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Protein a resin

Manufactured by GE Healthcare
Sourced in United Kingdom, United States

Protein A resin is an affinity chromatography medium used for the purification of antibodies and antibody-based products. It consists of Protein A, a bacterial protein with a high affinity for the Fc region of immunoglobulins, immobilized on a solid support matrix. This resin enables the selective capture and isolation of antibodies from complex mixtures, such as cell culture supernatants or serum samples.

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19 protocols using protein a resin

1

Monoclonal Antibody and Fab Production

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Antibodies and Fab fragments were produced as previously described17 (link). Briefly, heavy and light chain plasmids (IgG format) containing secretion signals were co-transfected in Expi293F cells (ThermoFisher) using Turbo293 transfection reagent (Speed Biosystem). Cells were incubated for 1 day at 37 °C, followed by 4 days at 37 °C. All subsequent steps were performed at 4 °C. Supernatant was collected by centrifugation and loaded onto Protein A resin (GE Healthcare) pre-equilibrated with PBS. Bound antibodies were washed with 50 ml of PBS and eluted dropwise in 1 mL fractions with Pierce IgG Elution buffer (Pierce). Elution was neutralized with 1 M Tris-Cl, pH 8.0 (final concentration 0.1 M). Fractions with highest A280 absorption were pooled and dialyzed overnight against PBS. Dialyzed protein was concentrated to ~10 mg/mL, filter sterilized, and kept at 4 °C until needed. For the production of Fab fragment, the purified antibodies were incubated with HRV-3C protease (Millipore-Sigma) overnight at 4 °C. Cleavage reaction was loaded onto Protein A resin (GE Healthcare), and flow-through was collected. Fabs were purified by size-exclusion chromatography on a Superdex 200 16/60 column in PBS. Fractions corresponding to Fab were pooled, concentrated to ~5 mg/mL, filter sterilized, and kept at 4 °C until needed.
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2

Production of Human Monoclonal Antibodies

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All human monoclonal antibodies were produced according to the procedure reported previously (Anami et al., 2017 (link); Shi et al., 2014 (link)). Briefly, free style HEK-293 human embryonic kidney cells (Invitrogen) were transfected with a mammalian expression vector encoding for the human IgG1 kappa light chain and full-length heavy chain sequences (based on variable sequences of cetuximab, depatuxizumab, ortrastuzumab). The transfected HEK-293 cells were cultured in a humidified cell culture incubator at 37°C with 8% CO2 and shaking at 150 rpm for 7 days before harvesting the culture medium. The antibody secreted into the culture medium was purified using Protein A resin (GE Healthcare).
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3

Antibody Expression and Purification

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Candidate antibodies were expressed with Expi-CHO Expression system(gibco) for 12days and the supernatant was harvested and purified by protein A resin (GE healthcare). The antibodies were further purified by Q FF (GE healthcare) and Capto S ImpAct (GE healthcare) sequentially and then changed to buffer containing 10 mM CH3COONa·3H2O, 30 mM NaCl, 5% sucrose, 0.03% tween-20, pH6.0.
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4

Affinity-based Purification and Characterization of Monoclonal Antibodies

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HCCF samples were purified by bench-scale affinity column chromatography using a protein A resin (GE Healthcare), standard protein A buffers, and gravity-drip columns. The resultant pools were titrated to pH 5.0 and then processed via cation exchange chromatography (Life Technologies), with proprietary buffers and gravity-drip columns. These pools were then concentrated to ~150 mg/mL using 50 kDa molecular weight cutoff centrifugal filters (UFC905024, Millipore), and buffer-exchanged into proprietary formulation buffer without surfactant to create “final pools” for color analysis and mAb concentration quantification. For qualitative color observation, final pools were imaged prior to removal from filtration devices. Final pools were then transferred from the filtration device into microcentrifuge or cryo-storage tubes and stored at 2–8 °C prior to quantification of mAb concentration and color.
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5

Anti-LILRB3 Antibody Production

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Human anti-LILRB3 antibodies were expressed in mammalian cells (HEK293F) and purified using affinity chromatography with Protein A resin. Briefly, equal molar amounts of heavy-chain and light-chain plasmids were co-transfected into HEK293F cells for transient expression of antibodies. Supernatants were harvested after 7 days in culture, and IgGs were purified with Protein A resin (GE Healthcare).
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6

Production of Human Monoclonal Antibodies

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All human monoclonal antibodies were produced according to the procedure reported previously (Anami et al., 2017 (link); Shi et al., 2014 (link)). Briefly, free style HEK-293 human embryonic kidney cells (Invitrogen) were transfected with a mammalian expression vector encoding for the human IgG1 kappa light chain and full-length heavy chain sequences (based on variable sequences of cetuximab, depatuxizumab, ortrastuzumab). The transfected HEK-293 cells were cultured in a humidified cell culture incubator at 37°C with 8% CO2 and shaking at 150 rpm for 7 days before harvesting the culture medium. The antibody secreted into the culture medium was purified using Protein A resin (GE Healthcare).
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7

