Non-thermal Plasma Process for simultaneous removal of SO2/NOx from a Sintering Plant of Steel Works

  • Nam, Chang-Mo (Div. of Environmental Engineering Yeungnam College of Science & Technology) ;
  • Mok, Young-Sun (Dept. of Chem. Eng., Cheju University) ;
  • Kwon, Gi-Hong (Div. of Environmental Engineering Yeungnam College of Science & Technology) ;
  • Suh, You-Duck (Div. of Environmental Engineering Yeungnam College of Science & Technology) ;
  • Cho, Byeung-Rak (Div. of Environmental Engineering Yeungnam College of Science & Technology)
  • 남창모 (영남이공대학 환경공학계열) ;
  • 목영선 (제주대학교 청정화학공학과) ;
  • 권기홍 (영남이공대학 환경공학계열) ;
  • 서유덕 (영남이공대학 환경공학계열) ;
  • 조병락 (영남이공대학 환경공학계열)
  • Received : 2002.01.10
  • Accepted : 2003.02.20
  • Published : 2003.02.28

Abstract

For the simultaneous removal of $SO_2$/NOx from an iron-ore sintering plant, industrial plasma experiments have been conducted with a flue gas flow rate of $5,000Nm^3/hr$. The maximum 40kW power using the magnetic pulse compression (MPC) system generates a peak value of 100-150kV pulse voltage with its risetime of 200nsec and full width at half maximum (FWHM) of 500nsec, and with a frequency <300Hz. The plasma reactor module adopts a wire-plate structure with a gap of 200-400mm ID between plates. Initial concentrations of $SO_2$ and NOx were around 100-150ppm, respectively in the presence of 15% $O_2$ and <10% $H_2O$. Various reaction parameters such as specific energy ($Whr/Nm^3$), $NH_3$ injection with corona discharge, flow rate and injection of hydrocarbons were investigated for $SO_2$/NOx removal characteristics. About 90/65% of $SO_2$/NOx were simultaneously removed with a specific energy of $3.0Whr/Nm^3$ when both $NH_3$ and hydrocarbons were injected. Practical implications that the pilot-scale plasma results provide are further discussed.

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