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Capto adhere

Manufactured by GE Healthcare
Sourced in Germany

Capto Adhere is a chromatography resin designed for the capture and purification of biomolecules. It utilizes a multimodal adsorption mechanism to enable the separation and isolation of various target molecules, including proteins, peptides, and other biomacromolecules. The resin's core function is to provide efficient and reliable purification performance for research and industrial applications.

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5 protocols using capto adhere

1

Purification of TIMP3 and Fusion Constructs

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Human TIMP3, modified TIMP3 with glycosylation mutations (v2, v82), and fusion constructs (HSA, Fc, or Ab) were expressed in a Chinese hamster ovary cell line, whereby conditioned media were concentrated by tangential flow filtration (TFF; Millipore,10 kDa MWCO) and filtered. The TIMP3 and fusion constructs were next purified through a three‐column chromatography procedure, each utilizing a specific capture column; TIMP3 and glycosylation mutants with Capto MMC (GE Healthcare, Freiburg, Germany): HSA fusions with Cibacron Blue (Merck KGaA, Darmstadt, Germany): and Fc or Ab fusions with MabSelect Sure (GE Healthcare, Pittsburg, PA). Each of these was then followed by Capto Adhere and SP HP (GE Healthcare, Freiburg, Germany) chromatography steps. The TIMP3 containing SP HP fractions were finally concentrated and buffer exchanged (10 mmol/L sodium acetate pH 5.2, 9% sucrose) by TFF. N‐TIMP3 (13.9 kDa N‐domain; aa 1‐120) was expressed as inclusion bodies in an E. coli system with a subtilisin prodomain fusion. After refolding and prodomain cleavage, the N‐TIMP3 was purified by a three‐column procedure using SP HP, CHT, and Butyl HP chromatography. The N‐TIMP3 containing Butyl HP fractions were also concentrated and buffer exchanged (10 mmol/L sodium acetate pH 5.2, 9% sucrose) by TFF (Pall, 5 kDa MWCO).
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2

Purification of IgG from Contaminants

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Example 17

An IgG-containing cell culture harvest containing 319,230 ppm host protein contaminants and 22% aggregates was conditioned by addition of 1% allantoin, 0.4% caprylic acid, pH 5.2; incubated for 2 hours, following which electropositive metal affinity particles (TREN 40 high, Bio-Works) were added in an amount of 4%, and incubated mixing for an additional 4 hours, then solids were removed through an electropositive depth filter (Sartorius PC1). Host proteins were reduced to 237 ppm and aggregates to less than 0.01%. The sample was loaded onto a multimodal hydrophobic cation exchanger (Millipore, HCX) at pH 7.0, and eluted in an increasing NaCl gradient. Host protein contamination was reduced to 37 ppm. The sample was loaded onto a multimodal hydrophobic anion exchanger at 1 M NaCl (Capto adhere, GE Healthcare) and eluted with a decreasing NaCl gradient, reducing host protein contamination to 1 ppm. Alternatively, the post-HCX sample was loaded onto a column of UNOsphere Q (Bio-Rad laboratories) equilibrated to 50 mM Tris, pH 8.0, operated in void exclusion mode, reducing host protein contamination to an undetectable level.

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3

Chromatography Media Evaluation Protocol

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All chemicals were obtained from Sigma-Aldrich (St. Louis, MO). WorkBeads™ 40 TRENhigh was purchased from BioWorks (Uppsala, Sweden). Eshmuno® HCX was purchased from Merck Millipore (Merck KGaA, Darmstadt, Germany). UNOsphere™ Q was purchased from Bio-Rad Laboratories (Hercules, CA). Toyopearl AF-rProtein A-650 was purchased from Tosoh Bioscience (Tokyo, Japan). Capto™ adhere was purchased from GE Healthcare (Uppsala, Sweden). Chromatography media were packed in XK or Tricorn™ series columns (GE Healthcare). Chromatography experiments were conducted on an ÄKTA™ Explorer 100 or Avant 25 (GE Healthcare).
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4

Purification of Recombinant Antibodies

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The chemicals used in this study were obtained from J.T. Baker (Phillipsburg, NJ). Recombinant antibody fragments (Fabs), mAbs, fusion proteins, and bispecific antibodies were produced in‐house using standard CHO cell culture techniques. Recombinant murine Cathepsin L (His‐tagged) was purchased from Sino Biological, Inc. (Gaithersburg, MD). The protease inhibitors used in the study were purchased from ThermoFisher Scientific (Grand Island, NY). Chromatographic resins MabSelect SuRe™ Protein A, Capto™ SP ImpRes, and Capto™ adhere were from GE Healthcare (Piscataway, NJ); POROS™ HQ, XQ, XS, and CaptureSelect™ CH1 (IgG‐CH1, specifically designed the purification of recombinant Fab fragments and IgGs) resins were from ThermoFisher Scientific; Toyopearl® GigaCap S650 M and NH2‐750F resins were from Tosoh Bioscience (King of Prussia, PA); Eshmuno® S and Fractogel® EMD SO3[M] resins were from EMD Millipore (Burlington, MA), Nuvia™ HR‐S and C‐prime resins were from Bio‐Rad (Hercules, CA), MEP® HyperCel were from Pall (New York, NY), Natriflo® HD‐Q membrane cassette was from Natrix (Burlington, ON, Canada).
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5

Cell-free production and purification of IgG

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Cell-free reactions were performed on 3 or 20 ml scale according to the same protocols described for wt trastuzumab IgG (Yin et al., 2012 ). The 20 ml crude cell-free reactions were diluted in 50 mM sodium phosphate, pH 7.3 and subsequently clarified via centrifugation. The IgGs were then captured by means of MabSelect SuRe (GE Lifesciences) chromatography, and further purified on Capto Adhere (GE Lifesciences) using manufacturer recommendations.
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