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
Flow (m³/h)
Flow (m³/s)
Cycles n₂
Per-cycle water (m³)
Feed time te (h)
Settling u (m/h)
Settle ts (h)
Aeration ta (h)
Reaction ratio e
Out soluble BOD (mg/L)
Reactor volume V (m³)
Decant h₁ (m)
Sludge load (kg/kg)
ΔXv (20°) kg/d
ΔXv (10°) kg/d
Anorganic ΔXs kg/d
ΔX (20°) kg/d
ΔX (10°) kg/d
Wet sludge (m³/d)
Wet sludge (10°) m³/d
Out BOD (mg/L)
Out NH₄ (10°) mg/L
Out NH₄ (20°) mg/L
Nitrified NH₄ eff (mg/L)
Carbon O₂ kg/d
Nitrify O₂ kg/d
Denitrify O₂ kg/d
AOR kg/d
AORmax kg/d
O₂/BOD kg/kg
SOR(25) kg/h
SORmax kg/h
Air QF(25) m³/h
Max air m³/h
Air pressure MPa
Aerators n₁
Service area m²

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.