TECHNICAL PAPERS
Oct 15, 2002

Dynamic Model of Ozone Contacting Process with Oxygen Mass Transfer in Bubble Columns

Publication: Journal of Environmental Engineering
Volume 128, Issue 11

Abstract

The dynamic process of the dissolution of ozone in a countercurrent bubble column is studied for model establishment. Bubble columns have been used widely for ozone contacting in the plant and laboratory. Ozone is produced by oxygen-enriched gas through an ozone generator, and introduced into the bottom of the column equipped with the gas diffuser. The ozone contacting system proceeds for a temporary and unsteady period before reaching steady state. The available ozone dissolution models employed for the description of the dissolved ozone profiles were commonly developed for the steady state. Moreover, oxygen mass transfer is usually neglected in the preceding ozone dissolution models. However, this information is desirable for proper operation of ozone dissolution in a bubble column. Thus, the objective of this study is to model and investigate the dynamic ozone dissolution process in a bubble column with the oxygen mass transfer. The dynamic axial dispersion model proposed is employed to predict the variations of ozone and oxygen concentrations along the column, and the amount of off-gas. The validity of the model is demonstrated by comparing the predicted results with the experimental data. The dynamic model of ozone dissolution is useful and referable for proper prediction of the variables of the ozone contacting system in a bubble column.

Get full access to this article

View all available purchase options and get full access to this article.

References

Akita, K., and Yoshida, F.(1973). “Gas holdup and volumetric mass transfer coefficient in bubble columns.” Ind. Eng. Chem. Process Des. Dev., 12(1), 76–80.
Alvarez-Cuenca, M., and Nerenberg, M. A.(1981). “Oxygen mass transfer in bubble columns working at large gas and liquid flow rates.” AIChE J., 27(1), 66–73.
Biń, A. K.(1995). “Application of a single-bubble model in estimation of ozone transfer efficiency in water.” Ozone. Sci. Eng., 17(5), 469–484.
Chang, C. Y., et al. (2001). “Kinetics of decomposition of polyethylene glycol in electroplating solution by ozonation with UV radiation.” J. Environ. Eng., 127(10), 908–915.
Chiu, C. Y., et al. (1997). “A refined model for ozone mass transfer in a semibatch stirred vessel.” Ozone. Sci. Eng., 19(5), 439–456.
Chiu, C. Y., Chang, C. Y., Chen, Y. H., Yu, Y. H., Chiang, P. C., and Ku, Y. (2002). “Ozone mass transfer with combined effects of ozone decomposition and reaction with pollutants in a semibatch stirred vessel.” J. Chin. Inst. Chem. Eng., in press.
Danckwerts, P. V. (1970). Gas–liquid reactions, 1st Ed., McGraw-Hill, New York.
Deckwer, W. D., Burckhart, R., and Zoll, G.(1974). “Mixing and mass transfer in tall bubble columns.” Chem. Eng. Sci., 29, 2177–2188.
Deckwer, W. D., Nguyen-Tien, K., Kelkar, B. G., and Shah, Y. T.(1983). “Applicability of axial dispersion model to analyze mass transfer measurements in bubble columns.” AIChE J., 29(6), 915–922.
Deckwer, W. D., and Schumpe, A.(1993). “Improved tools for bubble column reactor design and scale-up.” Chem. Eng. Sci., 48(5), 889–911.
Hikita, H., Asai, S., Tanigawa, K., Segawa, K., and Kitao, M.(1981). “The volumetric liquid-phase mass transfer coefficient in bubble columns.” Chem. Eng. J., 22, 61–69.
Huang, W. H., et al. (1998). “A refined model for ozone mass transfer in a bubble columns.” J. Environ. Sci. Health, Part A: Toxic/Hazard. Subst. Environ. Eng., 33(3), 441–460.
Kuo, C. H., and Huang, C. H.(1995). “Aqueous phase ozonation of cholorophenols.” J. Haz. Mat., 41, 31–45.
Langlais, B., Reckhow, D. A., and Brink, D. R. (1991). Ozone in water treatment application and engineering, 1st Ed., Lewis, Mich.
Le Sauze, N., Laplanche, A., Martin, N., and Martin, G.(1993). “Modeling of ozone transfer in a bubble column.” Water Res., 27(6), 1071–1083.
Letzel, H. M., Schouten, J. C., Krishna, R., and Van den Bleek, C. M.(1999). “Gas holdup and mass transfer in bubble column reactors operated at elevated pressure.” Chem. Eng. Sci., 54(13–14), 2237–2246.
Levenspiel, O. (1972). Chemical reaction engineering, 2nd Ed., Wiley, New York.
Li, H., et al. (2000). “Kinetics of ozonation of polyethylene glycol in printed wiring board electroplating solution.” J. Chin. Inst. Environ. Eng. (Taiwan), 10(1), 69–75.
Mariñas, B. J., Liang, S., and Aieta, E. M.(1993). “Modeling hydrodynamics and ozone residual distribution in a pilot-scale ozone bubble-diffuser contactor.” J. Am. Water Works Assoc., 85(3), 90–99.
Masschelein, W. J. (1982). Ozonization manual for water and wastewater treatment, 1st Ed., Wiley, New York.
McGhee, T. J. (1991). Water supply and sewerage, 6th Ed., McGraw-Hill, New York.
Qiu, Y., Kuo, C. H., and Zappi, M. E.(2001). “Performance and simulation of ozone adsorption and reaction in a stirred-tank reactor.” Environ. Sci. Technol., 35(1), 209–215.
Rankness, K., et al. (1996). “Guideline for measurement of ozone concentration in the process gas from an ozone generator.” Ozone. Sci. Eng., 18(3), 209–229.
Rice, R. G., Tupperainen, J. M. I., and Hedge, R. M.(1981). “Dispersion and hold-up in bubble columns—Comparison of rigid and flexible spargers.” Can. J. Chem. Eng., 59(6), 677–687.
Sawyer, C. N., McCarty, P. L., and Parkin, G. F. (1994). Chemistry for environmental engineering, 4th Ed., McGraw-Hill, New York.
Shah, Y. T., Kelkar, B. G., Godbole, S. P., and Deckwer, W. D.(1982). “Design parameters estimations for bubble column reactors.” AIChE J., 28(3), 353–379.
Shetty, S. A., Kantak, M. V., and Kelkar, B. G.(1992). “Gas-phase backmixing in bubble-column reactors.” AIChE J., 38(7), 1013–1026.
Smith, D. W., and Zhou, H.(1994). “Theoretical analysis of ozone distribution performance in a bubble column.” Ozone. Sci. Eng., 16(5), 429–441.
Sotelo, J. L., Beltrán, F. J., Benı´tez, F. J., and Beltrán-Heredia, J.(1989). “Henry’s law constant for the ozone–water system.” Water Res., 23(10), 1239–1246.
Staehelin, J., and Hoigné, J.(1982). “Decomposition of ozone in water: Rate of initial by hydroxide ions and hydrogen peroxide.” Environ. Sci. Technol., 16(10), 676–681.
Wilke, C. R., and Chang, P. C.(1955). “Correlations of diffusion coefficients in dilute solutions.” AIChE J., 1, 264–270.
Wright, P. C., Meeyoo, V., and Soh, W. K.(1998). “A study of ozone mass transfer in a cocurrent downflow jet pump contactor.” Ozone. Sci. Eng., 20(1), 17–33.
Zahradnı´k, J., and Fialová, M.(1996). “The effect of bubbling regime on gas and liquid phase mixing in bubble column reactors.” Chem. Eng. Sci., 51(10), 2491–2500.
Zhou, H., Smith, D. W., and Stanley, S. J.(1994). “Modeling of dissolved ozone concentration profiles in bubble columns.” J. Environ. Eng., 120(4), 821–840.

