Effect of different catalysts on the decomposition of VOCs using flow-type plasma-driven catalysis

This paper presents the effect of different catalysts on the decomposition of benzene and toluene using flow-type plasma-driven catalyst (PDC) system. Three representative materials of titanium dioxide, two types of gamma-alumina and two zeolites were tested. Several types of metal catalysts (Ag, Ni, Pt, Pd) and their loading amount were also investigated for the optimization of the PDC system. Three key factors of energy consumption, carbon balance and safety of products were emphasized in evaluating the performance of different catalysts. The type of catalysts greatly influenced on the carbon balance, CO<sub>2</sub> selectivity, ozone formation, while no much difference was observed in the degree of enhancement in energy efficiency. Pt/gamma-Al<sub>2</sub>O<sub>3</sub> catalyst was found to be effective in enhancing the CO<sub>2</sub> selectivity. The CO<sub>2 </sub> selectivity increased as Ag-loading amount on TiO<sub>2</sub> catalyst increased. The 4.0 wt% Ag/TiO<sub>2</sub> catalyst was effective in suppressing the formation of NO<sub>2</sub> and N<sub>2 </sub>O. Zeolites showed comparable decomposition efficiency and good carbon balance, while the CO<sub>2</sub> selectivity was poor compared to the other catalysts. Mechanical mixing of 2.0 wt% Ag/H-Y zeolite with Pt/gamma-Al<sub>2</sub>O<sub>3</sub> was effective in enhancing the CO <sub>2</sub> selectivity without changing other performance

[1]  Eric M. Gaigneaux,et al.  Plasma-assisted catalysis for volatile organic compounds abatement , 2005 .

[2]  Atsushi Ogata,et al.  Decomposition of Gas-Phase Benzene Using Plasma – Driven Catalyst Reactor: Complete Oxidation of Adsorbed Benzene Using Oxygen Plasma , 2005 .

[3]  Atsushi Ogata,et al.  Atmospheric plasma-driven catalysis for the low temperature decomposition of dilute aromatic compounds , 2005 .

[4]  Seung M. Oh,et al.  Decomposition of gas-phase benzene using plasma-driven catalyst (PDC) reactor packed with Ag/TiO2 catalyst , 2005 .

[5]  J. Röpcke,et al.  On NOx production and volatile organic compound removal in a pulsed microwave discharge in air , 2005 .

[6]  S. Futamura,et al.  Comparative assessment of different nonthermal plasma reactors on energy efficiency and aerosol formation from the decomposition of gas-phase benzene , 2005, IEEE Transactions on Industry Applications.

[7]  Dong-Wha Park,et al.  Effect of zeolite in surface discharge plasma on the decomposition of toluene , 2005 .

[8]  Shigeru Futamura,et al.  Catalytic oxidation of benzene with ozone over alumina-supported manganese oxides , 2004 .

[9]  Kui Zhang,et al.  A mechanism for the destruction of CFC-12 in a nonthermal, atmospheric pressure plasma , 2004 .

[10]  Hyun-Ha Kim,et al.  Nonthermal Plasma Processing for Air‐Pollution Control: A Historical Review, Current Issues, and Future Prospects , 2004 .

[11]  D. Mehandjiev,et al.  Metallurgical slag as a support of catalysts for complete oxidation in the presence of ozone , 2004 .

[12]  Seung M. Oh,et al.  Decomposition of Benzene Using Ag/TiO2 Packed Plasma-Driven Catalyst Reactor: Influence of Electrode Configuration and Ag-Loading Amount , 2004 .

[13]  G. Rim,et al.  Effect of nonthermal plasma reactor for CF/sub 4/ decomposition , 2003 .

[14]  Atsushi Ogata,et al.  Effective combination of nonthermal plasma and catalysts for decomposition of benzene in air , 2003 .

[15]  K. Mizuno,et al.  Mechanism of the dissociation of chlorofluorocarbons during nonthermal plasma processing in nitrogen at atmospheric pressure , 2003 .

[16]  Z. Zakrzewski,et al.  Abatement of perfluorinated compounds using microwave plasmas at atmospheric pressure , 2003 .

[17]  K. Sakamoto,et al.  Degradation of toluene with an ozone-decomposition catalyst in the presence of ozone, and the combined effect of TiO2 addition , 2003 .

[18]  D. Chang,et al.  Microwave Plasma Conversion of Volatile Organic Compounds , 2003, Journal of the Air & Waste Management Association.

[19]  Tetsuji Oda,et al.  Non-thermal plasma processing for environmental protection: decomposition of dilute VOCs in air , 2003 .

[20]  M. Cha,et al.  Synergetic Effects of Non-thermal Plasma and Catalysts on VOCs Decomposition , 2003 .

[21]  G. Rim,et al.  EFFECT OF NON-THERMAL PLASMA REACTOR FOR CF DECOMPOSITION , 2003 .

[22]  M. Šimek,et al.  Efficiency of ozone production by pulsed positive corona discharge in synthetic air , 2002 .

[23]  Frank Holzer,et al.  Improved oxidation of air pollutants in a non-thermal plasma , 2002 .

[24]  V. Sokolov,et al.  Kinetics of destruction of diisopropyl methylphosphonate in corona discharge , 2002 .

[25]  S. Kushiyama,et al.  Decomposition of Benzene in Air in a Plasma Reactor: Effect of Reactor Type and Operating Conditions , 2001, Conference Record of the 2001 IEEE Industry Applications Conference. 36th IAS Annual Meeting (Cat. No.01CH37248).

