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Example ApplicationBrewery, Dairy & Mixed Food

Brewery + Dairy: DAF + Electrocoagulation + UV/H2O2 + GAC + RO

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

Large mixed brewery-dairy wastewater plant processing 800 m3/day with combined COD 9,000 mg/L. Brewery contributes high-strength effluent from craft beer production (small batches, frequent recipe changes). Dairy adds whey permeate, cream, and CIP chemical consumption. Unique challenges: variable pH 3.5-11 from recipe changes and CIP, emulsified fats stabilised by brewery proteins, iron contamination from brewery equipment (up to 80 mg/L Fe), and seasonal volume swings of 50-120%. Discharge requires COD <50 mg/L, fat <3 mg/L, iron <0.5 mg/L for direct reuse as boiler feed makeup. Electrocoagulation chosen to eliminate external chemical dosing and use existing iron in wastewater as sacrificial anodes.

Key Performance Targets
<20
Final COD mg/L
99.8%
COD removal
<0.05
Iron mg/L
88%
Water recovery
<50
Conductivity µS/cm
0%
External chemicals

Treatment Approach

A six-stage hybrid train — from raw brewery + dairy effluent to boiler-feed-quality reuse water. Each stage links to the relevant equipment or process page.

400 m³ equalization tank with mixing and online pH monitoring. Acidic brewery batches (pH 3.5–5) mix with alkaline dairy CIP (pH 10–11) for natural buffering to pH 6.5–8.0. 12-hour retention smooths flow and load; automated acid/caustic trimming holds pH 7.0 ±0.3. Hot dairy streams blended with cooler brewery waste keep 25–30°C, preventing thermal shock and keeping fat liquid.

Volume400 m³Retention12 hpH7.0 ±0.3Temp25–30°C

Heated DAF at 36°C with dissolved air at 0.45 MPa. Brewery proteins act as natural surfactants — no polymer needed. Ferric chloride (150 mg/L) enhances phosphate precipitation. Float at 15% solids (65% fat, 25% protein, 10% solids) sold to a biogas plant as high-calorific feedstock. Skimmings removed continuously to prevent re-entrainment.

Air0.45 MPaFeCl₃150 mg/LFloat TS15%COD9,000→6,200

Electrocoagulation with iron anodes (20 A/m²) generates Fe²⁺ in-situ — no external iron dosing. A 30-min EC cell destabilises emulsified fats and coagulates colloidal proteins; electrolytic hydrogen micro-bubbles assist flotation. Fe(OH)₃ precipitate adsorbs organics, and sludge volume is 40% below chemical coagulation.

Current20 A/m²HRT30 minPower2.5 kWh/m³COD6,200→3,200

Medium-pressure UV (1.5 kW per m³/h) with H₂O₂ at 800 mg/L. UV photolysis generates hydroxyl radicals that break down brewery hop compounds (alpha/beta acids) and dairy lactose derivatives. UV fluence 800 mJ/cm² gives 4-log coliform reduction. UVT is monitored — if it drops below 65% from colour, H₂O₂ dose rises automatically. No chemical sludge produced.

UV1.5 kW/m³/hH₂O₂800 mg/LFluence800 mJ/cm²COD3,200→800

Lead-lag GAC columns (3.5 m diameter, 25 min EBCT) adsorb residual UV oxidation by-products and trace organics. Critically, GAC also captures residual dissolved iron from electrocoagulation — polishing 2 mg/L to <0.3 mg/L to protect the RO membranes from iron fouling. Iron breakthrough is flagged by a yellow tint; carbon is replaced every 14 months.

EBCT25 minIron2→<0.3 mg/LCOD800→120Carbon life14 mo

Two-stage RO with iron-fouling-resistant low-charge (LFC) membranes, anti-scalant 3 mg/L at pH 6.5. First pass: 92% recovery, COD to <20 mg/L, iron to <0.05 mg/L. Second pass: conductivity 1,500 to <50 µS/cm, silica <0.5 mg/L. Final effluent meets boiler-feed standards (BS EN 12953) at 88% overall recovery; concentrate recycles to the equalization tank.

Recovery88%Conductivity<50 µS/cmIron<0.05 mg/LCOD120→<20
9,000Raw COD (mg/L)
<20Final COD (mg/L)
>99%Overall COD removal
88%Water recovery

Equipment Configuration

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

Equalization Tank

400 m3 mixer tank, pH/temp monitoring, acid/caustic trimming, 12h retention.

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Heated DAF System

DAF 35 m3/h, 36°C, protein-enhanced flotation, 0.45 MPa, continuous skimming.

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Electrocoagulation Cell

Iron anode EC, 20 A/m2, 30 min HRT, 2.5 kWh/m3, H2 micro-flotation.

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UV/H2O2 Reactor

Medium-pressure UV 1.5 kW/m3/h, H2O2 dosing, UVT monitor, 800 mJ/cm2.

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GAC System

Lead-lag 3.5 m diameter, 25 min EBCT, iron polishing function, 14-month life.

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Two-Stage RO System

LFC iron-resistant membranes, 88% recovery, boiler feed quality output.

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Performance Achieved

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

<20
Final COD mg/L
99.8%
COD removal
<0.05
Iron mg/L
88%
Water recovery
<50
Conductivity µS/cm
0%
External chemicals

Related Equipment

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

pH Correction

Multi-point acid/caustic dosing for equalization and RO inlet pH control.

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Chemical Dosing

H2O2 day tank with metering pump, anti-scalant, and caustic preparation.

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Rectifier Power Supply

Thyristor-controlled DC rectifier for EC cell, 0-500A, auto current control.

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UV Transmittance Monitor

Online UVT analyser for automatic H2O2 dose adjustment.

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Related Treatment Processes

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

Apply This Configuration to Your Site

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

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