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GPS-X Technical Reference

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309 Others Models<br />

There are three parameters F max, F min and k a used in the model. The parameter F max may be<br />

interpreted as the amount of metal required to remove the said component at very low<br />

concentrations. It is general observation that the amount of metal required at lower concentration<br />

of soluble component is much higher than the metal amount required when the concentration of<br />

soluble component is higher. The parameter of F min, can be interpreted as the amount of metal<br />

required to remove the said component at high concentrations. The parameter of k a signifies the<br />

transition between the F min and F max. Higher values of k a will result in a very steep transition<br />

between the F min and F max, essentially improving the removal efficiencies. Conversely, lower<br />

values of k a will result in a mild transition and thus decreasing the removal efficiencies.<br />

It is important to highlight here regarding the fate of the removed soluble components. As, the<br />

flocculation process does not cause any mass loss, the removed soluble compounds are just<br />

converted into their particulate state. The si, scol and snd are just transformed to xi, xs and xns<br />

states respectively.<br />

It should be noted that the value of these parameters depends on the environmental conditions<br />

temperature, pH, mixing, and wastewater characteristics. Therefore, it is recommended that<br />

adequate calibration is performed to find the appropriate values for specific cases.<br />

GRIT CHAMBER<br />

The model associated with this object is a simple empirical model where grit production is<br />

directly proportional to the flow coming in the grit chamber. The amount of grit produced (in<br />

grams per m 3 of influent) is user specified.<br />

STRUVITE PRECIPITATION MODEL<br />

The struvite precipitation reactor model represents an up-flow granular bed reactor with recycle.<br />

The model uses a bed fluidization model to estimate the granular bed height and the solid<br />

concentration in the effluent stream. An internal recycle is provided to achieve bed fluidization<br />

velocity required by the user. A typical layout showing the application of struvite reactor is as<br />

shown in Figure 11-6. Some typical outputs from the struvite precipitation model are as shown in<br />

Figure 11-7and Figure 11-8.<br />

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

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