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Plant brochure designed by Charles L. Woodruff 1999 and revised in June 2004.


 

Kruger Oxidation Ditch - Phosphorus Removal

 
A three-stage anaerobic selector is incorporated prior to the distribution chamber. The anaerobic residence time is approximately 50 minutes based on the design flow of 2.9 MGD, which is not long enough to promote the build-up of sulphides or other noxious products sometimes associated with anaerobic treatment processes.

The RAS enters the first stage of the anaerobic selector where chemically bound oxygen in the form of nitrates is removed. The RAS then passes into the second stage where it is mixed with influent wastewater. At a microbiological level, the process functions by selectively feeding specialized activated sludge micro organisms under anaerobic conditions. The micro organisms have the ability to store energy in the form of polyphosphate chemical bonds. In the anaerobic zone, where substrate (BOD) concentration is high, the absence of oxygen causes the micro organisms to release the stored intracellular polyphosphates by decomposition to simple orthophosphate.
 

End View of Anaerobic Selector

 
The decomposition of polyphosphate to orthophosphate results in an increase of soluble phosphorus in the mixed liquor and also releases energy. The energy is used by the micro organisms to transport soluble BOD through the cell wall and to store the soluble BOD inside the cell (See Figure 2.4). Thus, the BOD concentration in the mixed liquor is reduced without the use of oxygen.
 

Figure 2.4: Biological phosphorus removal reactions

 
In the oxic phases of the process, the organisms, in the presence of dissolved oxygen, convert the stored BOD to CO2, water, and increased cell mass. A portion of the energy from this reaction then goes to recreating the intracellular polyphosphate using the orthophosphate released in the anaerobic zone. Since new cells are grown, the amount of phosphate removed from solution is greater than that previously solubilized in the anaerobic zone, thus providing for a net phosphate removal.

Phosphorus is removed from the system as a fixed biological material in the waste sludge. The amount of phosphorus in the sludge will be dependent upon the amount of BOD and phosphate in the influent and the volume of sludge produced. In addition, biological phosphorus removal is dependent on maintaining an adequate sludge blanket in the secondary clarifiers. Kruger's experience has shown that a sludge blanket of at least one foot must be maintained to promote a “stressful” environment that allows phosphorus removing organisms to proliferate. As a result of this requirement, modifications to the RAS pumping controls may be required to ensure that an adequate sludge blanket is maintained in the secondary clarifiers.

 
 

 

 

 

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