Southern Seawater Desalination Plant: Difference between revisions
From Desal Wiki
imported>WikiAdmin (Created page with "{{Infobox - Desal Plant Profile | image_name = Southern seawater desalination.jpg | caption = Labelled aerial photo of {{PAGENAME}} | total capacity (max) = Has Max Ca...") |
imported>WikiAdmin No edit summary |
||
| Line 11: | Line 11: | ||
| seawater intake system = [[Has Seawater Intake System::Open Intake]] | | seawater intake system = [[Has Seawater Intake System::Open Intake]] | ||
| pretreatment system = [[Has Pretreatment System Configuration::Travelling Band Screens, UF PVDF Pressure Filters, 5 Micron Cartridge Filtration]] | | pretreatment system = [[Has Pretreatment System Configuration::Travelling Band Screens, UF PVDF Pressure Filters, 5 Micron Cartridge Filtration]] | ||
| RO operating pressure = First pass RO operating pressure - [[Has RO Operating Pressure First Pass::64 bar]] ([[Has Recovery First Pass::45%]] recovery). Second pass - [[Has RO Operating Pressure Second Pass::15 bar]] ([[Has Recovery Second Pass::85%]] recovery) | | RO operating pressure = First pass RO operating pressure - [[Has RO Operating Pressure First Pass::64 bar]] ([[Has Recovery First Pass::45%]] recovery). Second pass - [[Has RO Operating Pressure Second Pass::15 bar]] ([[Has Recovery Second Pass::85%]] recovery) | ||
| RO passes = [[Has Number of RO Passes::2]] | | RO passes = [[Has Number of RO Passes::2]] | ||
| RO trains = 8 first pass trains, 4 second pass trains | | RO trains = 8 first pass trains, 4 second pass trains | ||
| post-treatment system = [[Has Post-Treatment System Configuration::Lime stabilization, CO2]] | | post-treatment system = [[Has Post-Treatment System Configuration::Lime stabilization, CO2]] | ||
Revision as of 23:14, 11 February 2015
| Desal Plant Profile - Southern Seawater Desalination Plant | |
|---|---|
 Labelled aerial photo of Southern Seawater Desalination Plant
| |
| Total capacity: | 273 ML/day |
| Date commissioned: | 2011 (Stage 1); 2013 (Stage 2) |
| Feed water TDS: | 35000 mg/L - 38000 mg/L |
| Product water TDS: | 200mg/L |
| Percent of water supply: | 31% of Perth |
| feed water temperature (low): | 15°C |
| Feed water temperature (high): | 24°C |
| Seawater intake system: | Open Intake |
| Pretreatment system: | Travelling Band Screens, UF PVDF Pressure Filters, 5 Micron Cartridge Filtration |
| RO operating pressure: | First pass RO operating pressure - 64 bar (45% recovery). Second pass - 15 bar (85% recovery) |
| RO passes: | 2 |
| RO trains: | 8 first pass trains, 4 second pass trains |
| Post-treatment system: | Lime stabilization, CO2 |
| Concentrate disposal: | Brine diluted and discharged into the ocean |
| Energy consumption: | 3.6 kWh/m3 |
| Energy recovery: | Pressure exchanger |
| Capital cost: | $1150 million (Stage 1: $700 million. Stage 2: $450million) |
Interactive process flow diagram
Water quality data
| Physical & Chemical Properties | |
|---|---|
| Turbidity: | 7 NTU |
| Cations |
|---|
| Anions |
|---|
