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GPS-X Technical Reference

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Modelling Fundamentals 22<br />

System Configuration<br />

The General Purpose Simulator can handle practically any flow scheme. Based on our<br />

experience it is very important to identify as closely as possible the hydraulic<br />

characteristics of a plant, including plant by-passes, overflows, flow splits and combiners,<br />

proportional, constant or SRT driven sludge wastage, etc. Parallel trains, multiple units<br />

and plug flow systems are easily simulated, but should be simplified where possible<br />

(unless the required supporting data required for calibration is available).<br />

OPERATIONAL PLANT DATA<br />

Flow Control Variables (Independent Variables)<br />

This is an important data group. For example, if the aeration capacity is not known (or<br />

cannot be estimated from the aerator power or other means), then the correct dissolved<br />

oxygen (DO) level can be set by either changing the K La or some stoichiometric or<br />

kinetic parameters (yield coefficient, growth rate, etc.). This makes the correct estimation<br />

of those parameters difficult. Similarly, model parameters having a strong effect on the<br />

aeration tank Mixed Liquor Suspended Solids (MLSS) are difficult to estimate when the<br />

wastage rate is not known.<br />

Activated Sludge Response Variables<br />

MLSS, Volatile Suspended Solids (VSS), COD of the mixed liquor, DO, and Oxygen<br />

Uptake Rate (OUR) are required to calibrate the activated sludge portion of the model.<br />

Refer to above section (p. 22) for a discussion on the importance of COD for this chapter<br />

(Why COD is Important to Know). In general, the stoichiometry of the mixed liquor<br />

(% VSS and COD/MLSS) is relatively constant over time and can be assessed<br />

occasionally during the course of a calibration/verification study, e.g., on a monthly or biweekly<br />

basis. However, the other parameters are generally dynamic, following the<br />

diurnal patterns of the plant.<br />

It is important to be able to perform a solids mass balance around the system.<br />

Accordingly, the sludge blanket height (and preferably the solids concentration profile)<br />

and underflow solids concentration are required to calibrate the settler portion of the<br />

model.<br />

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

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