Non-thermal plasma for air and water remediation.

A modular typed dielectric barrier discharge (DBD) device is designed and tested for air and water remediation. The module is made of a number of DBD tubes that can be arranged in series or parallel. Each of the DBD tubes comprises inner electrode enclosed with dielectric barrier and arranged as such to provide a gap for the passage of gases. Non-thermal plasma generated in the gap effectively creates gaseous chemical reactions. Its efficacy in the remediation of gas stream containing high NOx, similar to diesel emission and wastewater containing latex, are presented. A six tubes DBD module has successfully removed more than 80% of nitric oxide from the gas stream. In another arrangement, oxygen was fed into a two tubes DBD to generate ozone for treatment of wastewater. Samples of wastewater were collected from a treatment pond of a rubber vulcanization pilot plant. The water pollution load was evaluated by the chemical oxygen demand (COD) and biological oxygen demand (BOD5) values. Preliminary results showed some improvement (about 13%) on the COD after treatment and at the same time had increased the BOD5 by 42%. This results in higher BOD5/COD ratio after ozonation which indicate better biodegradability of the wastewater.

[1]  H. Shimelis,et al.  Genetic analysis among selected vernonia lines through seed oil content, fatty acids and RAPD DNA markers , 2010 .

[2]  Michael Hirth,et al.  Ozone synthesis from oxygen in dielectric barrier discharges , 1987 .

[3]  G. Samudro,et al.  REVIEW ON BOD, COD AND BOD/COD RATIO: A TRIANGLE ZONE FOR TOXIC, BIODEGRADABLE AND STABLE LEVELS , 2010 .

[4]  S. Dhali,et al.  Dielectric‐barrier discharge for processing of SO2/NOx , 1991 .

[5]  S. Mohapatro,et al.  Dielectric barrier discharge cascaded with red mud waste to enhance NOx removal from diesel engine exhaust , 2012, IEEE Transactions on Dielectrics and Electrical Insulation.

[6]  A. Adoki,et al.  Testing biological methods to treat rubber effluent , 2008 .

[7]  이화영 X , 1960, Chinese Plants Names Index 2000-2009.

[8]  Siglas de Palabras a D. g. , 2013 .

[9]  Mike Bradford,et al.  Controlling NOx emissions. Part 1 , 2002 .

[10]  D. J. Waters,et al.  Gas-phase reactions of hydroxyl radicals with alkyl nitrite vapours in H2O2+ NO2+ CO mixtures , 1982 .

[11]  M. Cleary,et al.  Environment and Development in the Straits of Malacca , 2000 .

[12]  M. Kushner,et al.  Removal of SO2 from gas streams using a dielectric barrier discharge and combined plasma photolysis , 1991 .

[13]  Charles Baukal,et al.  Industrial Combustion Pollution and Control , 2003 .

[14]  B.M. Penetrante,et al.  Pollution control applications of pulsed power technology , 1993, Ninth IEEE International Pulsed Power Conference.

[15]  Mohd Ali Hassan,et al.  Treatment of wastewater from rubber industry in Malaysia , 2010 .

[16]  M. Kushner,et al.  Reaction chemistry and optimization of plasma remediation of NxOy from gas streams , 1995 .

[17]  T. E. Chua,et al.  Waste management in the coastal areas of the ASEAN region: roles of governments, banking institutions, donor agencies, private sector and communities , 1992 .

[18]  K. Cen,et al.  Simultaneous oxidation of NO, SO2 and Hg0 from flue gas by pulsed corona discharge. , 2009, Journal of environmental sciences.

[19]  J. Rivera-Utrilla,et al.  Effectiveness of different oxidizing agents for removing sodium dodecylbenzenesulphonate in aqueous systems. , 2009, Water research.

[20]  T. Hvitved-Jacobsen,et al.  Biodegradability of wastewater--a method for COD-fractionation. , 2002, Water science and technology : a journal of the International Association on Water Pollution Research.

[21]  G. G. Stokes "J." , 1890, The New Yale Book of Quotations.

[22]  G. H. Ramsey,et al.  Control of volatile organic compounds by an AC energized ferroelectric pellet reactor and a pulsed corona reactor , 1989, Conference Record of the IEEE Industry Applications Society Annual Meeting,.

[23]  J. Norman Bardsley,et al.  Kinetic Analysis of Non-Thermal Plasmas Used for Pollution Control , 1997 .

[24]  A. Mahvi,et al.  Efficiency of Ozonation and Chemical Coagulation Using Aluminum Sulfate and Ferric Chloride for Reduction of COD from Wastewater of Rubber Industry , 2015 .

[25]  B. Penetrante,et al.  Non-Thermal Plasma Techniques for Pollution Control , 1993 .

[26]  M. Neiger,et al.  The influence of ethene on the conversion of in a dielectric barrier discharge , 1998 .

[27]  S. Masuda,et al.  Destruction of gaseous pollutants by surface induced plasma chemical process-SPCP , 1991, Conference Record of the 1991 IEEE Industry Applications Society Annual Meeting.

[28]  U. Kogelschatz Dielectric-Barrier Discharges: Their History, Discharge Physics, and Industrial Applications , 2003 .

[29]  M. Kushner,et al.  Removal of SO2 and the simultaneous removal of SO2 and NO from simulated flue gas streams using dielectric barrier discharge plasmas , 1992 .

[30]  Sayed R Qasim Wastewater Treatment Plants: Planning, Design and Operation , 1986 .

[31]  Hongmin Yang,et al.  Simultaneous removal of NO and SO2 from dry gas stream using non-thermal plasma. , 2007, Journal of environmental sciences.

[32]  Aik Heng Lee,et al.  BOD:COD Ratio as an Indicator for Pollutants Leaching from Landfill , 2014 .