Technical Guide to MBBR Suspended Carrier Selection and Application
The MBBR process uses suspended carriers as its core component. Carrier specific surface area (typically 200–600 m²/m³), material (polyethylene/polypropylene), and fluidization performance directly determine treatment efficiency. High-quality carriers have a density of 0.95–0.98 g/cm³, enabling uniform fluidization with low energy input, fast biofilm formation, and no backwashing required.
Carrier filling ratio ranges from 30% to 60% based on loading. For carbon removal, BOD surface area loading rates vary: >20 g/(m²·d) for high load, 5–15 g/(m²·d) for conventional load, and ≤5 g/(m²·d) for low load. Denitrification rates are typically 0.15–1.0 g/(m²·d) for pre-denitrification.
System design requires horizontal flow velocity <20 m/h, HRT of 1.0–1.2 h (anoxic) and 3.5–4.5 h (aerobic), and DO at 2.0–6.0 mg/L. Adequate pretreatment with fine screens (≤3 mm) is essential. Aerobic tanks use perforated pipe aeration; anoxic tanks require mixers with 25–35 W/m³ power.
MBBR offers high efficiency, shock load resistance, operational flexibility, and low-cost adaptability for municipal and industrial wastewater treatment.