MBBR Reactor
Product

MBBR Reactor

Moving bed biofilm reactor for biological COD and nitrogen removal

  • High biomass concentration on moving carriers
  • Compact – significantly smaller than conventional activated sludge tanks
  • Robust against load fluctuations and toxic shocks
  • No sludge recirculation required
  • Also available as a containerised unit

Image gallery

MBBR tank with moving carrier media
MBBR tank with moving carrier media

Technical data

Flow rate1 – 500 m³/h
COD removal> 85%
Carrier fill ratio30 – 60%
Protected surface area350 – 800 m²/m³ carrier
AerationFine or coarse bubble
MaterialStainless steel / concrete tank / container

Indicative values. Final data is confirmed project-specifically.

How it works

1

Inlet

Pre-treated wastewater enters the reactor.

2

Biofilm growth

Microorganisms grow as a biofilm on the moving plastic carriers.

3

Aeration & mixing

Aeration supplies oxygen and keeps the carriers in permanent motion.

4

Separation

Excess biomass is separated downstream by settling, flotation or filtration.

Typical applications

COD removal in industrial wastewaterNitrification and denitrificationUpgrading existing activated sludge plantsFood and beverage industryDecentralised and containerised plants

Sizes & configurations

MBBR — design parameters

ParameterTypical rangeRemark
Carrier fill ratio40–70 % (typically 50 %)Approx. 67 % is the practical maximum for free carrier movement
Specific surface area of carrier350–1200 m²/m³Standard carriers approx. 500 m²/m³ bulk (≈ 335 m²/m³ effective at 67 % fill)
Surface load BOD removal5–15 g BOD/m²·dTertiary polishing 2–5 g BOD/m²·d
Surface load nitrification0.5–1.5 g NH₄-N/m²·d< 10 °C: 0.3–0.8; > 20 °C: up to 2.0
Surface load denitrification1.0–3.0 g NO₃-N/m²·dRequires an external or internal carbon source
Dissolved oxygen (aerobic stage)2–4 mg/LHigher DO required at high surface loads
Design safety factor1.2–1.5Applied to the calculated carrier surface area

Literature design values for orientation, not a product specification. The plant is sized project-specifically from the measured load.

Sources: CED Engineering, "Moving Bed Biofilm Reactor Design"; US EPA wastewater technology documentation; carrier manufacturer data sheets.

Indicative values. Final data is confirmed project-specifically.

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