CIRCOX Brewery Wastewater Treatment in Shanghai: IC+CIRCOX Process Case Study

Jun 27, 2025

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Case Study of Brewery Wastewater Treatment -

CIRCOX Process at a Shanghai Company

 

This brewery wastewater treatment system has a capacity of 4,800 m³/day, with the process flow shown in Figure 1-1.

 

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Key Treatment Units

 

1. IC (Internal Circulation) Reactor

 

Developed in the 1980s by Paques (Netherlands) based on UASB principles, the IC reactor consists of:

 

  • Mixing zone
  • Sludge expansion bed
  • Polishing zone
  • Recirculation system

 

Advantages over conventional anaerobic processes:

Compact design (Height/Diameter ratio: 16–25 m tall, small footprint)

Low sludge production (~1% of influent COD, easy dewatering)

Energy-efficient (Self-circulating via biogas lift, no external mixing power)

Closed system (Controls VOC emissions; biogas: 70–80% CH₄, 20–30% CO₂)

 

2. CIRCOX(Closed Internal ReCirculation OXidation) Reactor

 

A vertical dual-cylinder aerobic biofilm reactor:

 

  • Inner riser tube: Water + compressed air flow upward, forming biofilm on carrier media (fine sand-like material).
  • Outer downcomer: Settled sludge returns to the reactor base.
  • "Cap-shaped" top section (diameter expanded by ~1/3) for three-phase separation (biogas/water/sludge).

 

Key features:

  • Excellent sludge settling properties (minimal biomass washout)
  • High treatment efficiency with 15–25 g/L VSS concentration

brewery wastewater treatment

 


 

Process Flow (Refer to Fig. 1-1)

 

  1. Wastewater collection → Inlet well → Pump → Rotary screen (with online pH/temperature monitoring).
  2. Buffer tank (submersible mixer for homogenization) → Pre-acidification tank (3h HRT; partial VFA conversion + pH/nutrient adjustment).
  3. IC reactor (2h HRT; COD load: 15 kg/(m³·d)) → CIRCOX reactor (1.5h HRT; COD load: 6 kg/(m³·d)).
  4. Lamella clarifier (flocculant dosing) → Effluent tank (partial reuse/discharge).
  5. Sludge → Dewatering system.
  6. Exhaust gas treatment: Centrifugal fan → Scrubber tower (using treated effluent + dilute alkali).

 


 

Design Parameters

 

Table 1-1 Main Treatment Unit Design Parameters
Unit Dimensions HRT COD Loading Notes
Pre-acidification Ø6m × H21m 3h - pH/nutrient adjustment
IC reactor Ø5m × H20.5m 2h 15 kg/(m³·d) Biogas yield: 0.35 m³/kg CODₜₕ
CIRCOX reactor Ø5m (base)–Ø8m (top) × H18.5m 1.5h 6 kg/(m³·d) VSS: 15–25 g/L

 

 


 

Performance

 

  • Effluent quality (Table 1-2): Meets all discharge standards.
  • Automation: Fully automated control (IC/CIRCOX core components imported from the Netherlands).

 

Table 1-2 Treatment Performance of a Brewery
Wastewater Plant in Shanghai
Parameter Influent Effluent
Average Range Average Range
COD (mg/L) 2000 1000-3000 78 50-100
BOD₅(mg/L) 1250 600-1875 ≤30 -
SS/(mg/L) 500 100-600 50 10-100
NH₄⁺-N (mg/L) 30 12-45 10 5-15
Phosphate (mg/L) - 10-30 - -
pH 7.5 4-10 7.5 6-9
Temperature (°C) 37 30-50 <40 -

 

 

Advantages of IC + CIRCOX combo:

 

  • Compact footprint
  • Odor-free operation
  • Low sludge yield
  • High treatment efficiency