Introduction
In this chapter, a quantitative model is developed that describes the removal of organic material in the activated sludge system and its consequences for the principal parameters of the process:
- Effluent quality
- Excess sludge production
- Oxygen demand
The model is applicable to all aerobic suspended sludge treatment systems, which include the different versions of the conventional activated sludge system, sequential batch reactors, carrousels and aerated lagoons. It will be demonstrated that the model can easily be extended to include the processes of nitrogen removal and phosphorus removal, while it is also shown that the model remains valid when it is used for sewage that has received anaerobic pre-treatment. Most of the concepts presented in this section have been developed at the University of Cape Town (UCT) in South Africa and form the backbone of the activated sludge models as developed by the specialist group of the International Water Association (IWA; 1986, 1994 and 2000).
In summary, the main advantages of this simplified steady state activated sludge model are:
- Design optimisation of activated sludge processes
- Incorporation of nutrient removal processes, both for nitrogen and phosphorus
- Easy integration with the design of auxiliary systems such as settlers and thickeners, sludge treatment units (aerobic digesters and anaerobic digesters) and pre-treatment units (primary clarifiers and UASB reactors, allowing for truly optimised design
Contents of this section
| Influent- and biomass composition |
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| Determination of oxygen uptake rate |
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General model of the activated sludge system
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We regret that the sections on the "General model of the activated sludge system", "Aeration" and "System Configurations" are not available as a free online resource. If you want to know more, please purchase the handbook. More info ? |
