Dairy Filtration Application Guide
Dairy Processing Conditions & Solutions
Raw Milk · Cheese · Whey · Yogurt · Cream · Powdered Milk
This guide covers raw milk reception, bioburden reduction, casein and whey protein fractionation, cheese brine, whey, yogurt, ice cream base, powdered milk ingredients, utilities, and filtration and membrane separation selection for CIP boundaries.
01 — 06
Typical Dairy Filtration and Membrane Separation Routes
01Raw Milk or Dairy Product Material→
02Sizing and Fat Separation→
03Clarification and Protective Filtration→
04Microfiltration or Depth Filtration→
05UF/NF/RO for Targeted Separation→
06Sanitary Filling and Quality Release
Pleated Filter Cartridges for Cheese, Brine, and Whey Processing
Sweet Whey: Curd Powder and Fat Load Material | Sweet Whey after Cutting/Whey Drainage
Cheese Brine: Turbidity and Microbial Build-Up Material | Circulating Brine
Brine Filtration Still Quickly Fouling Membrane Material | High Calcium, High Protein Brine
UF Cheese: Viscosity Increase, Change in Whey Drainage Material | UF Concentrated Cheese Whey
Acid Whey: NF/RO Scaling Material | Greek Yogurt or Acid Curd Wastewater
Acid Milk, Condensed Milk, Ice Cream, Milk Powder, and Additives
Greek Yogurt: Whey Separation, Protein Insufficiency Material | Milk Base before Fermentation
Condensed Milk / Ice Cream Base: Agglomerate Blockage of Heat Exchanger Material | Syrup, Stabilizers, Cocoa/Flavor Dispersions
Low Solids Liquid Additives: Final Microbial Load Material | Salt, Acid, Enzymes, Flavor or Vitamin Solutions
Milk Powder Pre-Stage: Concentrate Protection Material | Milk Liquid / Whey before Evaporation
Milk Powder Drying/Cooling: Air Re-Contamination Material | Spray Drying, Fluidized Bed, Packaging Area
Lactose/Mineral Concentrate: Conflict Between NF Flux and Purity Material | UF Permeate / Acid Whey
Utility Engineering, Aseptic Boundary, and CIP
Process Water: Final Microbial Fluctuation Material | Mixing Water, Rinse Water, Final Rinsing Water
Product Contact Compressed Air / Nitrogen Material | Filling, Purging, Tank Pressurization
Aseptic Tank Venting: Pressure Drop and Back Suction Material | Aseptic Buffer Tank, Fermentation Tank, Filling Tank
Membrane Flux Does Not Recover Post-CIP Material | MF/UF/NF/RO Systems
Microbiological Positive After Filtration Material | Liquid or Gas Final Filter
Fault Diagnosis and Acceptance
Differential Pressure / Flux Diagnostics
| Observation | Primary Considerations | Confirmations Required | Improvement Directions |
|---|---|---|---|
| High Differential Pressure Upon Startup | Pore Size Too Small, Low Temperature, High Viscosity, Insufficient Area | Actual Temperature/Flow; Filter Orientation; Valve Position | Increase Area, Raise to Allowable Temperature, Add Coarse Filtration |
| Initial Rapid Clogging in First Few Minutes | Clots, fat globules, protein aggregates, or pre-filtering not performed | Residues, particle size, fat/protein, pre-filter differential pressure | Separate/clear first; use depth or crossflow |
| Differential pressure normal but downstream turbid | Bypass, seal or nominal accuracy mismatched | End cap, O-ring, housing bypass, β-value/absolute grade | Calibration port; switch to verifiable grade |
| No flow recovery post-CIP | Irreversible protein/mineral composite pollution | Acid/base sequence, temperature, concentration, circulation flow rate | Step cleaning; reduce concentration/temperature shock |
| 0.2 μm Air filter airflow drop | Condensate moisture wets hydrophobic membrane or upstream oil presence | Drain, dew point, compressed oil, installation slope | Enhance water and oil removal; replace and perform integrity testing |
| Intermittent microbial positivity | Sample, downstream or installation integrity issue | Culture method, bypass, seal, terminal tubing, integrity testing | Isolate batch; system investigation, not just replace with smaller pore size |
Recommended process package
| Scenario | Recommended Process Flow | Filter Cartridge/Capsule | Validation Focus |
|---|---|---|---|
| Small Cheese Factory Brine | 50–100 μm Filtration → 10–20 μm PP → 1–5 μm PP → 0.2 μm PES Capsule (Low Load) or 0.1–0.2 μm Circulating Microfiltration | PP Pleated, PES Capsule, Necessary Gas Breathing Capsule | Batch, Turbidity, Colony Count, Salinity, pH, Pressure Differential |
| Whey Protein Line | 100–300 μm → 20–50 μm → 1–5 μm → 0.1 μm Microfiltration → 5–30 kDa Ultrafiltration/Dialysis → Nanofiltration/RO → Powdering | Screen/bag/PP pleated; water/gas final filter cartridge | Fats/curd powder, calcium phosphate, flux recovery, quality balance |
| Milk powder/formulation powder | Raw material screening/settling → thermal treatment → evaporation → spray drying → cooling → screening → packaging; independent validation of air system | initial coarse fine filtration, liquid additives in capsule filter, tank venting | Downstream air, condensate, dust, wet/dry area segregation and environmental monitoring |
