Difference between revisions of "Gold Coast Desalination Plant"
From Desal Wiki
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===References=== | ===References=== | ||
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<ref name="billiton">Billiton, BHP. Appendix H3: Comparisons With Other Desalination Plants Olympic Dams Supplementary EIS (pp. 2-5). http://www.bhpbilliton.com/home/society/regulatory/Documents/Olympic%20Dam%20Supplementary%20EIS/Appendices/Appendix%20H3_Comparisons%20with%20other%20Desalination%20Plants.pdf Accessed November 6th, 2014.</ref> | <ref name="billiton">Billiton, BHP. Appendix H3: Comparisons With Other Desalination Plants Olympic Dams Supplementary EIS (pp. 2-5). http://www.bhpbilliton.com/home/society/regulatory/Documents/Olympic%20Dam%20Supplementary%20EIS/Appendices/Appendix%20H3_Comparisons%20with%20other%20Desalination%20Plants.pdf Accessed November 6th, 2014.</ref> | ||
<ref name="crisp">Crisp, G. J. (2010). Desalination in Australia. Paper presented at the OC Water Summit, Grand Californian Hotel, Disneyland Resort. http://www.mwdoc.com/OCWaterSummit/Presentations/GHD%20Ocean%20Desalination.pdf Accessed November 6th, 2014.</ref> | <ref name="crisp">Crisp, G. J. (2010). Desalination in Australia. Paper presented at the OC Water Summit, Grand Californian Hotel, Disneyland Resort. http://www.mwdoc.com/OCWaterSummit/Presentations/GHD%20Ocean%20Desalination.pdf Accessed November 6th, 2014.</ref> | ||
| + | <ref name="bellizia">Bellizia, G. (2008). GOLD COAST DESALINATION PROJECT. Paper presented at the 33rd Annual Qld Water Industry Operations Workshop, Indoor Sports Centre, Carrara, Gold Coast. http://www.wioa.org.au/conference_papers/08_Qld/documents/GeorgeBellizia_000.pdf Accessed November 6th, 2014</ref> | ||
</references> | </references> | ||
Revision as of 05:20, 13 November 2014
| Desal Plant Profile - Gold Coast Desalination Plant | |
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 Labelled aerial photo of Gold Coast Desalination Plant
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| Total capacity: | 133ML/day |
| Date commissioned: | February 2009 |
| Percent of water supply: | 27% of South Eastern QLD |
| feed water temperature (low): | 17°C290.15 K 62.6 °F 522.27 °R |
| Feed water temperature (high): | 28°C301.15 K 82.4 °F 542.07 °R |
| 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) [1] |
| RO passes: | 2 [1] |
| 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/ |
Interactive process flow diagram
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Water quality data
| Physical & Chemical Properties | |
|---|---|
| Turbidity: | 7 NTU |
| Cations |
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| Anions |
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References
- ↑ 1.0 1.1 Bellizia, G. (2008). GOLD COAST DESALINATION PROJECT. Paper presented at the 33rd Annual Qld Water Industry Operations Workshop, Indoor Sports Centre, Carrara, Gold Coast. http://www.wioa.org.au/conference_papers/08_Qld/documents/GeorgeBellizia_000.pdf Accessed November 6th, 2014
Cite error: <ref> tag with name "billiton" defined in <references> is not used in prior text.
Cite error: <ref> tag with name "crisp" defined in <references> is not used in prior text.