Optimisation of Noosa BNR plant to improve performance
and reduce operating costs
M. Thomas*, P. Wright*, L. Blackall**, V. Urbain*** and J. Keller**
* Australian Water Services, PO Box 646, Cronulla, NSW 2230, Australia
(E-mail: michael.thomas@aws.aust.com)
** Advanced Wastewater Management Centre University of Queensland
*** Fairtec France
Abstract Noosa WWTP is publicly owned and privately operated by Australian Water Services. The
process includes primary sedimentation, raw sludge fermentation, biological nutrient removal (BNR), sand
filtration and ultraviolet (UV) disinfection. An innovative feature of the plant is the supplementary carbon
dosing facility to avoid the use of metal salts (alum or ferric) for phosphorus removal. The average flow
treated during 2000 was 9.0 ML/d. The annual 50 percentile effluent quality requirements for nutrients are
total N < 5 mg/L and total P < 1 mg/L. The objectives of this project were to: determine the cause of variability
in phosphorus removal; develop a strategy to control the variability in phosphorus removal; and minimise the
operating cost of supplementary carbon dosing while achieving the effluent quality requirements. An
investigation of chemical and microbiological parameters was implemented and it was concluded that there
were several factors causing variability in phosphorus removal, rather than a single cause. The following four
major causes were identified, and the control strategies that were adopted resulted in the plant achieving
annual 50 percentile effluent total P = 0.37 mg/L and total N = 3.0 mg/L during 2001. First, phosphorus
removal was limited by the available VFA supply due to consumption of VFA by other organisms competing
with phosphate accumulating organisms (PAO), and due to diurnal variations in the sewage VFA and
phosphate concentrations. Therefore, supplementary carbon dosing was essential to make allowance for
competing reactions. Second, increasing the fermenter VFA yield via supplementary carbon dosing with
molasses was found to be an effective and economic way of ensuring reliable phosphorus removal. Third,
nitrate in the RAS resulted in consumption of VFA by denitrifying bacteria, particularly with process
configurations where the RAS was recycled directly into the anaerobic zone. Incorporating a RAS
denitrification zone into the process rectified this problem. Finally, glycogen accumulating organisms (GAO)
were observed in BNR sludge samples, and consumption of VFA by GAO appeared to cause decreased
phosphorus removal. Better phosphorus removal was obtained using VFA derived from the fermenter than
dosing an equivalent amount of acetic acid. It was hypothesized that GAO have a competitive advantage to
use acetate and PAO have a competitive advantage to use propionate, butyrate or some other soluble COD
compound in the fermenter effluent. Contrary to popular belief, acetate may not be the optimum VFA for
biological phosphorus removal. The competition between PAO and GAO for different VFA species under
anaerobic conditions requires further investigation in order to control the growth of GAO and thereby
improve reliability of biological phosphorus removal processes.
Keywords Acetic acid; biological phosphorus removal; GAO; molasses; VFA
Introduction
Noosa wastewater treatment plant (WWTP) is located 150 km north of Brisbane. The plant
is publicly owned by Noosa Council and privately operated under a 25-year contract by
Australian Water Services. The design capacity of the plant is 12 ML/d and the average dry
weather flow treated during 2000 was 9.0 ML/d, which was equivalent to a population of
36,000 people. However, during the peak summer tourism season the flow increased to the
design flow of 12 ML/d.
The Noosa region is noted for its superb natural environment and it is one of
the premium resort areas in Australia. Noosa Council has a strong commitment to
Water Science and Technology Vol 47 No 12 pp 141–148 © 2003 IWA Publishing and the authors
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