LILRB1, MDB1, and RIFIN Protein Production

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LILRB1 D3D4, antibody MDB1 and RIFIN genes were synthesized and subcloned (GenScript, NJ) into pVRC8400 vectors, with HRV3C cleavable His or Fc tag. DNAs of RIFIN with either LILRB1 or MDB1 were co-transfected into Expi293 Gnti- cells (Thermo Fisher) using Turbo293 transfection reagent (Speed BioSystems). Six days post transfection, culture supernatants were harvested, and affinity purified with cOmplete™ His-Tag Purification Resin (Roche) or protein A resin (GE) by following manufacture’s protocols.
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8

Protein A-based IgG Purification Protocol

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Immunised rabbit terminal serum was purified using protein A resin (GE Healthcare, Chalfont St. Giles, Buckinghamshire, UK). Protein A-Sepharose beads (Sigma Aldrich, Gillingham, UK) were added to a 20 mL column and washed with 5× 10 mL PBS. Debris in the terminal serum was removed by filtration prior to addition to the column. The resin was re-suspended and mixed with the serum and left to mix gently on a roller overnight at 4 °C. The serum and resin were re-added to the column and the flow-through collected. The resin was washed 2× 50 mL PBS and antibodies eluted with 0.1 M sodium citrate (pH 3.5). 12× 8 mL fractions were collected in 1.2 mL 2 M Tris-HCl (pH 8.4) for pH neutralization (Sigma Aldrich, Gillingham, UK). Fractions containing antibodies were then pooled, buffer exchanged with PBS and concentrated using 10 kDa molecular weight cut off filters (Amicon; Sigma Aldrich, Gillingham, UK). Total IgG concentration was determined by absorbance at 280 nm using an A280 nanodrop (ThermoFisher Scientific, Loughborough, UK).
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9

Generating Anti-Insulin Fab Fragments

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We used an anti-insulin Fab, an antigen binding fragment of antibodies, as a model. The mouse monoclonal antibody against human insulin was developed by conventional hybridoma technology from Sysmex Corporation [14] (link). All mutants in framework region 3 (FR3) were generated by site-directed mutagenesis using a KOD -Plus- Mutagenesis Kit (Toyobo) in accordance with the manufacturer's protocol.
Antibodies were expressed using the pcDNA 3.4 TOPO expression vector (Life Technologies) and Expi293TM expression system (Life Technologies). Cell culture supernatant was filtered through a 0.8-μm-pore-size filter (ADVANTEC) and antibodies in the filtered supernatant were added to protein A resin (GE Healthcare). After washing with phosphate-buffered saline (PBS), antibodies were eluted with 0.1 M glycine-HCl (pH 2.7), neutralized with 100 mM Tris-HCl (pH 8.0), and dialyzed against PBS.
Fabs were prepared by using Mouse IgG1 Fab and F(ab′)2 Preparation Kits (Pierce). Eluted Fabs were further purified with size-exclusion chromatography using Superdex 200 Increase 10/300GL (GE Healthcare) in PBS.
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10

Recombinant RBD and ACE2 Protein Production

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The genes encoding the SARS-CoV-2 S protein RBD (GenBank: QHR63250.2, residues 319–541), SARS-CoV S protein RBD (GenBank: AAP30030.1, residues 306–527), and MERS-CoV S protein RBD (GenBank: AFS88936.1, residues 377–588) were constructed in the expression vector pCAGGS. The chimeric RBDs were also constructed as recently reported5 (link). The constructs contained a signal peptide at the N-terminus and an IgG1 Fc fragment at the C-terminus. In addition, a thrombin site was inserted between the RBD and Fc fragments. If there is no special indication, RBD indicates the SARS-CoV-2 RBD. Using the same strategy, the encoding recombinant hACE2 (GenBank: NP068576.1, residues 19–615), hACE2-Fc, was also constructed for expression. All proteins were prepared as previously described46 (link). Briefly, the plasmids were transfected into FreeStyle 293 cells (293F). After five days, the supernatant was collected and purified with Protein A resin (GE Healthcare). The purified proteins were concentrated with a 10-kDa centrifugal filter device (Millipore), and the concentrations were measured by a NanoPhotometer N60 (Implen) with the corresponding extinction coefficient. In addition, part of the purified RBD-Fc protein of SARS-CoV-2 was further digested by thrombin (Sigma-Aldrich) to obtain isolated RBD without the Fc fragment.
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