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Sephadex g 25 column

Manufactured by GE Healthcare
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Sephadex G-25 is a size-exclusion chromatography column used for the separation and purification of molecules based on their size. The column is packed with Sephadex G-25, a cross-linked dextran gel, which allows for the separation of small molecules from larger molecules or macromolecules. The core function of the Sephadex G-25 column is to perform desalting, buffer exchange, and the removal of low-molecular-weight substances from samples.

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116 protocols using sephadex g 25 column

1

Recombinant LAMP1 and mAb Production

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Nucleic acid sequences coding for LAMP1 extracellular domains fused to his-tag or Halotag-histag at the C-terminal or coding for the antibody heavy or light chains were cloned into mammalian expression plasmids under the CMV enhancer/promoter and the SV40 polyA signal. Resulting plasmids were transfected into HEK293 cells (Thermo Fisher Scientific; K9000-10) using FreeStyle MAX 293 Expression System according to the manufacturer’s instructions. LAMP1 proteins were purified by immobilized metal affinity chromatography (Chelating Sepharose, 17-0575-01 GE Healthcare) and stored in PBS after concentration and buffer exchange (Sephadex G-25 column, GE Healthcare).
For initial characterization, mAbs were produced at 30 mL scale, purified by protein A affinity chromatography and stored in PBS after desalting on mini trap Sephadex G-25 column. For the developability study, mAbs were produced at 1 L scale and purified by a two-step process including protein A affinity chromatography (HiScreen MabSelect Sure protein A, GE Healthcare, 28-9269-77) and size-exclusion chromatography (HiLoad 26/600 superdex 200 pg, GE Healthcare, 28-9893-36).
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2

Liposome Purification Protocols

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In order to remove non-encapsulated fisetin or cisplatin, a purification step is necessary. Fisetin-loaded liposomes were either purified using filtration under vacuum through a 0.45 µm filter (Sartorius, Göttingen, Allemagne) or using size-exclusion chromatography on Sephadex G-25 columns (GE Healthcare, Chicago, IL, USA). Cisplatin-loaded liposomes and co-loaded liposomes purification were carried out using size-exclusion chromatography on Sephadex G-25 columns (GE Healthcare). For DSC experiments, there was no purification step.
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3

Overexpression and Purification of EST2-S35C

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The mesophilic host E. coli strain BL21 (DE3), already available in our lab [25 (link)], was selected to over-express EST2-S35C, and was extracted and purified as previously detailed by Carullo et al. [23 (link)], with slight modifications. As previously described, TBP was added as a reducing agent to preserve the mutated cysteine in the reduced form. In addition, minor modifications to the extraction and purification steps were implemented. In particular, the protein was extracted using a sonication step performed on a Branson Sonifier Sound Enclosure Model SSE-1 (3 cycles of 40 s ON/30 s OFF, pulses at 50% power output intensity), in a water/ice bath at 4 °C. This step was followed by ultracentrifugation (80,000 g at 4 °C for 30 min) to remove the cell debris. After the thermo-precipitation/ultracentrifugation steps, gel filtration was performed using a Sephadex G-25 column (GE Healthcare Bio-Sciences AB, Uppsala, Sweden), achieving >95% purity of the enzyme. The final protein concentration was calculated after the Bradford method with bovine ɣ-globulin as the standard [26 (link)].
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4

Homocysteinylation of Fibrinogen and Fragment D

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42 or biotinylated Aβ42 peptides (Anaspec) were reconstituted in 4% NH4OH in 50mM TBS, pH 7.4, and aliquots were stored at 80°C. Before use, aliquots were centrifuged for 10 min at 12,000×g to remove pre- aggregated material. Aβ42 concentration was determined by BCA assay.
To homocysteinylate fibrinogen or fragment D (FragD), human plasminogen-free fibrinogen (29.4 μM, Calbiochem) and purified FragD[18 (link)] (34μM) were incubated with various doses of HC (Santa Cruz Biotechnology ) or HCTL (Sigma) at 37°C for 18h. To remove unreacted HC and HCTL, HC/HCTL-incubated fibrinogen samples were gel-filtered with a Sephadex G-25 column (GE Healthcare). Control and homocysteinylated fibrinogen and FragD concentrations were adjusted to 2.94μM or 5.67μM and subjected to assays described below.
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5

Kinetics of Cytochrome b5 Electron Transfer

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Reduction of CYB5 and electron transfer from ferrous CYB5 to the ferric globins was studied under anaerobic conditions. UV-visible spectra and kinetic data were recorded on an SX20 stopped-flow spectrophotometer equipped with a diode-array detector (Applied Photophysics). CYB5 was reduced to the ferrous form with excess sodium dithionite, which was removed using a Sephadex G25 column (PD10, GE Healthcare) equilibrated with 100 mM sodium phosphate buffer. Globins were oxidized with excess potassium ferricyanide (ferricyanide solutions ~1 M were added in a 1:10 ferricyanide:protein ratio (v/v) and incubated for 5–60 seconds at room temperature) and then excess oxidant was removed as described above. The absorbance at 568 nm was used to follow globin reduction, as this wavelength was found to be isosbestic for the transition of CYB5 from the ferrous to the ferric state, but not for that of any of globins tested. The final concentration of all globins was maintained between 5 and 10 μM, while the CYB5 concentration was varied from as high as 60 μM to less than 10 μM. Reactions were followed at 25 °C in 100 mM sodium phosphate, pH 7.4.
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6

