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Redox-stratification controlled biofilm (ReSCoBi) for completely autotrophic nitrogen removal: The effect of co- versus counter-diffusion on reactor performance

Authors

  • Akihiko Terada,

    1. Department of Chemical Engineering, Waseda University, Shinjuku-ku, Tokyo, Japan
    2. Institute of Environment and Resources, Technical University of Denmark, DK-2800 Lyngby, Denmark; telephone: +45-45-25-16-00; fax: +45-45-93-28-50
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  • Susanne Lackner,

    1. Institute of Environment and Resources, Technical University of Denmark, DK-2800 Lyngby, Denmark; telephone: +45-45-25-16-00; fax: +45-45-93-28-50
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  • Satoshi Tsuneda,

    1. Department of Chemical Engineering, Waseda University, Shinjuku-ku, Tokyo, Japan
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  • Barth F. Smets

    Corresponding author
    1. Institute of Environment and Resources, Technical University of Denmark, DK-2800 Lyngby, Denmark; telephone: +45-45-25-16-00; fax: +45-45-93-28-50
    • Institute of Environment and Resources, Technical University of Denmark, DK-2800 Lyngby, Denmark; telephone: +45-45-25-16-00; fax: +45-45-93-28-50
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Abstract

A multi-population biofilm model for completely autotrophic nitrogen removal was developed and implemented in the simulation program AQUASIM to corroborate the concept of a redox-stratification controlled biofilm (ReSCoBi). The model considers both counter- and co-diffusion biofilm geometries. In the counter-diffusion biofilm, oxygen is supplied through a gas-permeable membrane that supports the biofilm while ammonia (NHmath image) is supplied from the bulk liquid. On the contrary, in the co-diffusion biofilm, both oxygen and NHmath image are supplied from the bulk liquid. Results of the model revealed a clear stratification of microbial activities in both of the biofilms, the resulting chemical profiles, and the obvious effect of the relative surface loadings of oxygen and NHmath image (Jmath image/Jmath image) on the reactor performances. Steady-state biofilm thickness had a significant but different effect on T-N removal for co- and counter-diffusion biofilms: the removal efficiency in the counter-diffusion biofilm geometry was superior to that in the co-diffusion counterpart, within the range of 450–1,400 µm; however, the efficiency deteriorated with a further increase in biofilm thickness, probably because of diffusion limitation of NHmath image. Under conditions of oxygen excess (Jmath image/Jmath image > 3.98), almost all NHmath image was consumed by aerobic ammonia oxidation in the co-diffusion biofilm, leading to poor performance, while in the counter-diffusion biofilm, T-N removal efficiency was maintained because of the physical location of anaerobic ammonium oxidizers near the bulk liquid. These results clearly reveal that counter-diffusion biofilms have a wider application range for autotrophic T-N removal than co-diffusion biofilms. Biotechnol. Bioeng. 2007;97:40–51. © 2006 Wiley Periodicals, Inc.

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