Aeration Design
Calculate oxygen transfer, diffuser selection, and blower sizing for wastewater treatment systems.
SOTR/AOTR
Conversion
Diffuser Types
3 Types
Energy Analysis
kWh/kg O2
Cost Estimate
CAPEX/OPEX
Aeration System Design
Design diffuser system, blower sizing, and oxygen transfer calculations.
Quick Power Estimate
Design Parameters
Tank Parameters
Oxygen Demand
Conditions
Oxygen Transfer Correction Factors
Diffuser Types Comparison
Fine Bubble
Activated sludge, deep tanks
Pros:
- High efficiency
- Low energy
- Good for deep tanks
Coarse Bubble
Mixing, equalization, pre-treatment
Pros:
- Low fouling
- Simple maintenance
- Good mixing
Mechanical Surface
Oxidation ditches, lagoons
Pros:
- No diffuser fouling
- Good for shallow basins
Key Design Factors
Alpha (α)
Wastewater correction factor
Beta (β)
Salinity correction factor
Theta (θ)
Temperature correction factor
Fouling Factor (F)
Diffuser performance decline
Key Formulas
Oxygen Requirement
+ 4.57 × Q × (TKNo - TKN) / 1000
- 2.86 × Q × (NOx) / 1000
SOTR from AOTR
× (1 / α) × (1 / θ^(T-20))
Size aeration systems: convert standard oxygen transfer (SOTR) to actual field conditions (AOTR), select fine/coarse-bubble diffusers, size blowers with redundancy, and estimate energy cost.
ออกแบบระบบเติมอากาศ: แปลงค่าการถ่ายเทออกซิเจนมาตรฐาน (SOTR) เป็นสภาวะจริง (AOTR), เลือก diffuser แบบฟองละเอียด/หยาบ, เลือกขนาด blower พร้อมสำรอง และประเมินต้นทุนพลังงาน
When to use
- Determining oxygen demand and blower capacity for an aeration basin
- Comparing fine- vs coarse-bubble diffuser efficiency and energy
- Sizing standby blowers for reliability
How to use
- 1Enter oxygen demand, basin depth, temperature and elevation.
- 2Choose diffuser type and α, β, F (fouling) factors.
- 3Read required SOTR, air flow, blower power and energy cost.
Key formulas
Field to standard transfer
AOTR = SOTR · [(β·C_s,T,H − C_L)/C_s,20] · 1.024^(T−20) · α · F
α = transfer factor; β = salinity/surface factor; F = fouling
Blower adiabatic power
P_w = (w·R·T₁)/(k₁·e) · [(p₂/p₁)^k₁ − 1]
k₁ = (k−1)/k, k≈1.395 for air; e = efficiency
AOTR derate
- SOTR
- 100 kg O₂/h
- α, β, F
- 0.50, 0.95, 0.90
- T, C_L
- 28 °C, 2.0 mg/L
AOTR ≈ 100 · (0.95·7.8 − 2.0)/9.08 · 1.024^8 · 0.50 · 0.90 ≈ 26 kg O₂/h
References
- • Metcalf & Eddy (2014), Wastewater Engineering, 5th ed., Ch. 5
- • ASCE/EWRI 2-06 — Standard Guidelines for In-Process Oxygen Transfer Testing
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