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Estimates of Timeline for Peak in Phosphorus Production
Quantity of Phosphorous in sewage ,[object Object],[object Object],[object Object]
Value of Phosphorous in sewage ,[object Object],[object Object]
Value of Phosphorous in sludge
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[object Object],[object Object],[object Object]
Aqua Critox® ,[object Object],[object Object]
sludge is reduced to inert solid residue
Aqua Critox ® SEPARATOR BOILER WATER FEED PUMP STEAM SLUDGE FEED COOLER PRESSURE REDUCTION REACTOR HIGH PRESSURE PUMP HEATER ECONOMISER OXYGEN CO 2 ,N 2 ,0 2 Treated sludge STEAM GENERATOR GRINDER PUMP THICKENER CLEAN WATER RECYCLING PROCESS INERT RESIDUE Coagulant Phosphate
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Scenario A: P Mass Balance – Bio-P with AD (500K PE ) 1,125 kg/d DAFT Bio P  Removal  Secondary  Clarifiers Filters Primary  Clarifiers UV Digesters Centrifuge 112 kg/d  Treated Wastewater 1,013 kg/d 750 kg/d 638 kg/d  Waste Sludge 375 kg/d – Return P Load
Scenario B: Mass balance –  Bio P with  Aqua Critox®  (500K PE) 530kg/d Recovered  P from the recovery step. DAFT Bio P  Removal Secondary  Clarifiers Filters Primary  Clarifiers UV Aquacritox Ash 805 kg/d 115 kg/d  Treated Wastewater 690 kg/d 750 kg/d  585 kg/d 55 kg/d – Return P Load Supernatant 105 kg/d
Aqua Critox ® ,[object Object],[object Object]
Aqua Critox ® ,[object Object],[object Object],[object Object]
Aqua Critox ® ,[object Object],[object Object],[object Object],[object Object],[object Object]
For more information ,[object Object],[object Object],[object Object]

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Phosphorous Recovery From Sewage Sludge Using Aqua Critox Super Critical Water Oxidation

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  • 3. Estimates of Timeline for Peak in Phosphorus Production
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  • 10. sludge is reduced to inert solid residue
  • 11. Aqua Critox ® SEPARATOR BOILER WATER FEED PUMP STEAM SLUDGE FEED COOLER PRESSURE REDUCTION REACTOR HIGH PRESSURE PUMP HEATER ECONOMISER OXYGEN CO 2 ,N 2 ,0 2 Treated sludge STEAM GENERATOR GRINDER PUMP THICKENER CLEAN WATER RECYCLING PROCESS INERT RESIDUE Coagulant Phosphate
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  • 13. Scenario A: P Mass Balance – Bio-P with AD (500K PE ) 1,125 kg/d DAFT Bio P Removal Secondary Clarifiers Filters Primary Clarifiers UV Digesters Centrifuge 112 kg/d Treated Wastewater 1,013 kg/d 750 kg/d 638 kg/d Waste Sludge 375 kg/d – Return P Load
  • 14. Scenario B: Mass balance – Bio P with Aqua Critox® (500K PE) 530kg/d Recovered P from the recovery step. DAFT Bio P Removal Secondary Clarifiers Filters Primary Clarifiers UV Aquacritox Ash 805 kg/d 115 kg/d Treated Wastewater 690 kg/d 750 kg/d 585 kg/d 55 kg/d – Return P Load Supernatant 105 kg/d
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