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Dairy and Dairy Wastewater Treatment: DAF, UASB, and MBR Solutions

May 21, 2026 2 dk okuma 17 görüntülenme
Dairy and dairy product factories produce critical wastewater with high KOİ (1,500-6,000 mg/L), high oil (200-800 mg/L), and whey (KOİ 30,000+ mg/L). The biologically highly degradable nature of this wastewater allows for the correct process selection to enable energy recovery (biogas). In this article, we discuss wastewater characterization in the dairy sector, optimal flow diagrams, whey management, and water recovery strategies.
Dairy and Dairy Wastewater Treatment: DAF, UASB, and MBR Solutions

Short answer: Standard flow for dairy factory wastewater: Balancing → DAF (oil + AKM) → UASB (biogas production) → MBR (nitrogen + final polishing) → optional RO (water recovery). Whey (KOİ 30,000+ mg/L) should be collected separately and managed with anaerobic or valorization (whey protein). With proper design, 85-95% KOİ, 95% FOG, and 80+% nitrogen removal can be achieved; biogas meets 30-50% of the factory's energy needs.

Dairy Wastewater Treatment Character of Dairy Factory Wastewater

Dairy sector wastewater originates from different production lines:

  • CIP (Clean in Place) water: Alkali (NaOH) + acid (HNO₃) based washing
  • Production lines: Milk splashes, spills, equipment washing
  • Whey: The liquid remaining after milk proteins are precipitated — highly concentrated
  • Cooling and boiler blowdown: Low pollution

Typical composition (excluding whey):

Parameter Dairy Factory Whey SKKY Limit
KOİ (mg/L)1,500-6,00030,000-70,000< 200
BOİ (mg/L)900-4,00020,000-50,000< 50
BOİ/KOİ0.6-0.80.7-0.8
FOG (mg/L)200-800500-2,000< 50
AKM (mg/L)500-2,0001,000-3,000< 100
TN (mg/L)50-200300-700< 15
TP (mg/L)10-80100-300< 1
pH5-11 (fluctuating)4-66-9

As seen, the BOİ/KOİ ratio is 0.7+ — wastewater is biologically highly suitable. Main challenges: high FOG, acid-base fluctuations (due to CIP), load spikes created by whey.

Optimum Flow Diagram

A modern dairy factory wastewater treatment plant typically consists of 7 stages:

1. Bar Screen + Oil Separator

Holds coarse materials such as milk particles, casein clumps, fabric, labels. The grease trap reduces pre-FOG by 30-50%.

2. Balancing Tank

The most critical step of the dairy factory. Absorbs pH fluctuations in the range of 4-11 from CIP washings, flow peaks, and KOİ concentration fluctuations.

Typical HRT: 8-24 hours. pH adjustment: Stabilized in the range of 6.5-7.5 with NaOH/HCl dosing. Mixing: Aeration or mechanical mixer.

3. DAF (Dissolved Air Flotation)

Removes 85-95% of oil, casein clumps, and AKM. Generally chemically assisted (FeCl₃ + cationic poly-electrolyte). The float exiting the DAF prevents it from becoming a load on biological treatment.

4. Anaerobic Reactor (UASB / EGSB)

The energy recovery opportunity of the dairy sector. 70-85% of the wastewater's KOİ is converted to biogas (CH₄ + CO₂). Approximately 1,000-1,400 Nm³/day of biogas is produced from a facility with 1,000 m³/day and 4,000 mg/L KOİ — approximately 6-8 MWh/day energy potential.

UASB design parameters:

  • Ideal for high concentration KOİ (>1500 mg/L)
  • HRT 6-12 hours
  • Granular sludge technology → compact
  • Biogas collection → boiler or cogeneration (CHP)

5. Aerobic Biological (MBR or MBBR + MF)

Reduces the remaining KOİ in the anaerobic effluent (1,000-2,000 mg/L) to the target (<100 mg/L). Nitrogen and phosphorus removal is done here (A2/O configuration).

MBR advantage: High MLSS tolerance (10-12 g/L) in dairy wastewater, 100% retention of particulate casein/protein residues.

6. UF + RO (Water Recovery, Optional)

Modern dairy factories aim for 50-70% water recovery. RO permeate is used directly as CIP wash water or boiler feed. ROI is typically 2-4 years (savings from water bills).

7. Sludge Dewatering (Belt Press / Decanter)

UASB sludge (granular) is low; aerobic waste sludge is at a medium level. Compacted sludge is directed to the biogas facility or agricultural fertilizer (when appropriate).

Whey Management

Whey is the highest concentration wastewater in the dairy sector. There are two main approaches:

1. Directly Treating Whey

High KOİ anaerobic (UASB or high-speed EGSB) is mandatory. Giving it to aerobic biology alone = system failure. After anaerobic, it mixes with the normal flow.

