SBR Sewage Treatment Design
Classic SBR process sizing — reactor volume, oxygen demand (AOR/SOR), excess sludge, nitrogen removal check and aeration system.
Total change Kz
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Flow (m³/h)
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Flow (m³/s)
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Cycles n₂
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Per-cycle water (m³)
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Feed time te (h)
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Settling u (m/h)
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Settle ts (h)
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Aeration ta (h)
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Reaction ratio e
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Out soluble BOD (mg/L)
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Reactor volume V (m³)
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Decant h₁ (m)
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Sludge load (kg/kg)
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ΔXv (20°) kg/d
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ΔXv (10°) kg/d
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Anorganic ΔXs kg/d
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ΔX (20°) kg/d
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ΔX (10°) kg/d
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Wet sludge (m³/d)
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Wet sludge (10°) m³/d
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Out BOD (mg/L)
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Out NH₄ (10°) mg/L
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Out NH₄ (20°) mg/L
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Nitrified NH₄ eff (mg/L)
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Carbon O₂ kg/d
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Nitrify O₂ kg/d
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Denitrify O₂ kg/d
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AOR kg/d
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AORmax kg/d
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O₂/BOD kg/kg
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SOR(25) kg/h
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SORmax kg/h
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Air QF(25) m³/h
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Max air m³/h
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Air pressure MPa
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Aerators n₁
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Service area m²
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Classic SBR per GB 50014. Per-cycle water = Q/n₂/n₁; feed time te = 24/n₁n₂; settling velocity u = 46000·X⁻¹·²⁶; ts = (h₁+ε)/u; ta = t−te−ts−td; reactor volume V = Y·θc·Q·(S₀−Se)/(e·X·f·(1+Kd·θc)); Se = Sz−7.1·Kd·f·Ce. Excess sludge ΔXv = Y·Q·(S₀−Se)/1000 − e·Kd·X·V·f/1000; anorganic ΔXs = Q·(1−fb·f)·(SSin−SSout)/1000. Total oxygen AOR = carbon + nitrification − denitrification; AORmax = Kz·AOR. Standard SOR converts to field conditions by α, β, CS and altitude.