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GPS-X Technical Reference

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233 Attached-Growth Models<br />

The SBC model discussed herein is available in all the libraries, using the same<br />

biological reactions found in the suspended-growth models in the appropriate library. The<br />

model can predict the extent of carbon and nitrogen removal (by uptake or oxidation) and<br />

denitrification, as well as phosphorus uptake and release (in the carbon-nitrogenphosphorus<br />

library). This model incorporates the growth kinetics and transport processes<br />

for the corresponding state variables. The profiles of the various components through the<br />

biofilm are modelled so that different environments (aerobic, anoxic and anaerobic) can<br />

exist within the biofilm.<br />

To reduce the complexity of the model, some assumptions are necessary. The limitations<br />

of this model concern the hydraulics of the submerged biological contactor and the<br />

biofilm itself. The model assumes that the flow rate and solids loading to the SBC can<br />

always be processed; that is, clogging and head loss is not modelled. The maximum<br />

thickness of the biofilm is not calculated; rather it is specified by the user. This<br />

assumption was made because there are little or no data available for<br />

calibration/verification of the maximum film thickness calculations. It is assumed that<br />

there is equal flow distribution over the entire surface area of the SBC and the media<br />

inside the SBC. The effect of the rotation speed or direction of the SBC and its impact on<br />

media sloughing is neglected. The oxygen diffused into the biofilm when the media is in<br />

the air is neglected, since the SBC media is generally submerged more than 80 percent of<br />

the time; therefore, the SBC is modelled as completely submerged.<br />

Similar to the trickling filter model and the RBC, the SBC is more complex than the<br />

suspended-growth models since the state variables are now modelled through the film<br />

and through various SBC stages (or shafts).<br />

Conceptual Model<br />

The submerged biological contactor is divided into a number of stages (default is 2<br />

stages) each representing a baffled SBC shaft. The transfer of the state variables between<br />

each of these stages is through the liquid flow. The biofilm in each stage is modelled as a<br />

number of layers (default is one layer as the liquid film on top of five layers as the<br />

biofilm). The transfer of soluble state variables between each of these layers is by<br />

diffusion. Particulate variables have a certain physical volume associated with them and<br />

can be displaced into the neighbouring layer by growth processes. Each layer of the<br />

biofilm is modelled as a CSTR with the same biological reactions as the suspendedgrowth<br />

biological model (See Appendix A for the mantis model). Attachment and<br />

detachment coefficients are used to provide for a means of transfer of particulate<br />

components between the biofilm surface and the liquid film.<br />

<strong>GPS</strong>-X <strong>Technical</strong> <strong>Reference</strong>

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