Perth Seawater Desalination Plant: Difference between revisions
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{{Infobox - Desal Plant Profile | |||
| image_name = aerial_shot_perth_seawater_desal_plant.png | |||
| caption = Aerial photo of {{PAGENAME}} | |||
| total capacity (max) = | |||
| date commissioned = February 2007 | |||
| feed water tds = [[Has Feed Water TDS::36,500 mg/L]] | |||
| product water tds = [[Has Product Water TDS::30mg/L]] (before remineralising) | |||
| percent of water supply = 17% of Perth | |||
| feed water temperature (low) = [[Has Feed Water Temp - Low::14 degreesC]] | |||
| feed water temperature (high) = [[Has Feed Water Temp - High::26 degreesC]] | |||
| seawater intake system = [[Has Seawater Intake System::Submerged open sea]] | |||
| pretreatment system = [[Has Pretreatment System Configuration::Ferric sulphate coagulation, acid, dual media pressure filters]] | |||
| RO operating pressure = [[Has RO Operating Pressure::60 bar]] | |||
| RO passes = [[Has Number of RO Passes::2]] | |||
| RO passes = 2 | |||
| post-treatment system = [[Has Post-Treatment System Configuration::Lime stabilization, CO2]] | |||
| concentrate disposal = [[Has Concentrate Disposal::Treated supernatant discharged to sea, solids centrifuged and landfilled]] | |||
| energy consumption = [[Has Energy Consumption::4.0 kWh/m3]] | |||
| energy recovery = [[Has Energy Recovery::Pressure exchanger]] | |||
| capital cost = [[Has Capital Cost::$347 million]] | |||
| total water cost = | |||
| useful link A = [http://www.water-technology.net/projects/perth/] | |||
}} | |||
<!-- End Infobox template table --> | |||
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Image:Perth_desal_processflowdiagram.png|800px | Image:Perth_desal_processflowdiagram.png|800px | ||
Revision as of 02:05, 10 September 2014
| Desal Plant Profile - Perth Seawater Desalination Plant | |
|---|---|
 Aerial photo of Perth Seawater Desalination Plant
| |
| Date commissioned: | February 2007 |
| Percent of water supply: | 17% of Perth |
| feed water temperature (low): | 14 degreesC |
| Feed water temperature (high): | 26 degreesC |
| 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: | [1] |
