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Xk 16 40 column

Manufactured by GE Healthcare
Sourced in Germany

The XK 16/40 column is a laboratory equipment product designed for chromatography applications. It is a glass column with a diameter of 16 mm and a length of 40 cm, suitable for a variety of chromatographic separations. The column is constructed with a precision-engineered design to ensure consistent and reliable performance.

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5 protocols using xk 16 40 column

1

Recombinant IL-15 Protein Purification

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IL-15 D8SQ108S, mhIL-15 and siIL-15 proteins were expressed in E. coli and purified following the procedure previously described for obtaining siIL-15 [27 (link)]. Briefly, the proteins expressed in the insoluble fraction were solubilized in an 8 M urea solution. Then, the insoluble material was eliminated by centrifugation and chaotrope was removed through Sephadex G-25 Fine packed on XK 16/40 column (GE Healthcare Life Sciences, USA). The sample collected from G-25 (without urea) was loaded onto Q Sepharose Fast Flow using a column of 1.6 × 10 cm (GE Healthcare, USA), which was operated at 5 mL/min. After a washing step, IL-15 containing fractions were eluted and the collected sample was applied to a C4 column (1 × 25 cm, 10 µm, Vydac, USA) at a flow of 1 mL/min. Proteins were separated using a mobile phase containing solution A (0.1% TFA in water) and solution B (0.1% TFA in acetonitrile), using the same gradient as previously described [27 (link)]. Protein separations were monitored at 226 nm. The Bradford method was employed to determine the total protein concentration using BSA as standard [45 (link)].
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2

Antithrombin Purification Using Heparin Sepharose

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Pasteurized antithrombin (Kybernin P) was solubilized in buffer A [pH 7.4, 10 mL, phosphate-buffered saline (PBS, 10 mM), NaCl (0.25 m)] and loaded onto an XK 16/40 column (GE Healthcare) previously prepared with heparin sepharose 6-Fast Flow (50 mL) and equilibrated at 4°C in the same buffer. A low-af-finity fraction was eluted with buffer A (300 mL), whereas the high-affinity fraction was eluted with the same volume of elution buffer [PBS, pH 7.4, NaCl (2.5 M)]. The fractions were loaded onto 3 KDa MWCO filters (Millipore) in a stirred ultra-filtation cell (Millipore, Italy) for desalting and buffer-exchanged with phosphate buffer (pH 7.4, 20 mM). The final concentrations of the solutions were determined by using the bicinchoninic acid assay following the manufacturer’s instructions.
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3

Purification of RBD-CD Protein from Cell Culture

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Cell culture supernatant containing the RBD-CD protein was thawed and centrifuged at 4000× g for 10 min at 4 °C. The clarified cell culture supernatant was filtered through 0.45 µm and 0.2 µm cellulose nitrate filters (Sartorius). Afterward, protein purification was performed by metal affinity chromatography (IMAC). Briefly, filtered supernatant (250 mL) was equilibrated to a final concentration of PBS plus 2 mM imidazole (equilibrium buffer) by diluting in the same volume of PBS, and pH was adjusted to 7.4. Equilibrated supernatant was loaded at 0.5 mL/min at 4 °C onto an XK 16/40 column (GE Healthcare) packed with Ni-NTA agarose matrix (Qiagen, Hilden, Germany) previously equilibrated with 5 column volumes (CV) of equilibrium buffer. Then, the column was washed with 10 CV of washing buffer (PBS plus 10 mM imidazole, pH 7.4). The elution was performed with 5 CV of elution buffer (PBS plus 250 mM imidazole, pH 7.4). A buffer exchange to PBS was performed after purification with a PD10 desalting column (GE Healthcare, Chicago, IL, USA). The purified protein concentration was determined by measuring the absorbance at 280 nm (IMPLEN, Westlake Village, CA, USA). The purity of recombinant protein was assayed by densitometry scanning of protein gels, considering total protein concentration employing a BIO-RAD GS-800 scanner and the software Quantity One, version 4.6.9.
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4

Recombinant Hamster Prion Protein Preparation

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Recombinant hamster PrP proteins (residues 23–231 and 90–231; GenBank accession no. K02234) were prepared according to the method described previously [6 (link),7 (link)]. Briefly, the two DNA sequences of hamster PrP residues 23–231 and 90–231 were firstly ligated into the pRSET vector (cat. no. V35120; Thermo Fisher Scientific, Inc., Waltham, MA, USA), and then the recombinant plasmids were transformed into BL21(DE3)pLysS competent cells (cat. no. C1500; Beijing Solarbio Science & Technology Co., Ltd., Beijing, China). After treated the bacteria pellets by ultrasonication, the lysates were denatured with guanidine-HCL and the expressed proteins were purified by chromatography using Ni-NTA Superflow resin (cat. no. 30,430; Qiagen, Hilden, Germany) in an XK 16/40 column (GE Healthcare Life Sciences, Little Chalfont, UK) at a flow rate of 2.3 ml per min. The purified proteins were dialysed into 10 mM sodium phosphate buffer (pH 5.8) and the concentrations of recombinant PrP proteins (rHaPrP23-231 and rHaPrP90-231) were adjusted to 500 µg/ml as determined by absorbance measured at 280 nm. Following filtration (0.22 µm syringe filter, cat. no. SLGP033RB, Merck millipore), the recombinant PrP proteins were aliquoted and stored at −80°C, respectively.
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5

Chromatographic Sorbent Throughput Evaluation

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The throughput of the sorbent was determined using a GE AKTA chromatographic system with an XK 16/40 column (GE Healthcare, Munich, Germany) with a diameter of 1.6 cm. A total of 30 mL of sorbent was packed into the column (column height about 15 cm). The change in the pressure was recorded when the linear flow rate in the chromatographic system was varied.
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