Electrochemical regeneration of activated carbon loaded with p-nitrophenol in a fluidized electrochemical reactor

Abstract This paper described a novel electrochemical process for the regeneration of activated carbon (AC) loaded with p-nitrophenol (PNP), aiming to reduce regeneration time and improve cost-effectiveness of the process by adoption of a novel non-active anode of modified lead dioxide and operation of AC in a fluidized mode. The regeneration parameters such as current density, liquid flow rate, NaCl concentration, pH of the solution and regeneration time were systematically investigated. Under the optimum conditions, the regeneration efficiency of AC could reach 90% in 1.5 h, and no significant declination was observed after five-times continuous adsorption–regeneration cycles, confirming the reuse feasibility of the regenerated AC. The adsorption of organic pollutants was confirmed occurring in the micropore of AC, and AC regeneration was mainly due to the decomposition of organics by the attack of active species such as hydroxyl radical that were generated by electrochemical oxidation. The time-space production for AC regeneration has been greatly improved in the present modified process, indicating this regeneration process is much more potentially cost-effective for application.

[1]  Dennis J. Miller,et al.  Activated carbon from cherry stones , 1994 .

[2]  M. Gattrell,et al.  The electrochemical oxidation of aqueous phenol at a glassy carbon electrode , 1990 .

[3]  A. Ramiro,et al.  Thermal regeneration of activated carbon saturated with p-nitrophenol , 2004 .

[4]  R. Dryfe,et al.  Electrochemical regeneration of a carbon-based adsorbent loaded with crystal violet dye , 2004 .

[5]  Huiping Zhang Regeneration of exhausted activated carbon by electrochemical method , 2002 .

[6]  A. Alif,et al.  Photochemistry and environment Part XIV. Phototransformation of nitrophenols induced by excitation of nitrite and nitrate ions , 1991 .

[7]  Jyeshtharaj B. Joshi,et al.  Regeneration of spent activated carbon by wet air oxidation , 1991 .

[8]  M. Sheintuch,et al.  Comparison of catalytic processes with other regeneration methods of activated carbon , 1999 .

[9]  Zucheng Wu,et al.  A novel fluidized electrochemical reactor for organic pollutant abatement , 2004 .

[10]  Zucheng Wu,et al.  ELECTROCATALYTIC DEGRADATION OF PHENOL IN ACIDIC AND SALINE WASTEWATER , 2002, Journal of Environmental Science and Health. Part A: Toxic/Hazardous Substances and Environmental Engineering.

[11]  Giacomo Cerisola,et al.  Electrochemical oxidation as a final treatment of synthetic tannery wastewater. , 2004, Environmental science & technology.

[12]  H. Wendt,et al.  Fundamentals of electrosorption on activated carbon for wastewater treatment of industrial effluents , 1998 .

[13]  Pablo Cañizares,et al.  Modeling of Wastewater Electro-oxidation Processes Part I. General Description and Application to Inactive Electrodes , 2004 .

[14]  P. Cañizares,et al.  Electrochemical Oxidation of Aqueous Phenol Wastes Using Active and Nonactive Electrodes , 2002 .

[15]  M. Sudoh,et al.  OXIDATIVE DEGRADATION OF AQUEOUS PHENOL EFFLUENT WITH ELECTROGENERATED FENTON''S REAGENT , 1986 .

[16]  S. Ferro,et al.  Anodic mineralization of organic substrates in chloride-containing aqueous media , 2000 .

[17]  R. Narbaitz,et al.  Electrochemical regeneration of granular activated carbon , 1994 .

[18]  A. Savall,et al.  Mechanistic Aspects of Phenol Electrochemical Degradation by Oxidation on a Ta / PbO2 Anode , 1998 .

[19]  J. Do,et al.  Kinetics of the Oxidative Degradation of Formaldehyde with Electrogenerated Hypochlorite Ion , 1997 .

[20]  H. Shen,et al.  Observation and analysis of the diluted water and red tide in the sea off the Changjiang River mouth in middle and late June 2003 , 2005 .

[21]  R. Kötz,et al.  Electrochemical waste water treatment using high overvoltage anodes. Part I: Physical and electrochemical properties of SnO2 anodes , 1991 .

[22]  P. Cañizares,et al.  Combined adsorption and electrochemical processes for the treatment of acidic aqueous phenol wastes , 2004 .

[23]  Ming-hua Zhou,et al.  Long life modified lead dioxide anode for organic wastewater treatment: electrochemical characteristics and degradation mechanism. , 2005, Environmental science & technology.

[24]  Zucheng Wu,et al.  Partial degradation of phenol by advanced electrochemical oxidation process. , 2001, Environmental science & technology.

[25]  V. Montiel,et al.  Influence of chloride ion on electrochemical degradation of phenol in alkaline medium using bismuth doped and pure PbO2 anodes. , 2001, Water research.