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Kta purifier 10 system

Manufactured by GE Healthcare
Sourced in Sweden, United Kingdom, Germany

The ÄKTA purifier 10 system is a liquid chromatography system designed for protein purification. It features a modular design and can be configured with various components to meet specific research or production needs. The system provides precise control over flow rate, pressure, and other parameters to ensure efficient and reliable protein separation and purification.

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21 protocols using kta purifier 10 system

1

Inducible Production of mIL-6-RFP-Fc Protein

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Stable HEK293 Flp-In/T-Rex cells (Invitrogen) for the inducible production of mIL-6-RFP-Fc were generated with the Flp-In system using 250 μg/ml hygromycin B (Invivogen) and 15 μg/ml blasticidin (Invivogen). Protein expression was induced in serum-free medium with 400 ng/ml doxycycline (Sigma-Aldrich) for 72 h. Harvested conditioned media were cleared through centrifugation, passed through a 0.20 μm sterile-filter and afterwards loaded onto an ÄKTA Purifier 10 system (GE Healthcare, Chalfont St. Giles, UK) for affinity purification on a 1 ml Protein A Sepharose Column (#89924, Thermo Fischer, Waltham, MA). The column was washed with 20 mM sodium phosphate buffer (pH 7). mIL-6-RFP-Fc was eluted in fractions of 1 ml using 12.5 mM citric acid (pH 2.7) and neutralized immediately by adding 50 μl of 2 M Tris/HCl (pH 8). Protein containing fractions were quantified using a BCA colorimetric assay (#500-0006, Bio-Rad, Munich, Germany) following manufacturer’s instruction. Protein containing fractions were pooled and dialyzed against PBS.
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2

Protein Size Estimation by Superose 6 Chromatography

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A Superose® 6 Increase 3.2/300 column (Sigma-Aldrich Chemie GmbH, Taufkirchen, Germany), equilibrated with reaction buffer, was loaded with 30 µl of a 10 µM protein solution. Proteins were eluted using an ÄKTA purifier 10 system (GE Healthcare, Munich, Germany) at 7 °C and a flow rate of 0.03 ml/min. The standard proteins thyroglobulin (669 kDa) Ferritin (440 kDa), Aldolase (158 kDa), Conalbumin (75 kDa) and Ovalbumin (44 kDa) (Sigma-Aldrich Chemie GmbH, Taufkirchen, Germany) were used for protein mass estimation. Chromatograms were recorded using the software UNICORN (version 5.10).
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3

Recombinant Production and Purification of OAS1

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Human OAS1 (p41/E16 isoform) was expressed in E. coli BL21(DE3) as a SUMO-OAS1 fusion protein from vector pE-SUMOpro (LifeSensors). Cells for OAS1 expression were grown in Lysogeny Broth (LB) medium at 37°C to an OD600 of 0.4, protein expression induced with 0.1-mM isopropyl β-D-1-thiogalactopyranoside and growth continued overnight at 20°C. Cells were lysed by sonication in 50-mM Tris-HCl buffer (pH 8.0) containing 150-mM NaCl, 10-mM imidazole, 1-mM DTT and 10% (v/v) glycerol. Fusion protein was purified by sequential Ni2+-affinity and heparin-affinity chromatographies on an ÄKTA Purifier10 system (GE Healthcare). The fusion protein was then dialyzed overnight against SUMO cleavage buffer and cleaved with SUMO protease according to the manufacturer's instructions. Cleavage with SUMO protease leaves a native N-terminus, an important feature of the system as amino acid additions to the N-terminus of OAS1 have been reported to interfere with activity (27 (link)).
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4

Carbohydrate and Protein Purification

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Delipidated vesicle and matrix pellets containing carbohydrates and proteins were washed twice with acetone, dried under a stream of nitrogen, and reconstituted in 3 ml of 20 mM bis-Tris/HCl (pH 6.5) loading buffer. Aliquots were chromatographically desalted on a HiPrep 26/10 Desalting column (GE Healthcare Life Sciences, Uppsala, Sweden) and then separated on an anion exchanger HiPrep 16/10 DEAE FF column (GE Healthcare Life Sciences) equilibrated with 20 mM bis-Tris/HCl (pH 6.5). Carbohydrate positive flow-through fractions were pooled together, lyophilized, resuspended in 15% acetonitrile in 150 mM ammonium bicarbonate, and applied to gel filtration on a HighPrep 16/60 Sephacryl S-300 HR column (GE Healthcare). All chromatographic separation steps were performed at room temperature on the high-performance liquid chromatography ÄKTA-Purifier 10 system (GE Healthcare Life Sciences).
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5

Protein Size Characterization via SEC

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The samples (200 µL) were separated by size on a fast protein liquid chromatography system (GE ÄKTA Purifier 10 System with Monitor UV-900 and Sample Pump P-900). The SEC was carried on a calibrated Superdex 75 Increase 10/300 GL column at room temperature with a flow of 0.5 mL/min PBS buffer at pH 7.5 over 1.5 column volumes (CVs). The column was equilibrated over 2 CVs (1 CV = 24 mL) of running buffer before the sample injection with monitoring at 215, 280, and 663 nm. The molecular weight of each sample was calculated using a linear calibration curve of partition coefficient Kav Kav=retentionvolumeVoidvolumeColumnvolumeVoidvolume
versus log(MW) generated by standard proteins; Conalbumin (75 kDa), Ovalbumin (43 kDa), Carbonic Anhydrase (29 kDa), Ribonuclear (13.7 kDa), and Aprotinin (6.5 kDa) (Fig. 1). The Stoke’s radius (Rs) of each sample was calculated using a linear calibration curve of log(Kav) versus Rs of standard proteins; Conalbumin (36.4 Å), Ovalbumin (30.5 Å), Carbonic Anhydrase (23 Å), Ribonuclear (16.4 Å), and Aprotinin (13.5 Å) (Supplementary Fig. 22d).
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6

