Schwing Bioset, Inc Waste water Sedimentation inlet Pre treatment Primary Aeration Tank Secondary...
Transcript of Schwing Bioset, Inc Waste water Sedimentation inlet Pre treatment Primary Aeration Tank Secondary...
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Waste water inlet
Pre treatment
Primary Sedimentation
AerationTank
SecondarySedimentation
Post treatment
Sludge Thickener
Digester Biogas tank Cogen
Sludge Dewatering
Integrated Phosphate Management
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1. Phosphorus return load
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2. Pipe clogging / scaling issues
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3. Struvite grit accumulation
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4. Dewatering issues Bio-P
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5. Stabilizing Bio-P process
What are the Issues:
Case Specific Issues = Case Specific Approach
6. Increased sludge with iron salt
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Plant Issues: Mechanical:
Clogged pipes & damaged equipment Accumulations in tanks
Regulatory: Reduced Phosphorous effluent limits
Process: Poor dewatering characteristics resulting from biological
phosphourus removal process
Integrated Phosphate Management
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Plant Opportunity: Struvite can be recovered by precipitating into prills High value fertilizer product with opportunity to market Improve dewaterbaility of biosolids Global steward of phosphate management
Integrated Phosphate Management
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Struvite recovery is a two stage process: Air Stripping Crystallization
Two stages allow for: Greater process control Stabilize operations by limiting variables to
control in each vessel Design flexibility to solve more/specific plant
issues Process can be applied to Digestate streams,
Filtrate streams or combination of both
Integrated Phosphate Management
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Features: Concentrations reduced to ~15 - 20 ppm PO4-P regardless of starting
concentrations on centrate applications Reduced to ~40 ppm on digestate applications
Integrated Phosphate Management
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Current Installations since 2006 5 Municipal installations (4 operating, 1 PO received) 5 Industrial installations
Municipal Installation List: Apeldoorn, Netherlands (Hybrid Solution) Aaenmaas Beijersbos, Belgium (Centrate Solution) Aquafin Aartselaar, Belgium (Digestate Solution) Nieuwegein, Netherlands (Digestate Solution) Braunschweig, Germany (Centrate Solution)
Integrated Phosphate Management
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Three primary configurations:1. Digestate
Improved dewatering due to residual MgEliminate scalingHarvest up to 50% of produced struviteTanks twice the size as operating on CentrateReduce PO4-P levels to 40-50 ppm regardless of starting concentration
Integrated Phosphate Management
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Three primary configurations:2. Centrate
Harvest up to 90% of produced struviteAir Stripper & Crystallizer tanks half the size as operating on digestateDoes not help with dewatering performanceDoes not help with scaling controlReduce PO4-P levels to 15-20 ppm regardless of starting concentration
Integrated Phosphate Management
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Three primary configurations:3. Hybrid
Harvest up to 90% of struvite produced in CrystallizerCrystallizer tank half the size as operating on digestatePrevents scalingDoes not help with dewatering performanceReduce PO4-P levels to 15-20 ppm regardless of starting concentration
Integrated Phosphate Management
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Air Stripper
Struvite recovery is a two stage process:
Stage 1: Stripping Reactor Blow air to remove CO2
Raises pH to 7.5 – 8.0 pH acts like an accelerator in a car
Higher pH = faster reactiono Smaller prills
Lower pH = slower reactiono Larger prills
Integrated Phosphate Management
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MgCl2
Crystallizer
Truck Load
Stage 2: Crystallization & Settling Reactor Magnesium Chloride is added (MgCl2) Mg reacts with P and N Pure struvite crystals are formed Crystals are recycled to grow like pearl Prills can be harvested and then:
Washed Optionally dried Bagged or truck loaded Settler
Integrated Phosphate Management
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ApeldoornHybrid
1. Digester
2. Equalization tank
3. Stripping reactor
4. Pumps
5. Blowers
6. Odor control (not necessary – can use plant odor control)
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Redundant pumps to transfer settled solids to dewatering. This struvite is not recovered and comes out of plant in dewatered biosolids
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ApeldoornHybrid
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Redundant blowers to pump air through diffusers within stripping tank.
Air “strips off” the CO2 and results in a pH increase to 7.5 –8.0
In this pH range the magnesium that is present in the sludge will react and form struvite crystals
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ApeldoornHybrid
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1. MgCl2 storage tank
2. Primary crystallization reactor
3. Settling tank
4. Buffer tank to ensure optimum flow to hydrocyclones (area #6) (only used when high recovery rates required)
5. Finished product truck loadout from area #6
6. Additional process equipment indoors
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ApeldoornHybrid
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AaenmaasCentrate
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1. Air Stripper
2. Crystallization Reactors
3. MgCl2 tank
4. MgCl2 metering (wall mounted)
5. Blower
6. Product wash
7. Product loading
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AaenmaasCentrate
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1. Air Stripper2. Reaction Tank3. Settling Tank4. Agitator – no bearing in liquid 5. Hydrocyclone
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AaenmaasCentrate
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View from below1. Air Stripper2. Reaction Tank3. Recycle
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AaenmaasCentrate
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MgCl2 dosing system1. Mg tank2. Parallel metering
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AaenmaasCentrate
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Blower for Air Stripper
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AaenmaasCentrate
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Finished productBottom of washerProcess pumps
AaenmaasCentrate
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Finished product to storage Transport in
Classifying screw
Washing zone
AaenmaasCentrate
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Typical grit washer
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AaenmaasCentrate
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5 GPM digestate mode10 GPM Centrate modeCan harvest produced struviteCon operate in conjunction with screw press
Struvite Recovery