2. Valorizing Whey (Preferred)

Whey is actually a raw material: it contains lactose, protein (whey protein). Modern dairy factories:

  • Separate with UF — whey protein concentrate (WPC) → sold to the sports nutrition market
  • Concentration with RO → lactose production (baby formula)
  • Nanofiltration → separation of salt and lactose

With this approach, whey is no longer "waste" but becomes an additional source of income. The wastewater load is reduced by 60-80%.

Sectoral Best Practices

  1. Water savings at the source: Optimize CIP, reduce wastewater volume by 20-30% with dry cleaning techniques
  2. Collect whey separately: Evaluate without mixing with the main wastewater or a dedicated anaerobic line
  3. pH monitoring: Automate NaOH/HCl dosing with an online pH probe
  4. Prevent FOG from entering the pocket: Regular emptying of the grease trap (weekly) + DAF float disposal plan
  5. Biogas valorization: If you are producing it, definitely use it for energy production (CHP) — typical payback period is 3-5 years

Case Study: 1000 m³/day Dairy Factory

Target parameters for a typical integrated milk-yogurt-cheese factory:

  • Wastewater flow: 1,000 m³/day
  • Influent KOİ: 4,500 mg/L
  • Target effluent KOİ: < 150 mg/L (efficiency >96%)
  • Effluent FOG: < 30 mg/L
  • Biogas production: ~1,200 Nm³/day (~7 MWh/day energy)
  • Water recovery: 60% (with RO)

With this configuration, the factory ensures both discharge compliance and energy + water recovery. The investment payback period (from total savings of water bill + energy + waste sludge disposal): generally 3-5 years.

5 Common Mistakes

  1. Keeping the balancing tank small: During CIP washings, pH spikes to 2 or 12; a small tank cannot buffer, leading to biological shock.
  2. Skipping DAF and sending directly to biology: Oil + casein flocs damage the membrane or sludge. Chronic bulking, filament bursting.
  3. Mixing whey with the main wastewater: A load spike of 30+ g/L KOİ can disrupt the entire facility.
  4. Not valorizing anaerobic biogas: Letting it escape into the atmosphere is both an environmental and economic loss. CHP or boiler is mandatory.
  5. Ignoring phosphorus in sludge: Aerobic waste sludge is rich in P → suitable disposal or fertilizer valorization.

Conclusion

Dairy factory wastewater is highly concentrated but biologically very suitable. Proper process design (DAF + UASB + MBR + RO) enables both discharge compliance and energy + water recovery. If whey is managed separately, the wastewater load is significantly reduced, and raw material is recovered.

Related guides: FOG Removal, KOİ Removal, MBR vs MBBR. You can request wastewater characterization + biogas potential analysis for your dairy facility.

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Frequently Asked Questions

7 Soru
Typical flow: Balancing → DAF (oil + AKM) → UASB anaerobic (biogas production) → MBR (nitrogen + final polishing) → optional RO (water recovery). The BOD/COD ratio of dairy wastewater is high (0.6-0.8) — biological treatment is very effective. Due to the high COD concentration, anaerobic biogas utilization is attractive.
2 approaches: (1) Treatment: COD is removed by 85-90% using high concentration anaerobic (UASB/EGSB). (2) Evaluation (preferred): Whey protein concentrate (WPC) is separated by UF, lactose is concentrated by RO → sold to the baby food/sports nutrition market. This approach reduces wastewater load by 60-80% and generates revenue.
In a typical facility with a flow rate of 1000 m³/day and 4500 mg/L KOİ, 1,000-1,400 Nm³ of biogas is produced daily — approximately 6-8 MWh of energy potential. With CHP (co-generation), it can meet 30-50% of the factory's energy needs. The payback period is 3-5 years.
CIP (Clean in Place) is alternately performed with alkali (NaOH 1-3%) and acid (HNO₃/HCl) → wastewater pH fluctuates between 2-12. Solution: Large balancing tank (HRT 8-24 hours) + automatic pH dosing (NaOH/HCl). It cannot be sent to biological treatment without stabilizing the pH at 6.5-7.5.
Dairy wastewater is rich in fat (FOG) (200-800 mg/L). When directly fed to biology: (1) oxygen transfer decreases, (2) filamentous bacteria bloom (bulking), (3) membrane fouling (in MBR), (4) casein clumps swell the sludge. FOG is removed by 85-95% with DAF, biologically preserved.
50-70% water recovery is the current standard. Water treated with UF + RO is used for CIP washing, boiler feed, or cooling tower water. ROI is typically 2-4 years. Some new facilities are establishing ZLD (Zero Liquid Discharge) systems with a target of 85%+ recovery.
In the structure of milk protein (casein), there is a significant amount of nitrogen, and in the natural composition of milk, there is a large amount of phosphorus. The organic N that enters the wastewater is converted to NH₄ through protein decomposition. Solution: The MBR A2/O configuration (anaerobic-anoxic-aerobic) removes both N and P. The target for effluent is TN<15, TP<1 mg/L.

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