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Understanding the Options

Mammalian Cell Culture Clarification



Primary Clarification
Essential Process Requirements
  • Removes whole cells and solids from bioreactor fluid and recover product in filtrate
  • Requires high capacity
  • Wide feed stream variability depending on cell culture type and conditions
  • If solid content is too high, centrifugation becomes preferred technology

Recommended FilterFilter Characteristics
Prostak Open-Channel Modules with 0.22 µm or 0.65 µm Durapore Membrane
  • For bioreactors volumes up to 1,000 L or larger volumes with low usage rates of less than 10 batches/year
  • Double layer design enhances loading capacity and filtrate quality
  • Unique configuration allows compression of multiple process steps into one, lowering overall filtration costs.
  • Selection of C0HC or D0HC media grade depends on particle size distribution in feed solution. Choice should be based upon small-scale testing.
Prostak Open-Channel Modules with 0.22 µm or 0.65 µm Durapore Membrane
  • Best suited for large bioreactors >1,000 L or bioreactors with high usage rates of more than 10 batches/year
  • Open-channel design accommodates fluids containing low to medium cell density and solids
  • High flux at low transmembrane pressure
  • Robust construction allows multiple use
  • Validated for multiple SIP cycles
  • Selection of 0.22 µm or 0.65 µm membrane depends on particle size distribution in feed solution. Choice should be based upon small-scale testing.

ALTERNATIVE: If the cell culture has high cell viability and relatively low cell counts, all polypropylene Polygard-DF depth filter cartridges is a viable option for bioreactors up to 1,000L.
Secondary Clarification or Polishing
Essential Process Requirements
  • Feed stream quality can vary depending on cell type, culture conditions, and primary clarification technology
Recommended FilterFilter Characteristics

Triple-layer Millistak+ HC Filters
(Grade A1HC or B1HC)

Disc Filters

Pod Filters
  • Triple-layer configuration includes a membrane bottom layer to enhance filter loading capacity and retention
  • High filtrate quality allows smaller size requirements for downstream sterilizing-grade filtration step
  • Unique design enables the compression of multiple process steps into one, lowering overall filtration costs
  • The selection of grade A1HC or B1HC depends on the fluid particle size distribution and should be based on small-scale testing.

ALTERNATIVE: If process hardware dictates the use of pleated cartridge filters, Millipore suggests testing Polysep II multi-layer prefilters in your small-scale trials.
Bioburden Reduction
Essential Process Requirements
  • Reduces bioburden
  • Protects downstream chromatography and UF/DF steps
  • Maintains yield of dilute protein and preserves purity
  • Sterilizing-grade filtration recommended
Recommended FilterFilter Characteristics

Single-layer Durapore
0.22 µm PVDF Filters

Cartridge Filters

Optiseal Cartridge Filters

Opticap Capsule Filters

Optiseal Capsule Fitlers
  • Sterilizing-grade low-protein binding PVDF membrane
  • 100% Integrity testing to ensure performance
  • Can be integrity testable on-site
  • Although 0.22 µm is typical for this application, Durapore filters are available in several pore sizes and, in single-layer or multi-layer configurations to accommodate the degree of protection required for the downstream process and the plugging characteristics of the fluid. Choice should be based on small-scale testing.

Millipore Express SHC
0.5 µm + 0.2 µm PES Filters

Cartridge Filters

Opticap Capsules

Optiscale Capsules
  • Sterilizing-grade PES membrane providing broad chemical compatibility across a wide pH range (1–14)
  • Robust construction validated for multiple SIP cycles
  • 100% integrity tested to ensure quality
  • Asymmetric pore structure delivers extremely high flow rates at low pressure drop
  • Can be integrity tested on-site
  • Although double-layer 0.5 µm + 0.2 µm (SHC) is typical for this application, single-layer 0.2 µm (SHF) filters are available. The degree of protection required for the downstream process and the plugging characteristics of the fluid will guide this selection. Choice should be based on small-scale testing.