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Application of High-performance Jet Loop Reactor for the Decolorization of Reactive black 5 and Mineralization of Oxalic Acid by Ozone  

Byun, Seok-jong (Korea Institute of Science Technology (KIST))
Geissen, Sven-Uwe (Institut fuer Thermische Verfahrenstechnik, Technical University Clausthal)
Vogelpohl, Aflons (Institut fuer Thermische Verfahrenstechnik, Technical University Clausthal)
Cho, Soon-haing (Division of Environmental, Civil and Transportation Engineering, Ajou University)
Yoon, Je-yong (Seoul National University, School of Chemical Eng.)
Kim, Soo-Myung (SAMBO EN-Tec. Co., Ltd.)
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Abstract
As an ozone contactor, we newly adopted HJLR (High-performance Jet Loop Reactor) for the decolorization of Reactive black 5 and the mineralization of oxalic acid, which has been applied exclusively in biological wastewater treatments and well-known for high oxygen transfer characteristics. The ozonation efficiency for organic removals and ozone utilization depending on the mass transfer rate were compared to those of Stirred bubble column reactor, which was controlled by varing energy input in the HJLR and Stirred bubble column reactor. The results were as follows; first, the decolorization rate of Reactive black 5 in the HJLR reactor was nearly proportional to the increasing $k_La$. When the $k_La$ was increased by 25 % from $13.0hr^{-1}$ to $16.4hr^{-1}$, 30 % of the k' (apparent reaction rate constant) was increased from 0.1966 to $0.2665min^{-1}$ (Stirred bubble column; from 0.1790 to $0.2564min^{-1}$). Ozone transfer was found to be a rate-determining step in decolorizing Reactive black 5, which was supported by that no residual ozone was detected in all of the experiments. Second, the mineralization of oxalic acid was not always proportional to the increasing $k_La$ in the RJLR reactor. The rate-determining step for this reaction was OH(OH radical) production with ozone transfer, because residual ozone was always detected during the ozonation of oxalic acid in contrast with Reactive black 5. This result indicates that the increase of $k_La$ in the HJLR reactor is beneficial only when there are in ozone transfer limited regions. In addition, regardless of $k_La$, the mineralization of oxalic acid was nearly accomplished within 60 minutes. It was interpreted as that the longer staying of residual ozone by whirling liquid in the HJLR reactor contributed to an high ozone utilization(83-94%), producing more OR radicals.
Keywords
HJLR reactor; Mass transfer; Ozone; Oxalic acid; Reactive black 5;
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  • Reference
1 Rushton, J. H., Mixing of Liquids in Chemical Processing, Industrial & Engineering Chemistry, 44(12), pp. 2931 (1952)
2 Bader, H and Hoigne, J., Determination of Ozone in Water by the Indigo Method, Wat. Res., 15, pp. 449-456 (1981)
3 Beltran, F. J., Gmez-Serraxo, V and Durn A., Degradation Kinetics of p-nitrophenol Ozonation in Water, Wat. Res., 20(1), pp. 9-17 (1992)
4 Lee, S. Y., Ruutel, P., Barratt, P. A. and Tsui, Y. P., Impinging Zone Reactor And Its Mathematical Model For Ozonation of Waste Water, Ozone Science & Engineering, 21, pp. 501-522 (1999)
5 Baron, J. Martin-lonesco, N., Puznava, N., Fargeas, P., Peraudeau, M., The Flottazone Process to Combine Flotation and Ozonation in the Same Reactor, Proceedings of the 13th Ozone World Congress, Kyoto, 1, pp. 43-48 (1997)
6 변석종, 조순행, 윤제용, 김수명, 고효율 Jet Loop 반응기 및 수처리 응용, 첨단환경기술, 11(10), pp. 88-95 (2003)
7 Glaze, W. H., Kang, J. W., Chapin, D. H., The Chemistry of Water Treatment Process Involving Ozone, Hydrogen peroxide and Ultraviolet Radiation, Ozone Science & Engineering, 9, pp. 335-352 (1987)
8 Hoigne, J. and Bader. H., Rate Constants of Reactions of Ozone with Organic and Inorganic Compounds in Water-I, Wat. Res., 17, pp. 173-183 (1983)
9 Wachsmann, U., Rabiger, N. and Vogelpohl, A., The Compact Reactor - a Newly Developed Loop Reactor with a High Mass Transfer Performance, Ger. Chem. Eng., 7, pp. 39-44 (1984)
10 Wu, J. and Wang, T., Ozonation of Aqueous Azo Dye in a Semi-Batch Reactor, Wat. Res., 35(4), pp. 1093-1099 (2001)
11 Gottschalk, C., Libra, A., Saupe, A., Part B: Ozone Applied, Ozonation of Water and Waste Water, Wiley- VCH, pp. 39-79 (2000)
12 Gaddis, E. S. and Vogelpohl, A., The Impinging-stream Reactor: A High Performance Loop Reactor For Mass Transfer Controlled Chemical Reactions, Chemical Engineering Science, 47(9-11), pp. 2877-2882 (1992)
13 Kim, S. M., Geissen, S. U. and Vogelpohl, A., 'Landfill Leachate Treatment by a Photoassisted Fenton Reaction,' Water Science & Technology, 35(4), pp. 239-248 (1997)
14 Wright, Ph. C., Meeyoo, V. and Soh, W. K., A Study of Ozone Mass Transfer in a Cocurrent Downflow Jet Pump Contactor, Ozone Sci. & Eng., 20, pp. 17-33 (1998)
15 Yocum, F. H., Ozone Mass Transfer in Stirred Vessel. 86th National Meeting of American Institute of Chemical Engineering (1979)