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Oxygen Requirement & Aeration Calculator

Calculate total oxygen demand, air flow requirements, and blower sizing for biological wastewater treatment systems. Accounts for BOD removal, nitrification, alpha factor, and diffuser efficiency.

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Oxygen Requirement & Aeration Calculator

Enter your process parameters below to calculate design values. All calculations follow industry-standard methodologies.

m³/day
mg/L
mg/L
mg/L (0 if not nitrifying)
mg/L
% per metre submergence (fine bubble ~25-30%, coarse ~10-15%)
Process water correction (0.4-0.8 typical, default 0.65)
metres

Aeration Design Factors

Several correction factors affect real-world oxygen transfer: Alpha (α) = process water vs clean water transfer ratio (0.4-0.8 for wastewater); Beta (β) = saturation concentration ratio (0.95 typical); Temperature = warmer water holds less DO; Fouling = diffuser clogging reduces efficiency over time. Fine bubble diffusers (disc, tube, or panel) achieve 25-35% SOTE while coarse bubble achieves 10-15%.

  • Fine bubble: 25-35% SOTE, higher capital cost, lower energy requirement
  • Coarse bubble: 10-15% SOTE, lower capital cost, higher energy requirement
  • Jet aeration: 15-25% SOTE, good for high-solids applications
  • Surface aerators: 1.2-2.5 kg Oâ‚‚/kWh, good for lagoon systems

Nitrification Oxygen Demand

When nitrification is required to meet ammonia discharge limits, additional oxygen is needed. The stoichiometric requirement is approximately 4.6 kg O₂ per kg NH₃-N oxidised. This typically adds 30-50% to total oxygen demand. For designs requiring both nitrification and denitrification, consider an anoxic zone to recover approximately 2.9 kg O₂ per kg NO₃-N denitrified.

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Aeration & Oxygen Transfer

Aeration accounts for 50–70 % of a biological plant’s electrical Operating expenditure — designing it well is the single largest lifetime saving.

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