Difference between revisions of "Gold Coast Desalination Plant"
From Desal Wiki
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| caption = Labelled aerial photo of {{PAGENAME}} | | caption = Labelled aerial photo of {{PAGENAME}} | ||
| total capacity (max) = 133ML/day | | total capacity (max) = 133ML/day | ||
− | | date commissioned = February 2009 | + | | date commissioned = February 2009 <ref name="billiton" /> |
− | | feed water tds = [[Has Feed Water TDS low::34,000 mg/L]] - [[Has Feed Water TDS high::39,000 mg/L]] | + | | feed water tds = [[Has Feed Water TDS low::34,000 mg/L]] - [[Has Feed Water TDS high::39,000 mg/L]] |
| product water tds = [[Has Product Water TDS::140mg/L]] <ref name="crisp" /> | | product water tds = [[Has Product Water TDS::140mg/L]] <ref name="crisp" /> | ||
| percent of water supply = 27% of South Eastern QLD | | percent of water supply = 27% of South Eastern QLD |
Revision as of 05:49, 13 November 2014
Desal Plant Profile - Gold Coast Desalination Plant | |
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Labelled aerial photo of Gold Coast Desalination Plant | |
Total capacity: | 133ML/day |
Date commissioned: | February 2009 [1] |
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) [2] |
RO passes: | 2 [2] |
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 | |
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Turbidity: | 7 NTU |
Cations |
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Anions |
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References
- ↑ 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.
- ↑ 2.0 2.1 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>
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is not used in prior text.