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Selective Catalytic Reduction of Nitric Oxide over Metal Exchanged ZSM-5 Catalysts

금속을 이온교환시킨 ZSM-5 촉매 상에서 Nitric Oxide의 환원반응

  • Ahn, Sung-Hwan (Division of Ceramic and Chemical Engineering, Myongji University) ;
  • Kim, Tae-Ok (Division of Ceramic and Chemical Engineering, Myongji University) ;
  • Hahm, Hyun-Sik (Division of Ceramic and Chemical Engineering, Myongji University)
  • 안성환 (명지대학교 공과대학 세라믹화학공학부) ;
  • 김태옥 (명지대학교 공과대학 세라믹화학공학부) ;
  • 함현식 (명지대학교 공과대학 세라믹화학공학부)
  • Published : 2000.03.31

Abstract

The selective catalytic reduction(SCR) of nitric oxide by ethane in the presence of oxygen was investigated on Cu-ZSM-5, Co-ZSM-5 and Ga-ZSM-5 catalysts over a range of 400, 450 and $500^{\circ}C$. The catalysts were prepared by ion-exchange method. The composition of the reactant gases were 1000 ppm of NO, 1000 ppm of $C_{2}H_{6}$ and 2.5% of $O_{2}$, and the reaction was conducted in a fixed-bed reactor at 1 atm. For the 20wt% Co-ZSM-5(50) catalyst, the NO conversion reached up to 100%, while the $C_2H_6$ conversion and the CO selectivity were about 50% and 25%, respectively, at $450^{\circ}C$. For the 20wt% Cu-ZSM-5(50) catalyst, the NO conversion and the C2H6 conversion were about 80% and 100%, respectively, but there was no CO produced. The metal ion-exchanged ZSM-5 catalysts exhibited a tendency to increase the NO conversion with the Si/Al ratio of the ZSM-5, that is, NO conversion was inversely proportional to the acidity of the catalysts. But, the effect of the acidity on NO conversion was not so large. From the XRD results of the catalysts before and after SCR reaction it was found that there was no structural change.

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