Woodhull,et al.  Remediation of dichloromethane (DCM) ‐contaminated ground water , 1992 .

[10]  N. Sonoyama,et al.  Reductive Electrochemical Decomposition of Chloroform on Metal Electrodes , 1997 .

[11]  Y. Hori,et al.  Catalytic Activity of CO2 Reduction on Pt Single-Crystal Electrodes: Pt(S)-[n(111)×(111)], Pt(S)-[n(111)×(100)], and Pt(S)-[n(100)×(111)] , 1997 .

[12]  K. Hara,et al.  Large Current Density CO2 Reduction under High Pressure Using Gas Diffusion Electrodes. , 1997 .

[13]  W. Flanagan Biodegradation of dichloromethane in a granular activated carbon fluidized‐bed reactor , 1998 .

[14]  D. L. Freedman,et al.  Dichloromethane biodegradation under nitrate‐reducing conditions , 1997 .

[15]  Akihiko Kudo,et al.  Electrochemical reduction of carbon dioxide under high pressure on various electrodes in an aqueous electrolyte , 1995 .

[16]  Ch. Lambrou,et al.  Electrochemical reduction of dichloromethane to higher hydrocarbons , 1998 .