[26]  R. McAdams,et al.  Prospects for non-thermal atmospheric plasmas for pollution abatement , 2001 .

[27]  Shigeru Futamura,et al.  Performance evaluation of a hybrid system comprising silent discharge plasma and manganese oxide catalysts for benzene decomposition , 2001 .

[28]  M. Chang,et al.  Gas-Phase Removal of Acetaldehyde via Packed-Bed Dielectric Barrier Discharge Reactor , 2001 .

[29]  H. Sekiguchi Catalysis assisted plasma decomposition of benzene using dielectric barrier discharge , 2001 .

[30]  Y. Wu,et al.  Reaction Mechanisms in Both a CCl2F2/O2/Ar and a CCl2F2/H2/Ar RF Plasma Environment , 2000 .

[31]  K. Francke,et al.  Cleaning of Air Streams from Organic Pollutants by Plasma–Catalytic Oxidation , 2000 .

[32]  V. Mathur,et al.  Nitrogen Oxide Decomposition by Barrier Discharge , 2000 .

[33]  B. Penetrante,et al.  Environmental applications of low-temperature plasmas , 1999 .

[34]  Atsushi Ogata,et al.  Removal of dilute benzene using zeolite-hybrid plasma reactor , 1999, Conference Record of the 1999 IEEE Industry Applications Conference. Thirty-Forth IAS Annual Meeting (Cat. No.99CH36370).

[35]  K. Takaki,et al.  Removal of nitric oxide in flue gases by multi-point to plane dielectric barrier discharge , 1999 .

[36]  Toshiaki Yamamoto,et al.  Aerosol generation and decomposition of CFC-113 by the ferroelectric plasma reactor , 1999 .

[37]  T. Yamamoto Optimization of non-thermal plasma for the treatment of gas streams. , 1999, Journal of hazardous materials.

[38]  Toshikazu Ohkubo,et al.  Evaluation of NOx Removal by Corona Induced Non-Thermal Plasmas , 1998 .

[39]  Y. Wu,et al.  Decomposition of methyl chloride by using an RF plasma reactor , 1998 .

[40]  W. Hoffelner,et al.  Reduction of & SO2 and destruction of VOCs & PCDD/F in industrial flue gas by electrical discharge , 1998 .

[41]  R. Korzekwa,et al.  Advanced Oxidation and Reduction Processes in the Gas Phase Using Non-Thermal Plasmas , 1998 .

[42]  T. Yamamoto,et al.  The dependence of nonthermal plasma behavior of VOCs on their chemical structures , 1997 .

[43]  B. Penetrante,et al.  Identification of mechanisms for decomposition of air pollutants by non-thermal plasma processing , 1997 .

[44]  S. Barlow,et al.  Destruction of carbon tetrachloride in a dielectric barrier/packed‐bed corona reactor , 1996 .

[45]  P. H. Wallman,et al.  Pulsed corona and dielectric‐barrier discharge processing of NO in N2 , 1996 .

[46]  Moo Been Chang,et al.  GAS-PHASE REMOVAL OF H2S AND NH3 WITH DIELECTRIC BARRIER DISCHARGES , 1996 .

[47]  Jen-Shih Chang,et al.  NO/sub x/ removal by a pipe with nozzle-plate electrode corona discharge system , 1994 .

[48]  Jen-Shih Chang,et al.  NOx Removal by a Pipe with Nozzle-Plate , 1994 .

[49]  S. Masuda,et al.  The performance of an integrated air purifier for control of aerosol, microbial, and odor , 1993 .

[50]  G. H. Ramsey,et al.  Corona destruction: an innovative control technology for VOCs and air toxics. , 1993, Air & waste : journal of the Air & Waste Management Association.

[51]  J. A. Dorsey,et al.  Ozone production in electrostatic air cleaners with contaminated electrodes , 1992, Conference Record of the 1992 IEEE Industry Applications Society Annual Meeting.

[52]  S. Masuda,et al.  Decomposition of fluorocarbon gaseous contaminants by surface discharge induced plasma chemical processing , 1991, Conference Record of the 1991 IEEE Industry Applications Society Annual Meeting.

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

[54]  K. Okazaki,et al.  Effect of voltage waveform on partial discharge in ferroelectric pellet layer for gas cleaning , 1990, Conference Record of the 1990 IEEE Industry Applications Society Annual Meeting.

[55]  G. Dinelli,et al.  Pulse power electrostatic technologies for the control of flue gas emissions , 1990 .

[56]  Senichi Masuda,et al.  Control of NO/sub x/ by positive and negative pulsed corona discharges , 1990 .

[57]  S. Masuda,et al.  Control of NOx by positive and negative pulsed corona discharges , 1990 .

[58]  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,.

[59]  S. Masuda,et al.  A Ceramic-Based Ozonizer Using High Frequency Discharge , 1985, 1985 Annual Meeting Industry Applications Society.

[60]  G. Pietsch,et al.  Behaviour of NOx in air-fed ozonizers , 1988 .

[61]  S. Masuda Pulse corona induced plasma chemical process: a horizon of new plasma chemical technologies , 1988 .

[62]  Akira Mizuno,et al.  A Method for the Removal of Sulfur Dioxide from Exhaust Gas Utilizing Pulsed Streamer Corona for Electron Energization , 1986, IEEE Transactions on Industry Applications.

[63]  L. Bailin,et al.  Development of microwave plasma detoxification process for hazardous wastes. Part I , 1978 .