Gold Coast Desalination Plant: Difference between revisions

Revision as of 23:40, 14 November 2014

Desal Plant Profile - Gold Coast Desalination Plant
Labelled aerial photo of Gold Coast Desalination Plant

Total capacity:	133 ML/day
Date commissioned:	February 2009
Feed water TDS:	34000 mg/L - 39000 mg/L ^[1]
Product water TDS:	140mg/L ^[2]
Percent of water supply:	27% of South Eastern QLD
feed water temperature (low):	17°C
Feed water temperature (high):	28°C
Seawater intake system:	Submerged open sea
Pretreatment system:	Ferric sulphate coagulation, sulphuric acid injection (pH reduction), polyDADMAC, dual media pressure filters
RO operating pressure:	First pass RO operating pressure - 64 bar (45% recovery). Second pass - 15 bar (85% recovery) ^[3]
RO passes:	2 ^[3]
RO trains:	9, 3
Post-treatment system:	Lime stabilization, CO2, disinfection by sodium hypochlorite injection
Concentrate disposal:	Treated supernatant discharged to sea, solids centrifuged and landfilled
Energy consumption:	3.58 kWh/m3
Energy recovery:	Each RO train is fitted with dual-work exchanger energy recovery devices, which recover up to 97% of unused energy from the brine. Renewable energy certificates are being used to fully offset carbon emissions from the plant.
Capital cost:	$1200 million
Useful links:	http://www.water-technology.net/projects/gold-coast-plant/

Physical & Chemical Properties
Turbidity:	7 NTU

Cations

Anions

↑ Billiton, BHP. Appendix H3: Comparisons With Other Desalination Plants Olympic Dams Supplementary EIS (pp. 2-5). [1] Accessed November 6th, 2014.
↑ Crisp, G. J. (2010). Desalination in Australia. Paper presented at the OC Water Summit, Grand Californian Hotel, Disneyland Resort. [2] Accessed November 6th, 2014.
↑ ^3.0 ^3.1 Bellizia, G. (2008). GOLD COAST DESALINATION PROJECT. Paper presented at the 33rd Annual Qld Water Industry Operations Workshop, Indoor Sports Centre, Carrara, Gold Coast. [3] Accessed November 6th, 2014

@@ Line 16: / Line 16: @@
    | post-treatment system = [[Has Post-Treatment System Configuration::Lime stabilization, CO2, disinfection by sodium hypochlorite injection]]
    | concentrate disposal = [[Has Concentrate Disposal::Treated supernatant discharged to sea, solids centrifuged and landfilled]]
-   | energy consumption = [[Has Energy Consumption::3 kWh/m3]]
+   | energy consumption = [[Has Energy Consumption::3.58 kWh/m3]]
    | energy recovery = [[Has Energy Recovery::Each RO train is fitted with dual-work exchanger energy recovery devices, which recover up to 97% of unused energy from the brine. Renewable energy certificates are being used to fully offset carbon emissions from the plant.]]
    | capital cost = [[Has Capital Cost::$1200 million]]