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Probond purification system

Manufactured by Thermo Fisher Scientific
Sourced in United States

The ProBond™ Purification System is a laboratory instrument designed for the purification and isolation of biomolecules, such as proteins and DNA. It utilizes affinity chromatography principles to selectively bind and separate target molecules from complex mixtures. The system provides a controlled and automated workflow to streamline the purification process.

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34 protocols using probond purification system

1

Lipase Expression in E. coli BL21

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Transformation of a plasmid encoding lipase (accession number: YP_056770.1) into Escherichia coli (E. coli) BL21 competent cells (Invitrogen, Carlsbad, CA, USA). The E. coli BL21 transformed with a plasmid encoding GFP was used as a control by following the same procedure. A transformant of E. coli BL21 was inoculated with Luria–Bertani (LB) (Biokar Diagnostics, Beauvais, France) medium containing ampicillin (Sigma) at 37 °C until the OD600 reached 0.6–0.8. 1 mM Isopropyl-B-D-thiogalactoside (IPTG) (Sigma, Burlington, MA, USA) was added into culture for 4 h at 30 °C to induce protein expression. Proteins were purified by ProBond™ Purification System (Invitrogen, Carlsbad, CA, USA).
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2

Purification and Administration of TAT-fused Uch-L1 Protein

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TAT-fused Uch-L1 was provided by Dr. Ottavio Arancio (Professor at Columbia University), the construct was obtained as described by Gong et al. (2006 (link)).
Briefly, TAT vectors were transformed into E. Coli BL21(DE3) pLysS competent cells (Novagen), and the obtained colonies were grown as 1 ml overnight cultures in Luria broth (LB) medium (Sigma-Aldrich) with 100 mg ampicillin, in the presence of 100 mM IPTG. Then the cultures were transferred to 500 ml LB ampicillin plus 200 mM IPTG to obtain large-scale preparations. Fusion proteins were purified according to ProBond purification system (Invitrogen).
VUch-L1 fusion proteins were i.p. injected into mice at 0.03 g/kg, 20 min before the Rose Bengal injection and surgery procedure. After 6 or 12 h, mice were sacrificed and protein extracts were prepared and examined as described below.
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3

Plant Cell Culture Optimization

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Murashige and Skoog medium, 2,4-dichlorophenoxyacetic acid (2,4-D), kinetin, 2-(N-morpholino)ethanesulfonic acid (MES), triphenil-tetrazolium chloride (TTC), xylenol orange, EDTA, succinate, 4-morpholinepropanesulfonic acid (MOPS), Polyvinylpyrrolidone (PVP-40), hydroxylamine, sulphanilamide, α-naphthylamine, ampicillin, NP40, safranin, Salicylhydroxamic acid (SHAM), kalium-cyanide (KCN), linoleic acid, fatty acid free bovine serum albumin (BSA), luminol, p-Coumaric acid, Carbonyl cyanide-p-trifluoromethoxyphenylhydrazone (FCCP), were obtained from Sigma-Aldrich. ProBond Purification System was purchased from Invitrogen. Amicon Ultra 30K Centrifugal Filter Units were purchased from Merck. IPTG was obtained from Duchefa Biochemie, cytochrome c was purchased from Fluka. Primary and secondary antibodies were purchased from Agrisera Antibodies. All other chemicals were of analytical or HPLC grade, and were purchased from Reanal, Hungary. Pierce BCA Protein Assay Kit, GeneJET Plant RNA Purification Kit, and RevertAid First-Strand cDNA Synthesis Kit were obtained from Thermo Scientific; SensiFAST SYBR No-ROX Kit was purchased from Bioline.
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4

Recombinant Protein Expression and Purification

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MBP, SLPA, and LacZ cDNA were introduced into the Champion™ pET Directional TOPO® Expression Kit (Invitrogen, Carlsbad, CA, USA). BL21 Star™ (DE3) E. coli was transformed with the recombinant vectors, grown, and then their expression was induced by the addition of 1 mM IPTG into growth media according to manufacturer instructions. The recombinant His(6X)-tagged proteins were subsequently purified utilizing the ProBond™ Purification System (Invitrogen). The eluted protein was concentrated by PES, 3K MWCO (ThermoFisher Scientific, Waltham, MA, USA). Final concentration of protein was measured using the Pierce™ BCA Protein Assay Kit (ThermoFisher Scientific).
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5

Recombinant Protein Production and Purification

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GST- or His-tagged recombinant proteins were produced in E. coli using the GST Gene Fusion System (GE Healthcare) and the Probond Purification System (Invitrogen) respectively according to the manufacturers’ instructions and extracts were prepared by urea/DTT denaturation and renaturation as described previously [12 (link)]. Critical to reducing background ubiquitination, the recombinant His-tagged p21 was clarified by centrifugation at 100 000 g for 15 min at 4°C and the protein was stored in aliquots of 20 μl at −80°C, which were thawed no more than twice. Proteins prepared in this manner eluted as a well-defined single peak after gel filtration, albeit they were not purified to homogeneity.
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6