Purification of Human IgG from Sera

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Human sera were obtained from healthy volunteers aged between 30 and 50 years. Healthy donors were recruited at the University of Heidelberg (Germany), after giving their written informed consent. The protein G purified serum IgG was obtained from a clinical study approved by the appropriate local Ethics Committee and Institutional Review Board of the University of Heidelberg (S-040). 100 µL-aliquots were diluted with 900 µL PBS and applied on a HiTrap Protein G HP column (1 mL) using an ÄKTA purifier 10 system (GE Healthcare, Munich Germany) at 4 °C and a flow rate of 0.5 mL/min. After washing with 10 mL PBS, pure IgG fractions were eluted with 100 mM glycine pH 2.6 and immediately neutralized with 1.5 mM Tris-HCl (pH 8.8). Purity of the obtained samples was checked by SDS electrophoresis and Coomassie staining.
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7

Recombinant Collectin Purification and Protein Expression

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rcMBL was expressed and purified as previously described (Zhang et al., 2016b ). In brief, the pFRT vector containing the cMBL gene was transfected into HeLa-R19 cells and the culture supernatant was harvested at 5 days post-transfection. rcMBL was purified by affinity chromatography using mannan-coated beads, followed by gel filtration using an ÄKTA purifier10 system (GE Healthcare Bio Sciences, Sweden), that was equipped with a Hiload 16/60 Superdex 200 PREP GRADE column. Recombinant S1 protein (M41 S1) was expressed as described previously (Wickramasinghe et al., 2011 (link)).
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8

Overproduction and Purification of IolR-His6

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IolR-His6 was overproduced from the plasmid pET28b-IolR in E. coli BL21 (DE3) and S. Typhimurium strain 140282 (link). Overnight culture of the strains were diluted 1:100 into 400 ml of LB medium supplemented with 50 μg/ml kanamycin and incubated for 3 h at 37 °C with rotation at 180 rpm. At an OD600 of 0.6, IolR production was induced by adding 0.1 mM isopropyl-β-D-1-thiogalactopyranoside (IPTG). After an overnight incubation at 37 °C and 180 rpm, the cells were harvested by centrifugation at 4 °C and 7500 rpm for 20 min. The pellets were each resuspended in 5 ml of native lysis buffer (50 mM NaH2PO4, 300 mM NaCl and 10 mM imidazole at pH 8.0) and lysed by three passages through a French press (SLM Aminca Instruments, Rochester, NY, USA) at 900 psi; residual cell debris was removed twice by centrifugation at 4 °C and 9000 rpm for 15 min. Following filtration, IolR was isolated using a HisTrap HP colunm with an ÄKTA purifier 10 system (GE Healthcare, Little Chalfont, UK). The protein concentration was determined using RotiQuant solution (Carl, Roth GmbH, Karlsruhe, Germany) according to the Bradford method32 (link). The purity of the eluted fractions was analysed by separation on a 15% sodium dodecyl sulfate (SDS)-PAA gel.
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9

Determining Protein Native Molecular Mass

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The native molecular mass of the purified proteins was determined by gel filtration chromatography using a Superdex 200 10/300 GL column (GE Healthcare, China) according to the manufacturer’s instructions. The column was pre-equilibrated and eluted with Tris-HCl buffer (50 mM, pH 7.5) containing 0.15 M NaCl at a flow rate of 0.5 mL min−1, which was controlled by an ÄKTA Purifier 10 system (GE Healthcare, China). The standard proteins used for calculating the native molecular mass of enzymes were carbonic anhydrase (30 kDa), bovine serum albumin (67 kDa), alcohol dehydrogenase (150 kDa), catalase (200 kDa), ferritin (440 kDa), and thyroglobulin (669 kDa).
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10

Protein Purification from Bacterial and Mammalian Cells

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Bacteria from expression cultures were suspended in standard binding buffer for Ni-affinity chromatography and lysed by sonification. After clearing of the lysate, the proteins were purified by Ni-affinity chromatography using an ÄKTA purifier 10 system (GE Healthcare, Uppsala, Sweden). Cleavage of the N-terminal His tag was done by using TEV protease (Sigma-Aldrich, St. Louis, MO) according to the manufacturer’s recommendations. Additional purification steps via cation- or anion-exchange chromatography or size exclusion chromatography were performed if necessary. The purity of the recombinant expressed proteins was tested by Coomassie blue-stained SDS-PAGE.
HEK293-derived Fn derivates were purified from the supernatants by gelatin agarose affinity chromatography method as described elsewhere (28 (link)). The success of the purification was proven by dot immunoassay using monoclonal anti-GFP antibody (Abcam, Cambridge, MA).
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