Perth Seawater Desalination Plant: Difference between revisions
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| product water tds = [[Has Product Water TDS::30mg/L]] (before remineralising) | | product water tds = [[Has Product Water TDS::30mg/L]] (before remineralising) | ||
| percent of water supply = 17% of Perth | | percent of water supply = 17% of Perth | ||
| feed water temperature (low) = [[Has Feed Water Temp - Low:: | | feed water temperature (low) = [[Has Feed Water Temp - Low::14°C]] | ||
| feed water temperature (high) = [[Has Feed Water Temp - High:: | | feed water temperature (high) = [[Has Feed Water Temp - High::26°C]] | ||
| seawater intake system = [[Has Seawater Intake System::Submerged open sea]] | | seawater intake system = [[Has Seawater Intake System::Submerged open sea]] | ||
| pretreatment system = [[Has Pretreatment System Configuration::Ferric sulphate coagulation, acid, dual media pressure filters]] | | pretreatment system = [[Has Pretreatment System Configuration::Ferric sulphate coagulation, acid, dual media pressure filters]] | ||
Revision as of 23:32, 29 September 2014
| Desal Plant Profile - Perth Seawater Desalination Plant | |
|---|---|
 Aerial photo of Perth Seawater Desalination Plant
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| Date commissioned: | February 2007 |
| Percent of water supply: | 17% of Perth |
| feed water temperature (low): | 14°C |
| Feed water temperature (high): | 26°C |
| Seawater intake system: | Submerged open sea |
| Pretreatment system: | Ferric sulphate coagulation, acid, dual media pressure filters |
| RO operating pressure: | 60 bar |
| RO passes: | 2 |
| Post-treatment system: | Lime stabilization, CO2 |
| Concentrate disposal: | Treated supernatant discharged to sea, solids centrifuged and landfilled |
| Energy consumption: | 4.0 kWh/m3 |
| Energy recovery: | Pressure exchanger |
| Capital cost: | $347 million |
| Useful links: | http://www.water-technology.net/projects/perth/ |