Information & Authors

Information

Published In

Go to Journal of Environmental Engineering
Journal of Environmental Engineering
Volume 128Issue 11November 2002
Pages: 1036 - 1045

History

Received: Aug 17, 2001
Accepted: Feb 13, 2002
Published online: Oct 15, 2002
Published in print: Nov 2002

Permissions

Request permissions for this article.

Authors

Affiliations

Y. H. Chen
Graduate Institute of Environmental Engineering, National Taiwan Univ., Taipei 106, Taiwan.
C. Y. Chang
Graduate Institute of Environmental Engineering, National Taiwan Univ., Taipei 106, Taiwan (corresponding author).
C. Y. Chiu
Dept. of Environmental Engineering, Lan-Yang College of Technology, I-Lan 261, Taiwan.
W. H. Huang
Graduate Institute of Environmental Engineering, National Taiwan Univ., Taipei 106, Taiwan.
Y. H. Yu
Graduate Institute of Environmental Engineering, National Taiwan Univ., Taipei 106, Taiwan.
P. C. Chiang
Graduate Institute of Environmental Engineering, National Taiwan Univ., Taipei 106, Taiwan.
Y. Ku
Dept. of Chemical Engineering, National Taiwan Univ. of Science and Technology, Taipei 106, Taiwan.
J. N. Chen
Graduate Institute of Environmental Engineering, National Chiao-Tung Univ., Hsin-Chu 300, Taiwan.

Metrics & Citations

Metrics

Citations

Download citation

If you have the appropriate software installed, you can download article citation data to the citation manager of your choice. Simply select your manager software from the list below and click Download.

Cited by

View Options

Get Access

Access content

Please select your options to get access

Log in/Register Log in via your institution (Shibboleth)
ASCE Members: Please log in to see member pricing

Purchase

Save for later Information on ASCE Library Cards
ASCE Library Cards let you download journal articles, proceedings papers, and available book chapters across the entire ASCE Library platform. ASCE Library Cards remain active for 24 months or until all downloads are used. Note: This content will be debited as one download at time of checkout.

Terms of Use: ASCE Library Cards are for individual, personal use only. Reselling, republishing, or forwarding the materials to libraries or reading rooms is prohibited.
ASCE Library Card (5 downloads)
$105.00
Add to cart
ASCE Library Card (20 downloads)
$280.00
Add to cart
Buy Single Article
$35.00
Add to cart

Get Access

Access content

Please select your options to get access

Log in/Register Log in via your institution (Shibboleth)
ASCE Members: Please log in to see member pricing

Purchase

Save for later Information on ASCE Library Cards
ASCE Library Cards let you download journal articles, proceedings papers, and available book chapters across the entire ASCE Library platform. ASCE Library Cards remain active for 24 months or until all downloads are used. Note: This content will be debited as one download at time of checkout.

Terms of Use: ASCE Library Cards are for individual, personal use only. Reselling, republishing, or forwarding the materials to libraries or reading rooms is prohibited.
ASCE Library Card (5 downloads)
$105.00
Add to cart
ASCE Library Card (20 downloads)
$280.00
Add to cart
Buy Single Article
$35.00
Add to cart

Media

Figures

Other

Tables

Share

Share

Copy the content Link

Share with email

Email a colleague

Share