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Akta avant

Manufactured by Cytiva

The AKTA Avant is a chromatography system designed for purification of proteins, peptides, and other biomolecules. It is a versatile and automated platform that can perform a variety of chromatographic techniques, including ion exchange, size exclusion, and affinity chromatography. The AKTA Avant is equipped with advanced software and control systems to ensure accurate and reproducible results.

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5 protocols using akta avant

1

Transient Expression of Recombinant Antibodies

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Genes encoding heavy chains and light chain were inserted separately into pcDNA3.4 and amplified in E. coli DH5α. PureLink™ HiPure Plasmid Miniprep Kit (Invitrogen) was used for low endotoxin plasmid preparation. Monoclonal antibodies were transiently expressed by co-transfecting ExpiCHO-S cells (ThermoFisher) with heavy chain and light chain plasmids using an ExpiCHO™ Expression System (Gibco). Cell culture was harvested after an 8–14 day of incubation at 37 °C with humidified atmosphere of 8% CO2 with shaking. Full-length IgG was obtained by affinity purification utilizing a Protein A chromatography column (GE Healthcare) in AKTA avant (Cytiva). For long-term storage, antibodies were kept in a solution containing 10 mM Histidine-HCl, 9% trehalose, and 0.01% polysorbate 80.
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2

Scalable AAV6 Purification using Capto AVB

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An AAV6 cell paste slurry was generated using standard cell culture techniques and stored at −80°C. Capto AVB resin was sourced from Cytiva. C0SP filters were obtained from Millipore‐Sigma. Sartopore 2 XLG, 0.8/0.2um filters were obtained from Sartorius Stedim Biotech GmbH (Gottingen, Germany).
For detergent lysis, the AAV6 cell paste was diluted to a 10% (w/w) slurry with 20 mM Tris, 200 mM NaCl, 2 mM MgCl2, pH 7.5. A 10% (w/w) detergent stock solution was spiked into cell slurry to bring the final detergent concentration to 0.5% (v/w). Benzonase was spiked to 10 U/ml into cell slurry mixture and mixed slowly at room temperature for 1 h.
AAV purification was performed using a Capto AVB affinity column. Purification was controlled by Unicorn 7.0 software on an AKTA Avant purchased from Cytiva. A C0SP POD filter was flushed with 20 mM Tris, 500 mM NaCl, 2 mM MgCl2, pH 7.5. 10% AAV cell lysate was clarified with C0SP followed by Sartopore 2 XLG, 0.8/0.2um filter. The Capto AVB column was equilibrated with 20 mM Tris, 200 mM NaCl, 2 mM MgCl2, pH 7.5 for 3 column volumes. Clarified cell lysate was loaded with residence time of 6 min. The column was re‐equilibrated with 20 mM Tris, 200 mM NaCl, 2 mM MgCl2, pH 7.5 for 4 CV. Product was eluted from column with 50 mM citric acid, 500 mM NaCl, 2 mM MgCl2, pH 2.5. Eluate pH was adjusted to pH 8.0 with 1 M Tris/HCl, pH 8.0.
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3

Protein A Lifetime Studies

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The aliquots from the depth filtration experiments above were used for the Protein A lifetime studies. For each condition, 100 cycles were performed. The studies were conducted using a 1 ml HiTrap column prepacked with MabSelect Sure LX and the AKTA Avant (Cytiva) chromatography system. Eluates were collected every cycle and neutralized with 200 μl 2 M Tris‐Base. Precipitation was observed in some loading material and was removed by centrifugation at 500 rpm for 5 min. All feeds were clarified using a 0.2 μm syringe filter before loading.
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4

Optimizing S_dF_2P Protein Purification

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Based on promising S_dF_2P binding and elution pattern data from the resin screen, resins were selected for further screening and development. Each resin was tested at pH 7.0 and pH 8.0 on an AKTA Avant (Cytiva, Picastaway, NJ), mimicking the process parameters from the resin screen (i.e., 2-min residence time) with the loading density decreased to 50 g/L-r. All elution fractions were analyzed by SDS-PAGE. Following the initial screen, ToyoPearl QAE-550C (Tosoh Biosciences, King of Prussia, PA), POROS 50 D (ThermoFisher, Waltham, MA), and GigacapQ 650 M (Tosoh Biosciences, King of Prussia, PA) were selected and further tested at pH 6.5 in an MES buffer system and pH 7.0 in a Sodium Phosphate buffer system to assess the impact of lower pH and buffer system on recovery (as measured by Octet titer) and purity (measured by HP-SEC) while including a head-to-head comparison to previous experiments performed in Sodium Phosphate pH 7.0. Subsequently, POROS 50 D was tested at pH 6.5 in both buffer systems listed above to investigate the impact each factor individually (i.e., buffer system and pH) (Figure S3).
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5

Optimizing Ion Exchange Chromatography

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Based on promising S_dF_2P binding and elution pattern data from the resin screen, resins were selected for further screening and development. Each resin was tested at pH 7.0 and pH 8.0 on an AKTA Avant (Cytiva, Picastaway, NJ), mimicking the process parameters from the resin screen (i.e., 2-minute residence time) with the loading density decreased to 50 g/L-r. All elution fractions were analyzed by SDS-PAGE. Following the initial screen, ToyoPearl QAE-550C (Tosoh Biosciences, King of Prussia, PA), POROS 50 D (ThermoFisher, Waltham, MA), and GigacapQ 650M (Tosoh Biosciences, King of Prussia, PA) were selected and further tested at pH 6.5 in an MES buffer system and pH 7.0 in a Sodium Phosphate buffer system to assess the impact of lower pH and buffer system on recovery (as measured by Octet titer) and purity (measured by HP-SEC) while including a head-to-head comparison to previous experiments performed in Sodium Phosphate pH 7.0. Subsequently, POROS 50 D was tested at pH 6.5 in both buffer systems listed above to investigate the impact each factor individually (i.e., buffer system and pH) (Figure S3).
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