Aeration Basics the Bugs Eye View Leonard E. Ripley, Ph.D., P.E., - - PowerPoint PPT Presentation

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Aeration Basics the Bugs Eye View Leonard E. Ripley, Ph.D., P.E., - - PowerPoint PPT Presentation

Aeration Basics the Bugs Eye View Leonard E. Ripley, Ph.D., P.E., BCEE Senior Environmental Engineer Freese and Nichols, Inc. WEAT Electrical & Instrumentation Seminar March 20, 2019 Why Do We Aerate? Supply process oxygen: 1.


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SLIDE 1

Aeration Basics – the Bug’s Eye View

Leonard E. Ripley, Ph.D., P.E., BCEE

Senior Environmental Engineer

Freese and Nichols, Inc.

WEAT Electrical & Instrumentation Seminar March 20, 2019

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SLIDE 2

Why Do We Aerate?

  • Supply process oxygen:
  • 1. Oxidation of organics (BOD)
  • 2. Endogenous respiration
  • Suspend mixed liquor solids
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SLIDE 3

Biochemical Oxygen Demand (“BOD”)

BOD has two components:

  • 1. Carbonaceous BOD (“CBOD”) is oxygen required for oxidation of carbon:

CxHyOz + O2 → CO2 + H2O Carried out by heterotrophic bacteria … relatively rapid process

  • 2. Nitrogenous BOD is oxygen required for oxidation of ammonia to nitrate:

NH3 + O2 → NO2 + O2 → NO3 + H2O Carried out by “nitrifiers” … slow growing, relatively sensitive bacteria

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SLIDE 4

Endogenous Respiration

Without wastewater organics for food:

  • Bacteria coast and respire “endogenously” (resting rate)
  • Bacteria eventually die, rupture (lysis), and provide food for

their relatives

  • This is the main process in aerobic digestion, but it also is

important in aeration basins, especially if they are

  • rganically underloaded
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SLIDE 5

TCEQ Chapter 217 Design Criteria for DO

Oxygen Requirements (O2R) of wastewater: An aeration system must be designed to provide a minimum dissolved oxygen concentration in the aeration basin of 2.0 milligrams per liter (mg/L). Note: This is at the max design loading in the future.

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SLIDE 6

Mixing

Keep mixed liquor solids in suspension:

Air flow rate must be

  • > 20 scfm/1000 cu ft for course bubble diffusers,
  • > 0.12 scfm/sq ft for fine bubble diffusers

Mechanical mixing must provide

  • > 0.75 hp/1000 cu ft

Swing zone can be aerated or just mixed

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SLIDE 7

How Much Oxygen is Necessary?

Depends mainly on:

  • Wastewater flow rate, cBOD & ammonia concentrations

→ organic loading rates

Other factors:

  • Characteristics of BOD: degrades readily or slowly?
  • Solids retention time (sludge age)
  • Basin configuration -- selectors?
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SLIDE 8

Why Aeration is Expensive

Example: with 33% O2 transfer efficiency:

  • 1 lb O2 transferred requires 3 lb O2 applied
  • 3 lb O2 applied carries 11 lb nitrogen
  • Total air required to transfer 1 lb O2 = 14 lb
  • 1. Even highly efficient aeration is not very efficient in

actually transferring oxygen into solution.

  • 2. Besides pushing oxygen into the aeration basin, we also

have to pressurize the accompanying nitrogen.

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SLIDE 9

How Much Air is Necessary?

  • Depends mainly on:
  • Wastewater flow rate, BOD & ammonia concentraGons → loadings
  • Other factors:
  • Characteristics of BOD: readily or slowly degradable
  • Solids retention time (sludge age)
  • Transfer efficiency of diffusers
  • DO concentrations
  • Wastewater temperature
  • Presence of surfactants and/or grease
  • Basin configuration (selectors?) and AB volume
  • Air temperature and humidity

WHAT CAN YOU CONTROL?

