Projects

Wynnum WWTP

Wynnum 1 Thumb Wynnum 2 Thumb Wynnum 3 Thumb

Client:

Brisbane Water (BWEA Alliance)

Location:

Wynnum, QLD

Service:

Wastewater treatment

Value:

AUD $130 M

Completion Date:

2006

The Brisbane Water Enviro Alliance was a pure alliance project involving a series of plant upgrades to four of Brisbane Wastewater Treatment centres. Key features of the project were:

  • Biological Nutrient Removal (to N5) upgrade of the Sandgate WWTP (25 ML per day) involving the brown field construction of two oxidation ditches, three clarifiers, dewatering system, disinfection system, creek outfall diffuser and control building ($54 million).
  • Biological Nutrient Removal (to N5) (70 ML per day) upgrade of the Oxley WWTP involving the brown field construction of an inlet works two oxidation ditches, five clarifiers, dewatering system, disinfection system and control building ($96 million).
  • Upgrade the existing Wacol Treatment plant to achieve a total Nitrogen of 5 mg per litre. 
  • Design and construct of the CAMBI thermo hydrolysis plant and hazardous area upgrade to the existing digesters ($25 million).
  • Design and Construct the new Wynnum Wastewater Treatment plant (9 ML/day) ($21 million).


Design and Construction of the new Wynnum MFRO plant to recycle water to Caltex ($32 million). All of the reporting and management systems were as per the BCAA project. Aquatec Maxcon was responsible for the process design, mechanical and control of the membrane treatment system. The Wynnum Project was completed in September 2007.

 

Horseshoe Bay WWTP

 
  

Client:

Citiwater, Business Unit of Townsville City Council

(Water Matters Alliance)

Location:

Horseshoe Bay, Magnetic Island

Service:

Greenfield site, re-use

Value:

-

Completion Date:

2006

After 3 ½ years of successful operation at Picnic Bay, Citiwater in conjunction with the Water Matters Alliance selected a Kubota MBR system as the preferred option for a new wastewater treatment plant at Horseshoe Bay to meet the stringent discharge requirements.


Solution
A MLE Process utilising a Kubota MBR system was installed to meet low nitrogen, phosphate and pathogen limits. Alum was dosed to meet the low Phosphate requirements.
Kubota membranes have a nominal pore size of 0.4µm and an absolute pore size of 0.01µm, which provides an absolute barrier to biomass, and pathogens retaining them within the process tank.

Process Overview
The raw water first passes through a 3mm fine screen into a bioreactor. The bioreactor consists of 3 stages – two denitrification tanks, followed by the MBR tank. Filtration is achieved by drawing effluent through the surface of the flat sheet membranes under a gravity head. No suction pumps are required.

The effluent from the plant is reused to irrigate a dry tropical forest parkland or discharged to the Great Barrier Reef Marine Park.

Cleveland Bay WWTP

Clevaland Bay 1 Thumb Cleveland Bay 2 Thumb Cleveland Bay 3 Thumb
 
  

Client:

Citiwater, Business Unit of Townsville City Council

(Water Matters Alliance)

Location:

Townsville, QLD

Service:

Wastewater treatment

Cleveland Bay which was part of the Water Matters Alliance in Townsville, included mechanical design, equipment and installation including switchboards, PLCs & SCADA and the Kubota flat sheet membranes for the membrane bioreactor at Horseshoe Bay. This plant has received many awards including the Excellence Award for a Major Water Project Greater than $5M and the Alliance Project Team Excellence Award. Also becoming finalists in the 2009 Australian Water Association – Water Environment Merit Award and the 2008 Australasian Alliancing Association Awards.

Delivery of the programme of works included:

  • Brownfield capacity and quality upgrade of Cleveland Bay WRP to 126,000 EP Biological Nutrient Removal (BNR);
  • Membrane Treatment system retrofitted into the existing clarifiers which we reconfigured to become bioreactors. The plant combines an oxidation ditch with membrane separation. A biosolids handling facility was undertaken also. Effluent from the plant can be treated in a future water reclamation facility which will include reverse osmosis to achieve reuse water suitable for industrial and irrigation applications. The efficient equipment selections have resulted in the operating costs being substantially below the initial projections with savings approaching $1m per annum.
  • The Cleveland Bay WTF was, at commissioning, the largest MBR in the Southern Hemisphere and one of the largest MBR plants in the world.
  • The scope also included an upgrade of the plants control, SCADA and telemetry systems by MPA Engineering.
  • Effluent Achieved: Total N (mg/l – 3.5); Total P (mg/l – 0.5) discharging to Great Barrier Reef Marine Park

Sandgate WWTP

Sandgate 3 Thumb Sandgate 2 Thumb Sandgate 1 Thumb

Client:

Brisbane Water (BWEA Alliance)

Location:

Sandgate, QLD

Service:

Wastewater treatment

Value:

AUD $130 M

Completion Date:

2006

The Sandgate WWTP is located on Paperbark Drive at Sandgate. It is bordered by residential properties on the northern side of Cabbage Tree Creek in the north Brisbane suburbs of Shorncliffe and Deagon. Sandgate WWTP upgrade was delivered as part of the Brisbane Water Enviro Alliance in which Aquatec Maxcon was a partner. The programme also included upgrades to Oxley Creek, Wynnum and Wacol WWTPs.

The plant discharges treated wastewater into Cabbage Tree Creek. The upgrade to the Sandgate WWTP involved heavily brown fields replacement of out-dated infrastructure and mechanical equipment with new state of the art technology. These works have improved treatment quality, increased plant capacity, reduced odour and improved the quality of water in Cabbage Tree Creek.

Features of the upgrade included:

  • Increased capacity from 18mega litres per day to 25 megalitres per day, servicing an ultimate population of 110,000 persons;
  • Nitrogen reduced from 30 milligrams per litre to less than 5 milligrams per litre;
  • Odour mitigation works between December 2004 and March 2005;
  • Replacement of existing trickling filters with bioreactors to improve nitrogen and phosphorus removal using fine bubble aeration oxidation ditch process;
  • New final settling tanks;
  • New sludge dewatering and handling facilities;
  • Installation of ultra violet (UV) disinfection equipment to replace existing chlorine disinfection;
  • Decommissioning of primary settling tanks and digesters;
  • Upgrade fully constructed inside plant fence line; and
  • Effluent quality achieved.

Somerset Dam Package WTP

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