Biological Phosphorous Removal An Operators Guide Glenn Burkhardt, - - PowerPoint PPT Presentation

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Biological Phosphorous Removal An Operators Guide Glenn Burkhardt, - - PowerPoint PPT Presentation

Biological Phosphorous Removal An Operators Guide Glenn Burkhardt, PE Engineered Logic LLC What is Bio P Removal? It is NOT a mysterious brown box Bio P Model Two Step Process (Anaerobic then Aerobic) Acetate + Poly- P PHA + ATP


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SLIDE 1

Biological Phosphorous Removal An Operator’s Guide

Glenn Burkhardt, PE Engineered Logic LLC

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SLIDE 2

What is Bio P Removal?

  • It is NOT a mysterious brown box
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SLIDE 3

Bio P Model

  • Two Step Process (Anaerobic then Aerobic)

Acetate + Poly-P → PHA + ATP → H20 + CO2 ← Anaerobic → ← Aerobic →

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SLIDE 4

Bio P Process Discussion

  • Anaerobic Step
  • Carbon Conversion to Volatile Fatty Acids
  • Volatile Fatty Acid Conversion to Acetate
  • Acetate & Poly-P Conversion to PHA & ATP

PHA Polyhydroxyalkanoic Acid ATP Adenosine Triphosphate

  • Aerobic Step
  • PHA & ATP Conversion to Glycogen, H2O & CO2
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SLIDE 5

Phosphorous Uptake Diagram

Anaerobic→← Aerobic

10 20 30 40 50 60 25 50 75 100 150 200 300

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SLIDE 6

Treatment Process Diagram

  • A/O Process
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SLIDE 7

Anoxic Zone

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SLIDE 8

Aerobic Zone

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SLIDE 9

Important Design Parameters

  • BOD to P ratio > 20
  • COD to P ratio > 45
  • VFA to P ratio > 7
  • Anaerobic HRT 1 to 2 hours
  • Aerobic SRT 15 to 20 days
  • Nitrate Loading < O2 Demand of Waste
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SLIDE 10

Important Operating Parameters

  • Anaerobic Zone pH 8.0 to 8.5
  • Anaerobic Zone ORP -100 to -200 mV
  • Aerobic Zone pH 7.0 to 7.5
  • Aerobic Zone ORP +100 to +300 mV
  • Return Sludge Rate Manage ML Conc.

Maintain ORP Limits

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SLIDE 11

pH and ORP Monitoring

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SLIDE 12

Bio P Troubleshooting

  • Phosphorous Increasing (normal NH3 & SS)
  • P uptake could be due to low VFA production
  • ATP production could be affected by anaerobic pH
  • Nitrates could be affecting anaerobic conditions
  • Parameters to Check
  • VFA to P ratio (greater than 7)
  • Anaerobic reactor pH (8.0 to 8.5)
  • Anaerobic reactor ORP (-100 to -200 mV)
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SLIDE 13

Bio P Troubleshooting

  • Rapid P Increase (normal NH3 & SS)
  • Side Stream with High P Being Introduced
  • P Release from Clarifier Sludge Blanket
  • P Release from High Solids Retention time
  • Parameters to Check
  • P Concentration to Anaerobic Reactor
  • ORP of Sludge Blanket ( 0 to 100 mV is the goal )
  • Soluble P of Mixed Liquor ( < 0.5 mg/l is the goal )
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SLIDE 14

Bio P Troubleshooting

  • High Effluent P ( high effluent SS)
  • Could be due to High Effluent Solids
  • Could be due to P Release
  • Could be due to Aerobic Reactor pH
  • Parameters to Check
  • Check P of Filtered Effluent Sample
  • Check P Profile of Anaerobic and Aerobic Reactors
  • Check pH of Anaerobic and Aerobic Reactors
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SLIDE 15

Bio P Performance

  • Improved Solids Settling Characteristics
  • Less Risk of Aerobic Reactor Foaming
  • More Stable Under Shock Loading Conditions
  • No Chemicals Required
  • Less Sludge Production
  • Effluent P Typically 0.2 to 0.5 mg/l
  • Effluent NH3 Typically < 0.5 mg/l
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SLIDE 16

Questions?

Glenn Burkhardt, PE Engineered Logic LLC