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SLIDE 10

Aeration Control Overview (simplified)

FLOW RATE (MGD) BOD & NH3 (mg/L) OXYGEN UPTAKE RATE (mg/L-hr) O2 TRANSFER EFFICIENCY (%) OXYGEN REQUIRED (lbs/hr) AIR SUPPLIED (scfm) DISSOLVED OXYGEN (mg/L) If supplied > required DO ↑ If supplied < required DO ↓

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SLIDE 11

Aeration Control Overview (simplified)

AIR SUPPLIED (scfm) FLOW RATE (MGD) BOD & NH3 (mg/L) OXYGEN UPTAKE RATE (mg/L-hr) OXYGEN REQUIRED (lbs/hr) ? ? ? DISSOLVED OXYGEN (mg/L) O2 TRANSFER EFFICIENCY (%) Is DO increasing or decreasing?

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SLIDE 12

Possible Game-Changing Technology

FLOW RATE (MGD) BOD & NH3 (mg/L) OXYGEN UPTAKE RATE (mg/L-hr) O2 TRANSFER EFFICIENCY (%)

Floating hood collects off-gas and analyzes residual O2 and CO2

  • content. Calculates:
  • Oxygen Uptake Rate (OUR)
  • Oxygen Transfer Efficiency

Expensive … no units in Texas at this time.

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SLIDE 13

Example AB Oxygen Uptake Patterns

(Dallas Water Utilities Central Plant – B Complex)

10 20 30 40 50 60 70 80 25 50 75 100 Oxygen Uptake Rate (mg/L-hr) Influent ← Basin PosiGon (%) → Effluent BOD & Ammonia Oxidation Endogenous Respiration (Digestion)

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More Typical AB Oxygen Uptake Pattern

10 20 30 40 50 60 70 80 25 50 75 100 Oxygen Uptake Rate (mg/L-hr) ← Basin PosiGon (%) → BOD & Ammonia Oxidation Endogenous Respiration (Digestion) Much higher demand at front of basin.

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SLIDE 15

Tapered Aeration

Install diffusers in zones to match

  • xygen uptake

pattern – higher density at influent end of basin.

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Example Air Flow Distribution: Leon Creek

1,008 605 403 2,058 1,235 823

500 1,000 1,500 2,000 2,500 A B C Air Flow Rate (scfm) Aeration Basin Zone Annual Average Max Month Peak Load

50% 30% 20%

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SLIDE 17

Leon Creek Minimum Air Flow Rates

500 1,000 1,500 2,000 2,500 A B C Air Flow Rate (scfm) Aeration Basin Zone Annual Average Max Month Peak Load

435 361 361

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SLIDE 18

Non-Aeration: Anoxic and Anaerobic Zones

“Anoxic” – with very little, if any, oxygen present. Heterotrophic bacteria substitute nitrate for oxygen in degrading BOD ... Can reduce aeration by 15-20%. “Anaerobic” – with no oxygen and no nitrate present. Phosphorus Accumulating Bacteria (PAO’s) release phosphorus, then take up extra phosphorus in the aerobic zone … biological phosphorus removal.

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SLIDE 19

Anoxic/Anaerobic Zones for BNR

Anaerobic Anoxic RAW INFLUENT CLARIFIER Aerobic Nitrified Recycle Return Activated Sludge

8 8 PAO’s release phosphorus Denitrifiers use nitrate to replace oxygen

N2 Gas

Heterotrophs oxidize BOD, nitrifiers oxidize ammonia, PAO’s uptake phosphorus

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Anoxic/Anaerobic (BNR) Effects on Aeration

  • Can reduce oxygen, and aeration, demand by 15-20%.
  • Recycle will even out uptake rate along length of basin.
  • Important to minimize returning dissolved oxygen to an

anoxic zone.

  • Critically important to avoid returning dissolved oxygen to

an anaerobic zone.

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The “Perfect” Aeration Strategy?

Supply just enough air to meet process requirements – no air “wasted” on mixing. Supply enough air to meet process requirements by mid-basin, use last zone(s) as a safety cushion.

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Final (Process) Thoughts …

  • 1. Every plant has large aeration fluctuations – hourly, daily, seasonally –

you’ll never reach “perfection”.

  • 2. Compliance is priority #1, even if you have to waste some air.
  • 3. Be diligent about monitoring/maintaining the DO probes.
  • 4. Make aeration changes gradually.
  • 5. Turndown may require taking AB’s out of service.
  • 6. DO control may be more important for BNR than for saving energy.
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SLIDE 23

Thank You!

Questions / comments: Leonard E. Ripley, Ph.D., P.E. BCEE Freese and Nichols, Inc. LER@Freese.com