Standard Operating Procedure for Buffer Exchange Using TFF in Biosimilar Manufacturing
| Department | Biosimilars |
|---|---|
| SOP No. | SOP/BS/158/2025 |
| Supersedes | SOP/BS/158/2022 |
| Page No. | Page 1 of 10 |
| Issue Date | 04/05/2025 |
| Effective Date | 06/05/2025 |
| Review Date | 04/05/2026 |
1. Purpose
To define the procedure for performing buffer exchange of biosimilar monoclonal antibody (mAb) intermediates using tangential flow filtration (TFF) systems to enable downstream purification or formulation compatibility.
2. Scope
This SOP applies to all operations involving TFF-based buffer exchange processes in downstream processing (DSP) of biosimilar proteins, using either reusable or single-use TFF systems.
3. Responsibilities
- Production: Set up, execute buffer exchange cycles, and document process parameters.
- QA: Review TFF logs, approve buffer preparations, and verify completion of exchange.
- Engineering: Ensure TFF skid maintenance and calibration.
4. Accountability
The Downstream Manufacturing Manager is accountable for GMP-compliant execution of TFF buffer exchange operations and ensuring data integrity.
5. Procedure
5.1 Pre-Operational Setup
- Verify TFF skid status, tubing integrity, and membrane compatibility with product.
- Document membrane type, lot number, and molecular weight cutoff (MWCO) in Annexure-1.
- Sanitize system with 0.1 M NaOH and flush with WFI to achieve neutral pH.
- Prime the system with process buffer to ensure wetting of membrane.
5.2 Buffer Preparation
- Prepare target buffer (e.g., 20 mM Histidine, 150 mM NaCl, pH 6.0).
- Filter buffer through 0.22 µm filter into sanitized holding tank.
- Record buffer details in Annexure-2: Buffer Preparation Record.
5.3 Buffer Exchange Operation
- Load product pool into TFF feed tank.
- Set TFF parameters:
- Transmembrane pressure (TMP): 1.0–1.5 bar
- Crossflow rate: 300–500 mL/min (depending on skid capacity)
- Diafiltration volume: Typically 5–8× of retentate volume
- Initiate diafiltration by adding target buffer and removing filtrate simultaneously.
- Monitor conductivity and pH in permeate and retentate until buffer exchange is confirmed.
- Record cycle parameters and sample analysis in Annexure-3.
5.4 Post-Process Steps
- Upon completion, collect retentate for further purification or formulation.
- Flush membrane with WFI or sanitizing solution and clean system as per cleaning SOP.
- Inspect pressure gauges, flow sensors, and record cleaning data.
5.5 Acceptance Criteria
- Buffer exchange is complete when:
- Permeate conductivity = target buffer conductivity ±10%
- pH = target buffer ± 0.2 units
6. Abbreviations
- TFF: Tangential Flow Filtration
- MWCO: Molecular Weight Cut-Off
- TMP: Transmembrane Pressure
- DSP: Downstream Processing
7. Documents
- TFF Setup and Membrane Log – Annexure-1
- Buffer Preparation Record – Annexure-2
- Buffer Exchange Process Record – Annexure-3
8. References
- ICH Q8 – Pharmaceutical Development
- WHO TRS 999 – GMP for Biotherapeutics
- OEM TFF Skid Operating Manual – Sartorius, Pall, or equivalent
9. SOP Version
Version: 2.0
10. Approval Section
| Prepared By | Checked By | Approved By | |
|---|---|---|---|
| Signature | |||
| Date | |||
| Name | |||
| Designation | |||
| Department |
11. Annexures
Annexure-1: TFF Setup and Membrane Log
| Date | Skid ID | Membrane Type | MWCO | Lot No. | Sanitized By |
|---|---|---|---|---|---|
| 04/05/2025 | TFF-102 | Hollow Fiber | 30 kDa | HF-3071 | Ajay Verma |
Annexure-2: Buffer Preparation Record
| Date | Buffer Name | pH | Conductivity | Filter Lot No. | Prepared By |
|---|---|---|---|---|---|
| 04/05/2025 | 20 mM Histidine + 150 mM NaCl | 6.0 | 12.1 mS/cm | FL-2204 | Sunita Reddy |
Annexure-3: Buffer Exchange Process Record
| Time | TMP | Flow Rate | Conductivity | pH | Remarks | Operator |
|---|---|---|---|---|---|---|
| 14:15 | 1.2 bar | 400 mL/min | 11.9 mS/cm | 6.1 | Exchange complete | Ajay Verma |
Revision History:
| Revision Date | Revision No. | Revision Details | Reason for Revision | Approved By |
|---|---|---|---|---|
| 04/05/2025 | 2.0 | Added diafiltration volume specification and post-process checks | Process control enhancement |