TY - JOUR
T1 - Redox-stratification controlled biofilm (ReSCoBi) for completely autotrophic nitrogen removal
T2 - The effect of co- versus counter-diffusion on reactor performance
AU - Terada, Akihiko
AU - Lackner, Susanne
AU - Tsuneda, Satoshi
AU - Smets, Barth F.
PY - 2007/5/1
Y1 - 2007/5/1
N2 - 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 (NH4+) is supplied from the bulk liquid. On the contrary, in the co-diffusion biofilm, both oxygen and NH4+ 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 NH4+ (J O2/JNH4+) 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 NH4+. Under conditions of oxygen excess (J O2/JNH4+ > 3.98), almost all NH4+ 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.
AB - 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 (NH4+) is supplied from the bulk liquid. On the contrary, in the co-diffusion biofilm, both oxygen and NH4+ 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 NH4+ (J O2/JNH4+) 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 NH4+. Under conditions of oxygen excess (J O2/JNH4+ > 3.98), almost all NH4+ 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.
KW - Biofilm modeling
KW - Co-diffusion biofilm
KW - Completely autotrophic nitrogen removal
KW - Counter-diffusion biofilm
KW - Redox-stratification controlled biofilm (ReSCoBi)
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U2 - 10.1002/bit.21213
DO - 10.1002/bit.21213
M3 - Article
C2 - 17013935
AN - SCOPUS:34247526795
SN - 0006-3592
VL - 97
SP - 40
EP - 51
JO - Biotechnology and Bioengineering
JF - Biotechnology and Bioengineering
IS - 1
ER -