Year

2015

Degree Name

Doctor of Philosophy

Department

School of Mathematics and Applied Statistics

Abstract

The activated sludge process is one of the major aerobic processes used in the biological treatment of wastewater. A significant drawback of this process is the production of exces sludge, the disposal of which can account for 50-60% of the running costs of a plant. Thus there is a growing interest in methods that reduce the volume and mass of excess sludge produced as part ofj biological wastewater treatment processes. In practice a target value is often set for the sludge content inside the bioreactor. If the sludge content is higher than the target value, the process is stopped and the reactor is cleaned. The is undesirable as it increases running costs.

In chapter 2 we investigate a simple model for the activated sludge process in which the influent contains a mixture of soluble and biodegradable praticulate substrate. Within the bioreactor the biodegradable particulate substrate is hydrolyzed to form soluble substrate. The soluble organics are used for energy and growth by the biomass. Biomass decay produces soluble substrate in addition to inert material. We use steady-state analysis to investigate how the amount of sludge formed depends upon the residence time and the use of settling unit. We show that when the steady-state sludge content is plotted as a function of the residence time that there are five generic response diagrams, depending upon the value of the effective recycle parameter. Four of them are desirable because the sludge content is below the target value if the residece time is higher than some critical value that is not 'too large' in practice.

In chapter 3 we investigate how the volume and mass of excess sludge produced by the activated sludge proces can be reduced by coupling the bioreactor used in the process to sludge disintegration unit.

In chapter 4 a seemingly minor modification is made to the model in chapter 2. Instead of the biomass decay producing soluble substrate and inert material it produces slowly biodegradable substrate and non-biodegradable particulates. We use steady-state analysis to investigate how the amount of sludge formed depends upon the residence time and the use of a settling unit. We show that when the steady-state sludge content is plotted as a function of the residence time that there are three generic response diagrams, depending upon the value of the effective recycle parameter. In particular, the seemingly minor change has had a pronounced effect on the behavior of the model. Unlike the model investigated in chapter 2 we find that in practice excessive sludge formation is inevitable.

In chapter 5 we investigate how increasing the decay rate effected the bheavior ofj models one and two. We find htat this is not an effective way to reduce sludge formation.

In the final chapter we summarize the results ofj the thesis and include recommendations for future research.

FoR codes (2008)

0102 APPLIED MATHEMATICS, 0904 CHEMICAL ENGINEERING, 0907 ENVIRONMENTAL ENGINEERING

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Unless otherwise indicated, the views expressed in this thesis are those of the author and do not necessarily represent the views of the University of Wollongong.