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Received August 30, 2006
Accepted November 1, 2006
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Effective combination of non-thermal plasma and catalyst for removal of volatile organic compounds and NOx
Korea Institute of Energy Research, Daejeon 305-343, Korea
sgjeon@kier.re.kr
Korean Journal of Chemical Engineering, May 2007, 24(3), 522-526(5), 10.1007/s11814-007-0092-9
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Abstract
A plasma/catalyst hybrid reactor was designed to overcome the limits of plasma and catalyst technologies. A two-plasma/catalyst hybrid system was used to decompose VOCs (toluene) and NOx at temperature lower than 150 ℃. The single-stage type (Plasma-driven catalyst process) is the system in which catalysts are installed in a nonthermal plasma reactor. And the two-stage type (Plasma-enhanced process) is the system in which a plasma and a catalyst reactor are connected in series. The catalysts prepared in this experiment were Pt/TiO2 and Pt/Al2O3 of powder type and Pd/ZrO2, Pt/ZrO2 and Pt/Al2O3 which were catalysts of honeycomb type. When a plasma-driven catalyst reactor with Pt/Al2O3 decomposed only toluene, it removed just more 20% than the only plasma reactor but the selectivity of CO2 was remarkably elevated as compared with only the plasma reactor. In case of decomposing VOCs (toluene) and NOx using plasma-enhanced catalyst reactor with Pt/ZrO2 or Pt/Al2O3, the conversion of toluene to CO2 was nearly 100% and about 80% of NOx was removed.
References
Choi JH, Kim SK, Ha SJ, Park YO, Korean J. Chem. Eng., 18(4), 456 (2001)
Mizuno A, Clements JS, US Patent 4,695,358 (1987)
Chang MB, Kushner MJ, Rood MJ, J. Environ. Eng., 119, 414 (1993)
Tokunaga O, Suzuki N, Radiat. Phys. Chem., 24, 145 (1984)
Yamamoto T, Yang CL, Beltran MR, Kravets Z, IEEE Trans. Ind. Applicat., 36, 923 (2000)
Ogata A, Yamanouchi K, Mizuno K, Kushiyama S, Yamamoto T, IEEE Trans. Ind. Applicat., 35, 1289 (1999)
Demidiouk V, Moon SI, Chae JO, Catal. Commun., 4, 51 (2003)
Kim HH, Takashima K, Katsura S, Mizuno A, J. Phys. D-Appl. Phys., 34, 604 (2001)
Einaga H, Ibusuki T, Futamura S, IEEE Trans. Ind. Appl., 37, 1476 (2001)
Hammer T, Kishmoto T, Miessner H, Rudolph R, SAE Trans., 108, 2035 (1999)
Li D, Yakushiji D, Kanazawa T, Ohkubo T, Nomoto Y, J. Electrost., 55, 311 (2002)
Song YH, Kim SJ, Choi KI, Yamamoto T, J. Electrost., 55, 189 (2002)
Kim HH, Tsunoda K, Katsura S, Mizuno A, IEEE Trans. Ind. Appl., 35, 1306 (1999)
Mizuno A, Clements JS, US Patent 4,695,358 (1987)
Chang MB, Kushner MJ, Rood MJ, J. Environ. Eng., 119, 414 (1993)
Tokunaga O, Suzuki N, Radiat. Phys. Chem., 24, 145 (1984)
Yamamoto T, Yang CL, Beltran MR, Kravets Z, IEEE Trans. Ind. Applicat., 36, 923 (2000)
Ogata A, Yamanouchi K, Mizuno K, Kushiyama S, Yamamoto T, IEEE Trans. Ind. Applicat., 35, 1289 (1999)
Demidiouk V, Moon SI, Chae JO, Catal. Commun., 4, 51 (2003)
Kim HH, Takashima K, Katsura S, Mizuno A, J. Phys. D-Appl. Phys., 34, 604 (2001)
Einaga H, Ibusuki T, Futamura S, IEEE Trans. Ind. Appl., 37, 1476 (2001)
Hammer T, Kishmoto T, Miessner H, Rudolph R, SAE Trans., 108, 2035 (1999)
Li D, Yakushiji D, Kanazawa T, Ohkubo T, Nomoto Y, J. Electrost., 55, 311 (2002)
Song YH, Kim SJ, Choi KI, Yamamoto T, J. Electrost., 55, 189 (2002)
Kim HH, Tsunoda K, Katsura S, Mizuno A, IEEE Trans. Ind. Appl., 35, 1306 (1999)