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Example ApplicationBrewery & Beverage

Brewery Effluent: DAF + Fenton AOP + GAC (Non-Biological)

This is an illustrative scenario showing how Reynolds & Bauhm equipment can be configured for this application. Every site has unique requirements — contact us for a solution tailored to your specific wastewater characteristics.

Process Requirements & Constraints

Brewery startup producing 350 m3/day of high-strength effluent with COD 7,000 mg/L, BOD 4,500 mg/L, TSS 1,800 mg/L, and fat 600 mg/L. Site has no space for advanced biological treatment and requires rapid commissioning. Discharge limit COD <500 mg/L. Zero biological processes used – pure chemical and physical treatment.

Key Performance Targets
<400
Final COD mg/L
94%
COD removal
88%
Fat removal
0%
Biological processes
6 hr
Total treatment time
2 wk
Commissioning time

Treatment Approach

Step-by-step process configuration from raw wastewater to compliant discharge.

01

DAF Fat & Solids Removal

Heated DAF at 35°C with ferric chloride (200 mg/L) and cationic polymer removes 88% of fats and 75% of suspended solids. Float sludge at 10% solids recovered for rendering. DAF effluent COD reduced from 7,000 to 4,800 mg/L. Retention 30 minutes at 0.5 MPa saturation.

02

Fenton AOP Oxidation

Acidified effluent (pH 3.0) treated with FeSO4 (400 mg/L) and H2O2 (1,200 mg/L) in 3-hour reaction tank. Hydroxyl radicals mineralise recalcitrant organics. COD reduced from 4,800 to 1,200 mg/L (75% removal). Residual iron precipitates as hydroxide.

03

neutralisation & Clarification

pH raised to 8.5 with hydrated lime for iron hydroxide precipitation. Lamella clarifier captures precipitated iron and organics at 6 m/h upflow. Effluent COD 900 mg/L, TSS <30 mg/L. Sludge at 5% solids dewatered via screw press to 22% cake.

04

GAC Adsorption Polishing

Two-column lead-lag GAC system adsorbs residual organics. EBCT 25 minutes. Lead column breakthrough triggers carbon replacement. Effluent COD <400 mg/L consistently. Spent carbon thermally regenerated off-site.

05

Final Filtration & Discharge

5-micron cartridge filtration captures any GAC fines. Effluent pH adjusted to 7.0 with CO2. No biological stage required – total treatment time 6 hours from influent to discharge. System operational within 2 weeks of delivery.

Equipment Configuration

The specific equipment selected for this application, sized for the flow rate and contaminant load.

DAF System

Heated DAF 15 m3/h, ferric/polymer dosing, fat skimmer, 0.5 MPa saturation, insulated tank.

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Fenton Reactor

SS baffled reactor, FeSO4/H2O2 dosing, pH control, 3h HRT, automated sludge separation.

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Lamella Clarifier

SS clarifier 50 m2, iron hydroxide separation, 6 m/h upflow, automatic desludging.

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GAC System

Lead-lag columns 2.4 m diameter, 25 min EBCT, steam regeneration, breakthrough monitoring.

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Performance Achieved

Representative performance data based on typical operating conditions for this equipment configuration.

<400
Final COD mg/L
94%
COD removal
88%
Fat removal
0%
Biological processes
6 hr
Total treatment time
2 wk
Commissioning time

Related Equipment

Explore the full range of equipment used in this and similar applications.

Chemical Dosing System

FeSO4, H2O2, lime, and polymer preparation with day tanks and metering pumps.

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pH Correction

Multi-stage acid and alkali dosing for Fenton reaction and discharge pH.

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Screw Press

Multi-disc press for iron hydroxide and DAF sludge dewatering.

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Cartridge Filter

5-micron final filtration for GAC fines capture.

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Related Treatment Processes

Discover how these treatment processes connect to form complete wastewater treatment solutions.

Project Approach & Engineering

Reynolds & Bauhm follows a structured engineering methodology for every project. We begin with detailed wastewater characterisation, process selection based on contaminant profiles, pilot testing where required, and full-scale design with performance guarantees. Our multidisciplinary team of chemical, mechanical, and electrical engineers ensures seamless integration of process, mechanical, and control disciplines.

Characterisation

Comprehensive influent analysis including COD, BOD, TSS, heavy metals, pH, temperature, and flow profiling.

Process Design

Process flow development with P&IDs, mass balances, and hydraulic modelling validated by CFD where appropriate.

Pilot Testing

On-site pilot trials validate performance guarantees under actual operating conditions before capital commitment.

Commissioning

FAT, SAT, performance trials, operator training, and handover documentation ensuring operational readiness.

Equipment Configuration

Pre-TreatmentScreening, grit removal, and flow equalisation
Primary TreatmentDAF or lamella clarification for solids and oil removal
Secondary TreatmentBiological oxidation (activated sludge, MBBR, or SBR)
Tertiary TreatmentFiltration, UV disinfection, or chemical polishing
Sludge ManagementThickening and dewatering via belt press or centrifuge
Control SystemPLC with HMI touchscreen and optional SCADA integration
Chemical DosingAutomated coagulant, flocculant, and pH correction
MaterialsSS316L, duplex, or rubber-lined carbon steel

Performance Outcomes

COD Removal

85 – 98% chemical oxygen demand reduction depending on process configuration and influent variability.

TSS Removal

90 – 99% suspended solids reduction through combined physical and biological treatment stages.

Water Reuse

Tertiary treatment enables up to 80% water recycling for non-potable process applications.

Apply This Configuration to Your Site

Our engineers will adapt this equipment configuration to your specific wastewater analysis, flow rate, and discharge requirements.

Industries We Serve

Our expertise spans multiple industries with sector-specific water treatment solutions.