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Kta purifier system

Manufactured by Cytiva
Sourced in United Kingdom, Sweden, United States

The Äkta purifier system is a versatile liquid chromatography platform designed for protein purification and preparative-scale separations. It offers precise control and monitoring of critical parameters such as flow rate, pressure, and conductivity to ensure reliable and reproducible purification results.

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18 protocols using kta purifier system

1

Purification and Characterization of L. lactis Recombinant Proteins

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Recombinant L. lactis were grown until OD600 = 0.6 and induction with 10 ng/ml of nisin (Sigma) was performed during 3 h. The cells were harvested and the supernatant was concentrated using a 100 kDa cut-off membrane. The resulting protein fraction was subjected to an anion exchange chromatography (Mono-Q 5/50GL, GE Healthcare). Purification was achieved by a size exclusion chromatography step (S200 column, Amersham Bioscience) using an ÄKTA purifier system (Amersham Biosciences). The used buffer was 100 mM sodium acetate (pH 5.0) and elution fractions were 0.5 ml.
The harvested L. lactis cells were washed twice with 100 mM sodium acetate buffer (pH 5.0) and disrupted by glass beads (diameter of 212–300 µm, v/v, Sigma). Crude cell extract were recovered by centrifugation (30,000×g, 20 min at 4 °C).
Lactobacillus sakeil-AI produced in E. coli strain (MRS36) was over-expressed and purified as previously reported [30 (link)].
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2

Purification of Bacteriocin from V. fluvialis

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V. fluvialis LMGT 4216 was cultivated in 1 L of BHI broth at 30°C for 24 h. Cells were removed by centrifugation (10,000 × g for 30 min at 4°C), and the bacteriocin was precipitated from the culture supernatant with ammonium sulfate (60% saturation at 4°C overnight). The precipitate was harvested by centrifugation (15,000 × g for 40 min at 4°C), redissolved in 700 mL of distilled water, and adjusted to pH 3.5 with 1 M hydrochloric acid. The sample was applied to a Hi-Prep 16/10 SP-XL column (GE Healthcare, Chicago, IL, USA). Unbound material was washed from the column with 150 mL of 25 mM sodium citrate-phosphate buffer (pH 3.5). The bacteriocin was eluted with 100 mL of 0.5 M sodium chloride, and the eluate was then applied to a 1-mL Resource RPC column (GE Healthcare) connected to an Äkta purifier system (Amersham Pharmacia Biotech, Amersham, UK). The column was previously equilibrated with 0.1% (vol/vol) trifluoroacetic acid (TFA), and the bacteriocin was eluted from the column using a linear gradient (40 column volumes [CV]) of isopropanol containing 0.1% (vol/vol) TFA at 1 mL/min.
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3

Characterization of Anti-Biofilm Compounds from K. pneumoniae

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The planktonic extract from K. pneumoniae MGH 78578 at 10 g.L−1 in 50 mM phosphate buffer (pH 7) supplemented with NaCl (150 mM) was filtered (at 0.45 µm) and analyzed by SEC at room temperature. The column used was a Superdex 200 column (1.5 cm×50 cm), (GE Healthcare, Sweden) coupled to an ÄKTA Purifier system (Amersham Pharmacia Biotech, Sweden) and eluted with a 50 mM phosphate buffer (pH 7) supplemented with NaCl (150 mM) at a flow rate of 0.5 mL.min−1. Fractions of 0.5 mL were collected and the sugar content was determined by phenol–sulphuric acid method. Each fraction collected was assayed by the magnetic beads-mediated agglutination assay to determine the anti-biofilm activities with dialyzed planktonic extract from K. pneumoniae.
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4

Generating Antibodies for Maize Proteins

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To generate antibody specific to ZmMADS47, cDNA fragment containing the first 400 bp from 5’ ORF was cloned into the pGEX-4T-1 GST-tagged vector by BamHI/XhoI sites. Recombinant protein were expressed in bacterial strain BL21 (DE3) (Novagen) by adding 500 μM IPTG (Dingguo) to a final concentration of 0.4 mM under 25°C, and purified using the ÄKTA purifier system (GE Healthcare). The antibody was prepared by Shanghai ImmunoGen Biological Technology in rabbit according to standard protocol. To generate antibodies specific to O2, O2 ORF was amplified and cloned into NotI/NcoI sites of pET-32a (Novagen). His-O2 fused protein was induced in E. coli strain Rosetta (DE3), and purified by the ÄKTA purifier system (Amersham Biosciences). The antibodies were prepared by Shanghai ImmunoGen Biological Technology according to standard protocol. The 19-kD, 22-kD α-zein, 16-kD, 27-kD, 50-kD γ-zein, 14-kD β-zein, 10-kD δ-zein specific antibodies were produced according to the protocol published before [4 (link)].
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5

