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Biopharma · APPLICATION GUIDE

Concentration & Diafiltration

Compare membrane MWCO, flow path, and operating conditions together to meet recovery and processing time targets.

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FIELD APPLICATION & FLOW

See the application in its industrial setting.

Review product locations and fluid paths.

APPLICATION IN CONTEXT
A feed bag, pump and membrane form a recirculation loop. Permeate is collected separately, while fresh buffer enters the feed bag during diafiltration. 1. Feed/retentate bag; 2. Recirculation pump; 3. TFF membrane module; 4. Permeate collection; 5. Buffer supply
A feed bag, pump and membrane form a recirculation loop. Permeate is collected separately, while fresh buffer enters the feed bag during diafiltration.
  1. Feed/retentate bag
  2. Recirculation pump
  3. TFF membrane module
  4. Permeate collection
  5. Buffer supply

Connections to review

  • 01 → 02 Feed/retentate bag → Recirculation pump
  • 02 → 03 Recirculation pump → TFF membrane module
  • 03 → 01 Retentate return
  • 03 → 04 Permeate
  • 05 → 01 Buffer during DF

This UF/DF example retains the target product in the retentate. Other separation objectives may use a different product outlet.

A conceptual illustration created to explain equipment and application locations. It is not an actual product photograph, installation photograph or piping/wiring design.

Connection principles and operating/test methods

2D PROCESS GUIDE

TFF · Concentration and diafiltration

FluidPermeateRetentate / return
TFF cassette — dimensional product illustration
PRODUCT TYPETFF cassetteIllustrative product form
TFF · Concentration and diafiltrationProduct liquid → Recirculation pump (Fluid); Recirculation pump → UF membrane (Fluid); UF membrane → Permeate (Permeate); UF membrane → Product liquid (Retentate / return); Fresh buffer → Product liquid (Fluid). Retentate recirculates to the feed vessel, while permeate is discharged separately. During DF, add buffer according to the defined strategy and confirm the actual extent of buffer exchange by analysis.FeedFlow along membranePermeateTarget retentionBuffer additionProduct liquidFeed + returnRecirculation pumpFlow controlUF membraneTangential flowPermeatePermeate sideFresh bufferDF stage

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Retentate recirculates to the feed vessel, while permeate is discharged separately. During DF, add buffer according to the defined strategy and confirm the actual extent of buffer exchange by analysis.

These conceptual views explain flow direction. Actual piping, wiring and physical flow rates require a separate design.

01 — PROCESS

Where does each step fit?

Define the intended use and conditions to identify the required role of each item.

01

Screen membranes and flow paths

Compare materials, MWCO, hollow fibers and cassettes, and flow channel dimensions.

02

Concentration and DF

Track flux and quality as TMP, crossflow, temperature, and concentration change.

03

Recovery and scale-up

Review hold-up volume, flushing, final recovery, and flow conditions during scale-up.

02 — SELECTION

What should be selected and verified?

In TFF, liquid flows along the membrane surface and a portion passes through it. Select the membrane and process conditions according to whether the target product must be retained and concentrated or low-molecular-weight components must pass through for buffer exchange.

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Process objectiveStep to reviewSelection evidence
Retention and selectivityMWCO and materialTarget product passage into the permeate, impurity transmission, and actual separation curves
Operating rangeTMP / crossflowFlux saturation, pressure loss, shear, and temperature rise
Concentration and exchange targetsConcentration factor / DF volumesFinal concentration, conductivity, and analysis of residual components
RecoveryModule, piping, and recovery methodHold-up volume, adsorption, dilution during flushing, and preservation of activity

These examples start the application review. Pore size or nominal rating alone does not establish suitability or retention; confirm with the actual process fluid and supplier evidence.

03 — OPERATING CHECKS

Use operating data to identify improvements.

Higher pressure is not always better

Concentration polarization and fouling can cause flux to plateau. Use tests combining TMP and flow rate to establish a stable operating range.

Compare hollow fibers and cassettes

Review flow paths, hold-up volume, shear, and cleaning, sterilization, and scale-up conditions for the target product.

Assess recovery with quality preserved

Measure not only total recovered quantity but also product attributes such as aggregation, degradation, and biological activity.

04 — QUESTIONS

Frequently asked questions

Are membranes with the same MWCO equivalent?

Differences in materials, pore size distribution, flow paths, and test methods can lead to different actual retention and transmission performance.

How is TMP calculated?

A common approximation is (inlet pressure + outlet pressure)/2 − permeate-side pressure. Check the pressure measurement locations in the equipment and the manufacturer’s definition.

05 — APPLICATION REVIEW

Prepare the conditions for a technical discussion.

These details help narrow the configuration and the evidence to review.

Prepare an enquiry
TECHNICAL NOTES

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