Antibody Purification Using Membrane Adsorbers - A membrane adsorber in retention mode can be used efficiently in a commercial antibody manufacturing process. - BioPharm International

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Antibody Purification Using Membrane Adsorbers
A membrane adsorber in retention mode can be used efficiently in a commercial antibody manufacturing process.


BioPharm International Supplements


Performance Evaluation


Table 1. Reproducibility and robustness of the dual Q/S polishing system, as determined by measuring yield and elution conductivity. Yield is expressed as [D]/[PD]%, where D is the amount of antibody dimer recovered after polishing and PD is the amount of antibody dimer submitted for processing. Elution conductivities (MC, mSi/cm) represent values between fraction T collection, and the value in parentheses represents conductivity at the edge of the chromatogram peak.
The initial capture and purification step using Protein A affinity chromatography yields a product with >90% purity, but further polishing is required to reduce impurities and viruses to acceptable levels and conform with regulatory guidelines. The dual Sartobind Q/S disposable system tackles both positively and negatively charged impurities in a single step. The Q membrane is able to remove nearly 400 g of DNA, 1.2 mg of Protein A, and nearly 30,000 EU of endotoxin (Sartobind Q5, surface area 5 cm2 equivalent to a 0.137 mL bed volume). Experiments to test the system for virus removal capacity are in progress.

The reproducibility of these results has been tested by monitoring the yield (calculated as the amount of Teleukin obtained after polishing as a percentage of the input amount) and the elution conductivities of several runs. The results, as presented in Table 1, confirm the robustness of the process. The elution conductivities are highly reproducible both among lots and between runs, and the yield ranges from 82.2 to 99.9%, which shows that the process, when optimized, can recover nearly all of the input product. The Q/S dual adsorber system is therefore suitable as a manufacturing process for this product, and probably all MAbs.

Nanofiltration

This final step in the process is a nanofiltration operation to mechanically remove endogenous or adventitious virus particles <20 nm in diameter. A 4-inch NFP Millipore cartridge filter (Millipore, Billerica, MA) is used for this step, and the efficiency of this device has been confirmed for a sample load up of up to 1.6 g of Teleukin in a volume of up to 6.5 L, loaded at a constant pressure (4 bar) using the Akta Pilot chromatographic system. The filtration flow rate is automatically adjusted by the Akta system to keep the pressure value constant. The flow rate usually ranges from 100 to 300 mL/min and sample recovery after filtration is usually very high (>90%).


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