Conjugation of Panitumumab with IR700

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Panitumumab (1 mg, 6.8 nmol) was incubated with IR700 (66.9 μg, 34.2 nmol, 10 mmol/L in DMSO) and 0.1 mol/L Na2HPO4 (pH 8.5) at room temperature for 1 h. The mixture was purified with a gel filtration column (Sephadex G 25 column, PD-10, GE Healthcare, Piscataway, NJ, USA). The protein concentration was determined with Coomassie Plus protein assay kit (Thermo Fisher Scientific Inc., Rockford, IL, USA) by measurement of the absorption at 595 nm with spectroscopy (8453 Value System; Agilent Technologies, Santa Clara, CA, USA). We abbreviate IR700-conjugated panitumumab as pan–IR700.
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7

Purification of Cry11Aa Toxin from B. thuringiensis

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B. thuringiensis strain (pCG6), producing Cry11Aa toxin [45 (link)], was grown in nutrient broth sporulation medium containing erythromycin (25 mg/mL) at 30 °C for 4–5 days up to complete sporulation [46 (link)]. The spores and crystal inclusions were harvested and purified according to the procedure described by previously reported studies [47 (link),48 (link),49 (link)]. The purified Cry11Aa inclusions were activated by trypsin (1:20, w/w) at 37 °C [50 (link)]. The activated Cry11Aa was biotinylated and purified using a Sephadex G25 column according to the manufacturer’s instruction (GE Healthcare Life Science, Pittsburgh, PA, USA).
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8

Preparation of Novel Anti-Tau Antibodies

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Example 1

Preparation of Novel Antibodies of Invention

Human IgG1 antibodies were constructed by cloning the heavy (VH) and light (VL) chain variable regions into a single expression vector containing IgG constant regions. Plasmids encoding the sequences corresponding to human anti-tau mAbs were transiently transfected in human embryonic kidney 293-derived Expi293F™ cells (Thermo Fisher) and 7 days post transfection, the expressed antibodies were purified from the culture medium by MabSelect SuRe (GE Healthcare) Protein A affinity chromatography. IgGs were eluted from the column with 100 mM sodium citrate buffer, pH 3.5 which was immediately buffer exchanged into PBS, pH 7.4 using a self-packed Sephadex G-25 column (GE Healthcare). Each antibody was quality controlled by SDS page and size exclusion chromatography coupled with multi angle light scattering (SEC-MALS) and was further confirmed for reactivity to cognate tau peptide by Octet biolayer interferometry.

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9

Fragmentation and Purification of Vi Capsular Polysaccharide

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Vi, freeze dried as the sodium salt, was solubilized in water and H2O2 was added to give a final concentration of 2.5 mg/mL Vi and 5% (wt/v) H2O2 in water. The mixture was heated at 80±0.5°C for 2h. The mixture was then injected into a Hiscreen Capto Q [GE Healthcare] column (4.7 mL of resin loading up to 100 mg of fragmented Vi mixture) equilibrated with buffer A and populations of different average size were separated using a gradient step method. NaH2PO4 20 mM pH 7.2 and NaH2PO4 20 mM NaCl 1M pH 7.2 were used as buffer A and B respectively. Pools at average size Vi of 8.6 and 43 kDa were eluted at 25 and 37% of buffer B respectively. Each pool was desalted on a Sephadex G-25 column [GE Healthcare] equilibrated with water. The average size of the fragmented Vi pools was determined by HPLC-SEC equipped with a TSK gel 3000 PWXL column and a TSK gel PWXL guard column (Tosoh Bioscience). Dextrans (5, 25, 50, 80, 150 kDa) were used as standards (Sigma Aldrich). The mobile phase was 0.1 M NaCl, 0.1 M NaH2PO4, 5% CH3CN, pH 7.2, at the flow rate of 0.5 mL/min (isocratic method for 30 min). HPAEC-PAD was used to measure Vi content [10 (link), 21 (link)]. 1H NMR was used to verify Vi identity and confirm O-acetylation levels were >60% [10 (link), 21 (link)].
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10

Lectin Microarray Analysis of Protein Profiles

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The manufacture of the lectin microarray and data acquisition were performed as described previously [26 (link)–28 (link)]. The proteins isolated from cells or tissue were labeled with Cy3 fluorescent dye (GE Healthcare, Biosciences, Piscataway, NJ, USA) and purified using a Sephadex-G25 column (GE Healthcare). Subsequently, 4 μg of labeled protein was applied to the lectin microarrays and incubated in the chamber at 37 °C for 3 h. After washing and centrifugation, the slides were scanned using a confocal scanner (4000B, AXON Instruments, USA). The fluorescence intensities were extracted by GenePix 7.0 software (Axon). After filtration and normalization, the parallel datasets were compared with each other based on fold changes according to the following criteria: fold changes ≥ 1.50 or ≤ 0.67 and p < 0.05 indicated upregulation or downregulation, respectively. Significant differences in lectin between samples were evaluated using Student’s t test.
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