DOI QR코드

DOI QR Code

Treatment Characteristics of Trichloroethylene(TCE) by Oxidation and Reduction with Nanoscale Zero-valent Iron

나노영가철의 산화·환원에 의한 트리클로로에틸렌 처리특성

  • Park, Young-Bae (Department of Environmental Engineering, Catholic University) ;
  • Jung, Yong-Jun (Department of Environmental Engineering, Catholic University) ;
  • Choi, Jeong-Hak (Department of Environmental Engineering, Catholic University) ;
  • Moon, Boung-Hyun (Department of Environmental Engineering, Changwon National University)
  • 박영배 (부산가톨릭대학교 환경공학과) ;
  • 정용준 (부산가톨릭대학교 환경공학과) ;
  • 최정학 (부산가톨릭대학교 환경공학과) ;
  • 문병현 (창원대학교 환경공학과)
  • Received : 2014.01.16
  • Accepted : 2014.04.10
  • Published : 2014.05.30

Abstract

This study examined the treatment characteristics of hard-to-degrade pollutants such as TCE which are found in organic solvent and cleaning wastewater by nZVI that have excellent oxidation and reduction characteristics. In addition, this study tried to find out the degradation characteristics of TCE by Fenton-like process, in which $H_2O_2$ is dosed additionally. In this study, different ratios of nZVI and $H_2O_2$, such as 1.0 mM : 0.5 mM, 1.0 mM : 1.0 mM, and 1.0 mM : 2.0 mM were used. When 1.0 mM of nZVI was dosed with 1.0 mM of $H_2O_2$, the removal efficiency of TOC was the highest and the first order rate constant was also the highest. When 1mM of nZVI was dosed with 0.5 mM of $H_2O_2$, the first order rate constant and removal efficiency were the lowest. The size of first order rate constant and removal efficiency was in the order of nZVI 1.0 mM : $H_2O_2$ 1.0 mM > nZVI 1.0 mM : $H_2O_2$ 2.0 mM > nZVI 1.0 mM : $H_2O_2$ 0.5 mM > $H_2O_2$ 1.0 mM > nZVI 1.0 mM. It is estimated that when 1.0 mM of nZVI is dosed with 1.0 mM of $H_2O_2$, $Fe^{2+}$ ion generated by nZVI and $H_2O_2$ react in the stoichiometric molar ratio of 1:1, thus the first order rate constant and removal efficiency are the highest. And when 1.0 mM of nZVI is dosed with 2.0 mM of $H_2O_2$, excessive $H_2O_2$ work as a scavenger of OH radicals and excessive $H_2O_2$ reduce $Fe^{3+}$ into $Fe^{2+}$. As for the removal efficiency of TOC in TCE by simultaneous dose and sequential dose of nZVI and $H_2O_2$, sequential dose showed higher first order reaction rate and removal efficiency than simultaneous dose. It is estimated that when nZVI is dosed 30 minutes in advance, pre-treatment occurs and nanoscale $Fe^0$ is oxidized to $Fe^{2+}$ and TCE is pre-reduced and becomes easier to degrade. When $H_2O_2$ is dosed at this time, OH radicals are generated and degrade TCE actively.

Keywords

References

  1. Agrawal, A., Tratnyek, P. G., 1996, "Reduction of nitro aromatic compounds by zero-valent iron metal", Environ. Sci. & Technol., 30, 153-160. https://doi.org/10.1021/es950211h
  2. Arnold, W. A., Roberts, A. L., 2000, "Pathways and kinetics of chlorinated ethene and chlorinated acetylene reaction with Fe(0) particles", Environ. Sci. & Technol., 34, 1794-1805. https://doi.org/10.1021/es990884q
  3. Choi, S. H., Jang, Y. Y., Hwang, G. Y., Kim, J. H., 1999, "Treatment of hazardous chemicals by Nanoscale Iron powder", Journal of KoSSGE, 4(3), 85-93.
  4. Gilliham, R. W., O'Hannesin, S. F., 1994, "Enhanced degradation of halgenated aliphatics by zero valent iron", Ground Water, 32, 958-967. https://doi.org/10.1111/j.1745-6584.1994.tb00935.x
  5. Jeffers, P. M., Ward, L. M., Wolfe, N. L., 1989, "Homogenous hydrolysis rate constants for selected chlorinated methanes, ethanes, ethenes and propanes", Environ. Sci. & Technol., 23, 965-969. https://doi.org/10.1021/es00066a006
  6. Johnson, T. L., Scherer, M. M., Tratnyek, P. G., 1996, "Kinetics of halogenated organic compound degradation by iron metal" Environ. Sci. Technol., 30, 2634-2640. https://doi.org/10.1021/es9600901
  7. Joo, S. H., 2004, "Oxidative degradation of organic contaminants using nanoscale zero valent iron", Ph. D. Dissertation, New South Wales University, USA.
  8. O, D. G., 1993, "Oxidation treatment of Organics in Wastewater by Fenton reagent ", Ph. D. Dissertation, Inha University.
  9. Orth, W. S., Gilliham, R. W., 1996, "Dechlorination of trichloroethene in aqueous solution using $Fe^0$", Environ. Sci. & Technol., 30, 66-71. https://doi.org/10.1021/es950053u
  10. Park, S. H., 2005 "Characteristics of Fenton Oxidation in $Fe^0$, $Fe^{(2+)}$, $Fe^{(3+)}$ / $H_2O_2$ Systems", Master of Engineering Dissertation, University of Seoul.
  11. Patterson, J. W., 1985, "Industrial wastewater treatment technology", Butterworth, Boston,
  12. Quinn, J., Geiger, C., Clausen, C., Brooks, K., Coon, C., Ohara, S., 2005, "Field demonstration of DNAPL dehalogenation using emulsified zero-valent iron", Environ. Sci. Technol. 39, 1309-1318. https://doi.org/10.1021/es0490018
  13. Robert, A. L., Totten, L. A., Arnold, W. A., Burris, D. R., Cambell, T. J., 1996, "Reductive elimination of chlorinated ethylenes by zero valent metal", Eviron. Sci. & Technol., 30, 2654-2659. https://doi.org/10.1021/es9509644
  14. Roy, S., Bay, B., Chakravorty, E., 1996, "Magnetic properties of iron nanoparticles grown in a glass matrix", J. Appl. Phys., 79, 1642-1650. https://doi.org/10.1063/1.361008
  15. Shin, H. S., Lim, J. R., 1995, "Processes for the Wastewater Treatment Containing Trichloroethylene (II)", Journal of Korean Society of Environmental Engineer, 17(1), 1079-1088.
  16. Tratnyek, P. G., Matheson, L. J., 1994, "Reductive dehalogenation of chlorlnated methanes by iron metal", Environ. Sci. & Technol., 28, 2045-2053. https://doi.org/10.1021/es00061a012
  17. Wang, C. B., Zhang, W. X., 1997, "Synthesizing nanoscale iron particles for rapid and complete dechlorination of TCE and PCBs", Environ. Sci.. & Technol. 31, 2154-2156. https://doi.org/10.1021/es970039c
  18. Zhang, W. X., 2003, "Nanoscale iron particles for environmental remediation: An overview", Journal of Nanoparticle Research, 5, 205-209.