Two-step Fc Fusion Protein Purification

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ÄKTA-purifier system (Amersham Biosciences, USA), an automated two-step purification method for Fc fusion proteins, was selected based on capture by affinity chromatography followed by “polishing” by gel filtration. Affinity chromatography on HiTrap recombinant protein A (GE Healthcare, USA) was selected due to its high selectivity for IgG1. Appropriate conditions for binding and elution buffers have been amended. Proteins were polished by gel filtration on HiLoad 16/60 Superdex 200 size exclusion columns.
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6

Purification of Hexahistidine-Tagged PaHigA

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Bacterial cells were grown to mid-log phase (OD600 nm = ∼0.8) in LB media at 37°C in the presence of 50 μg/mL Kanamycin and 100 μg/mL chloroamphenicol. Induction of the culture was then carried out with 0.3 mM isopropyl-1-thio-β-D-galactopyranoside (IPTG) at 20°C. Cells were pelleted after 20 h by centrifugation at 8, 000 rpm for 10 min at 4°C. The cell pellet was resuspended in buffer A [20 mM Tris, 300 mM NaCl, 5% (v/v) glycerol, and 1 mM PMSF, pH 8.0] and lysed by ultrasonification on ice. The cell debris and membranes were pelleted by centrifugation at 15,000 rpm (R20A2 rotor, Hitachi high-speed refrigerated centrifuge R21GIII) for 45 min at 4°C. The soluble C-terminally hexahistidine-tagged PaHigA was purified by affinity chromatography with nickel-nitrilotriacetic acid resin (Bio-Rad). Untagged proteins were removed with buffer A containing 50 mM imidazole. Recombinant PaHigA was then eluted with buffer A containing 250 mM imidazole. The protein was further purified by gel filtration (Superdex 200, GE Healthcare) equilibrated in buffer B [20 mM Tris, 300 mM NaCl, 5% (v/v) glycerol, pH 8.0] using an ÄKTA Purifier System (Amersham).
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7

Purification of Bacteriocin from V. fluvialis

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V. fluvialis LMGT 4216 was cultivated in 1 L of BHI broth at 30°C for 24 h. Cells were removed by centrifugation (10,000 × g for 30 min at 4°C), and the bacteriocin was precipitated from the culture supernatant with ammonium sulfate (60% saturation at 4°C overnight). The precipitate was harvested by centrifugation (15,000 × g for 40 min at 4°C), redissolved in 700 mL of distilled water, and adjusted to pH 3.5 with 1 M hydrochloric acid. The sample was applied to a Hi-Prep 16/10 SP-XL column (GE Healthcare, Chicago, IL, USA). Unbound material was washed from the column with 150 mL of 25 mM sodium citrate-phosphate buffer (pH 3.5). The bacteriocin was eluted with 100 mL of 0.5 M sodium chloride, and the eluate was then applied to a 1-mL Resource RPC column (GE Healthcare) connected to an Äkta purifier system (Amersham Pharmacia Biotech, Amersham, UK). The column was previously equilibrated with 0.1% (vol/vol) trifluoroacetic acid (TFA), and the bacteriocin was eluted from the column using a linear gradient (40 column volumes [CV]) of isopropanol containing 0.1% (vol/vol) TFA at 1 mL/min.
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8

Size Exclusion Chromatography Optimization

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All size exclusion chromatography (SEC) experiments were carried out using an Äkta purifier system (Cytiva) with indicated buffers and columns. 10/300 columns were loaded with max. 8 mg protein with 0.5 ml/min flow rate at 4 °C. 16/600 columns were loaded with max. 80 mg protein with 1 ml/min flow rate at 4 °C.
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9

Size Exclusion Chromatography Protein Purification

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Size exclusion chromatography (SEC) experiments were carried out using an Äkta purifier system (Cytiva) and a Superdex 75 10/300 column (Cytiva). The column was loaded with max. 10 mg protein with a flow rate of 0.5 ml/min at 4 °C using the indicated buffers.
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10

Size-Exclusion Chromatography of Purified Proteins

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SEC was carried out at 12 °C, using an Äkta purifier system (Cytiva, Munich, Germany) and Increase Superose 6 5/150 or 3.2/300 columns (Cytiva, Munich, Germany). The columns were equilibrated in sterile-filtrated, degased and pre-cooled buffer (100 mM NaCl, 20 mM HEPES, pH 7.4) before injecting the affinity purified protein samples. Flow rate was 0.15 mL/min for Superose 6 5/150 and 0.05 mL/min for Superose 6 3.2/300. UV absorbance was recorded at 280 nm and data were plotted using GraphPad Prism (v.9.5).
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