Purification of Recombinant Flagellin-Cap Protein

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The viral titer of the recombinant flagellin-Cap baculovirus was assayed and expressed as plaque forming unit (PFU) according to the standard protocol. Sf9 cells were infected with the recombinant virus followed by assaying protein expression at different harvest time intervals. The optimized harvesting time was 72 h postinfection. For protein production, Sf9 cells were infected with the recombinant baculovirus at a MOI of 1 PFU and harvested at the indicated time point. The expressed fusion protein was purified under denaturing conditions using the ProBond Purification System (Invitrogen, USA) in accordance with the manufacturer’s protocol. Briefly, the recombinant baculovirus-infected Sf9 cells for 72 h after infection were collected and centrifuged at 3,000 × g for 35 min. The cell lysates were resuspended in 8 ml of 6.0 M guanidine hydrochloride (pH 8.0) and applied to a ProBond Nickel-Chelating Resin with a His-tag for purification of recombinant fusion proteins. Prior to inoculation into mice, the purified proteins under denaturing conditions were further dialyzed against 0.5 M NaCl in 50 mM phosphaste buffered solution (PBS) (pH 7.4) with a step-wise reduction of urea concentrations. As a control, Sf9 cells were infected with a recombinant Cap baculovirus (35) and the purified recombinant Cap protein was included in animal experiments.
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7

Purification of BTV NS2 Protein Domains

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To obtain recombinant proteins NS2-Nt and NS2-Ct, recombinant baculoviruses (rBac) Bac-NS2-Nt and Bac-NS2-Ct were generated using the Bac-to-Bac system (Invitrogen, Barcelona, Spain), following the supplier protocols. Briefly, plasmid pSC11-NS2 containing the sequence coding for NS2 protein of BTV serotype 4 was used to amplify the sequence of NS2-Nt and NS2-Ct with specific primers (Table 2). The PCR products were then cloned into plasmid pFastBac1 (Invitrogen, Barcelona, Spain) digested with BamHI and NotI to obtain the transfer vectors HTA-NS2-Nt and HTA-NS2-Ct that were used to generate the recombinant baculoviruses that express the NS2-Nt or NS2-Ct BTV proteins in insect high five cells (H5), named Bac-NS2-Nt and Bac-NS2-Ct. These proteins were purified using the ProBond Purification System (Invitrogen, Barcelona, Spain) following the procedure indicated by the manufacturer for protein purification under native (NS2-Ct) or hybrid native-denaturing (NS2-Nt) conditions.
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8

Recombinant Protein Production in High Five Cells

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Another insect cell line High Five was used to produce large amount of recombinant proteins. High Five cells were cultured in Express Five serum-free medium (Invitrogen, Grand Island, NY, USA) supplemented with 5% FBS, 10 μg/ml gentamicin and 18 mM L-glutamine, and incubated in a non-humidified incubator at 28 °C. Optimal conditions for protein production were empirically established. Capillary western blot was used to detect recombinant R16/17 protein. Briefly, cell lysates with different MOIs were harvested at different time points. The expression of recombinant R16/17 protein was detected with a mouse anti-6xHis tag antibody (1:10, ab18184, Abcam) by ProteinSimple WES capillary western blot system according to a previously published method (Beekman et al. 2014 (link)). α-tubulin (mouse anti-α-tubulin antibody, 1:20, T5168, Sigma-Aldrich) was used as the loading control.
To scale up protein production, P2 viral stock was added to High Five cells in T175 flasks at a multiplicity of infection (MOI) of 20. Cells were harvested 3 days after infection, and the recombinant proteins were purified from cell lysates with the Probond purification system (Invitrogen, Grand Island, NY, USA). The identities of recombinant proteins were confirmed by western blot using anti-R17 and anti-His tag antibodies.
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9

Recombinant Expression and Purification of HPgV-2 NS4A/4B Protein

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The Protean 3D program (DNASTAR, Madison, WI, USA) was used to predict that an 81-amino acid segment of HPgV-2 NS4A/4B (derived from GenBank accession number KT427414.1) would be localized to the cytoplasm. This region was chosen for expression in the pMAL-C5X vector, which, under the control of an isopropyl-β-d-thiogalactopyranoside (IPTG)-inducible promoter, allowed for the addition of a maltose-binding protein (MBP) tag at the amino terminus and a 6-histidine tag at the carboxyl terminus (Genscript, Piscataway, NJ, USA). The construct was expressed in Escherichia coli strain BL21(DE3). Following IPTG induction for 4 h at 37°C, cells were lysed, and soluble protein was purified using the ProBond purification system (Invitrogen, Grand Island, NY, USA). Western blotting of the purified protein was performed using a WesternBreeze chromogenic kit (Invitrogen), and purified protein was detected using an anti-His antibody (Invitrogen). Protein was visualized using 5-bromo-4-chloro-3-indolylphosphate (BCIP)/nitroblue tetrazolium (NBT) staining (Novex by Life Technologies) and a Bio-Rad Gel Doc EZ imager, using Image Lab v4.0 software.
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10

Cloning and Expression of LRR and STK Domains

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The sequences encoding the leucine-rich repeated domain (from bp 1 to 283, named LRR283) and the serine/threonine-protein kinase domain (from bp 826 to 1145, named STK319) were amplified, expressed, and purified using the EasySelect™ Pichia Expression Kit and ProBond™ Purification System (Invitrogen, USA). Primer sequences are listed in Supplementary Table S1. The sequences were cloned into the pPICZ B expression vector in-frame with the C-terminal His tag, and transformed into E. coli to select transformants on low-salt LB plates containing 25 μg ml–1 Zeocin™. The purified and linearized recombinant plasmids were transformed into Pichia pastoris to select the Zeocin™-resistant yeast transformants on YPDS (yeast peptone dextrose sorbitol) plates containing the appropriate concentration of Zeocin™. The two fusion proteins were expressed and purified by Ni-NTA His Bind Resins according to the manufacturer’s protocols (Invitrogen, USA).
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