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Hiload 26 60 superdex 75 gel filtration column

Manufactured by GE Healthcare
Sourced in United States

The HiLoad 26/60 Superdex 75 gel filtration column is a size-exclusion chromatography product used for the separation and purification of proteins, peptides, and other macromolecules. It features a prepacked column with a bed height of 60 cm and a column diameter of 26 mm. The column is designed for high-resolution separations and can be used on a variety of chromatography systems.

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6 protocols using hiload 26 60 superdex 75 gel filtration column

1

Purification and Characterization of Lpg0393 Protein

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The DNA fragments encoding full-length Lpg0393 (GI:52840638) or Lpg0393Δ17 were inserted into the pET22b CPD vector by standard PCR-based cloning methods. This vector was designed to produce these proteins with a C-terminal fusion of the cysteine protease domain (CPD) of the Vibrio cholera MARTX toxin [37 (link)] with a (His)10-tag. Cell lysate was applied onto a gravity flow column containing HisPur Cobalt Resin (Thermo Scientific). The column was washed with Buffer A (20 mM Tris-HCl (pH 7.5), 0.1 M NaCl and 1mM dithiothreitol) and the CPD-(His)10 tag was autolytically cleaved off on this resin by incubation with 100 μM sodium phytate (Sigma Aldrich). The flow-through fraction was further purified using a Hitrap Q anion exchange column (GE Healthcare) and a HiLoad 26/60 Superdex 75 gel filtration column (GE Healthcare) equilibrated with Buffer A. Selenomethionine (SelMet)-labeled Lpg0393Δ17 was obtained by using E. coli B834(DE3) RIL (Novagen), and purified using the same procedure for native Lpg0393Δ17. Final protein sample was concentrated to 20 mg/ml and flash frozen for storage at -80°C.
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2

Recombinant Expression and Purification of Perdeuterated H-FABP

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Perdeuterated H-FABP was recombinantly expressed at the Institut Laue–Langevin (ILL) Deuteration Laboratory in Grenoble, France, and purified based on the procedure described previously (Zanotti et al., 1992 ▸ ). Briefly, Escherichia coli BL21(DE3) strain (Novagen), transformed with the pJexpress411 plasmid containing the synthetic cDNA coding for H-FABP, was over-expressed in perdeuterated minimal medium using d8-glycerol as carbon source (Artero et al., 2005 ▸ ). A high cell density fed-batch culture was grown at 30°C to an OD600 of 8.5. H-FABP expression was then induced by the addition of 0.5 mM IPTG and cells (40 g wet weight) were harvested at an OD600 of around 11. H-FABP was purified using 25 ml of Capto Q resin (GE Healthcare). The protein was eluted with 150 mM NaCl, 25 mM Tris-HCl pH 8.0. Finally, H-FABP was purified in a Hiload 26/60 Superdex 75 gel filtration column (GE Healthcare) in 20 mM Tris pH 7.5, 50 mM NaCl. The published crystallization conditions (Young et al., 1994 ▸ ) were optimized in terms of concentration and seeding conditions.
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3

Purification and Characterization of PKR Complexes

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The wt-PKR1-169 and Δloop-PKR1-169 complexes were prepared by incubating purified protein in the presence of a 1.1-fold excess of RNA in Buffer 1 for 15 minutes at room temperature. After incubation, the mixture was applied on a HiLoad 26/60 Superdex 75 gel filtration column (2.6 x 60 cm, GE Healthcare Life Sciences, USA). The elution profile for both complexes showed two distinct peaks: a higher molecular weight peak corresponding to RNA-protein complex followed by a lower molecular weight peak corresponding to free RNA. Elution fractions for both complexes were assayed for the presence of RNA-protein complex via in-line spectrophotometer (at 260 and 280 nm simultaneously), and confirmed by native polyacrylamide gel electrophoresis. Fractions containing RNA-protein complex were pooled and concentrated using GE Healthcare Vivaspin 2 concentrators (GE Healthcare Life Sciences, USA). The purity of the complexes was assessed by the native polyacrylamide gel electrophoresis, whereas concentration was determined using the extinction coefficients of protein and RNA. The DLS profiles of wt-PKR1-169 and Δloop-PKR1-169 complexes showed no signs of aggregation across the concentration range at which the experiments were performed.
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4

Purification of His-SUMO-BD1 and BD2

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His-SUMO-BD1 (42–168) and BD2 (349–460) constructs were expressed in LOBSTR E. coli cells (Kerafast, EC1002). Expression and purification of both constructs followed the same protocol. For NMR studies the His-SUMO-BD constructs were expressed in M9 minimal media containing 15N ammonium chloride. Cells were induced with 0.1 mM IPTG and grown at 16°C overnight before the pellet was collected. The cells were resuspended in lysis buffer (50 mM Tris, 200 mM NaCl, pH 7.5), lysed by sonication and centrifuged. The supernatant was purified using Ni resin equilibrated in binding buffer (50 mM Tris, 200 mM NaCl, 20 mM imidazole, pH 7.5), washed first with lysis buffer and 30 mM imidazole and then a final wash with lysis buffer and 50 mM imidazole. The protein was eluted from the Ni resin after incubation with SUMO protease Ulp1 in order to remove the His-SUMO tag. The cleaved proteins were then further purified by size-exclusion chromatography using a Hiload 26/60 Superdex 75 gel filtration column (GE, GE28-9893-34) in a buffer of 50 mM sodium phosphate, 100 mM NaCl pH 7.4 buffer before being concentrated and flash–frozen.
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5

Expression and Purification of PKR Proteins

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Recombinant human PKR1-169 (N-terminal double-stranded RNA binding motifs with residues 1 to 169) as well as full-length PKR were expressed and purified as previously described [14 (link)]. Affinity purified proteins were subjected to SEC using a HiLoad 26/60 Superdex 75 gel filtration column (2.6 x 60 cm, GE Healthcare Life Sciences, USA) for PKR1-169, or HiLoad 26/60 Superdex 200 size exclusion column for full length PKR (all in 50 mM TRIS (pH 7.50), 100 mM NaCl, and 5 mM 2-mercaptoethanol (Buffer 2)). The elution fractions were monitored by means of absorbance at 280 nm and fractions containing purified protein were combined and concentrated using Millipore concentrator filters (Millipore, USA). Protein purity was confirmed by SDS-PAGE and concentration was determined using the known extinction coefficient as measured by UV-Vis spectrophotometry (NanoDrop2000c, Thermo Scientific, USA).
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6

Purification of sCageHA protein variants

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sCageHA_267–1S and sCageHA_267–1S(E99Y/T144Y) were expressed at 18 °C in the E. coli LEMO21(DE3) strain (NEB) as a fusion protein containing a (His)10-tagged cysteine protease domain (CPD) derived from Vibrio cholerae48 at the C-terminus. The protein was purified using HisPur™ nickel resin (Thermo), a HiTrap Q anion exchange column (GE Healthcare) and a HiLoad 26/60 Superdex 75 gel filtration column (GE Healthcare). For Selenomethionine (SelMet)-labeling, an I30M mutation was introduced additionally to generate a sCageHA_267–1S(E99Y/T144Y/I30M) variant. This protein was expressed in the E. coli B834 (DE3) RIL strain (Novagen) in the minimal media containing SeMet, and purified according to the same procedure for purifying the other variants.
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