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1.
Biotechnol Adv ; 31(8): 1374-85, 2013 Dec.
Article in English | MEDLINE | ID: mdl-23747736

ABSTRACT

Magnetic separations are probably one of the most versatile separation processes in biotechnology as they are able to purify cells, viruses, proteins and nucleic acids directly from crude samples. The fast and gentle process in combination with its easy scale-up and automation provide unique advantages over other separation techniques. In the midst of this process are the magnetic adsorbents tailored for the envisioned target and whose complex synthesis spans over multiple fields of science. In this context, this article reviews both the synthesis and tailoring of magnetic adsorbents for bioseparations as well as their ultimate application.


Subject(s)
Biotechnology , Magnetic Fields , Magnetite Nanoparticles , Nucleic Acids/isolation & purification , Proteins/isolation & purification
2.
Article in English | MEDLINE | ID: mdl-22857861

ABSTRACT

In this work we have evaluated the potential of boronic acid functionalized magnetic particles for the one-step capture of a human monoclonal antibody (mAb) from a Chinese hamster ovary (CHO) cell culture supernatant. For comparison, Protein A coated magnetic particles were also used. The most important factor influencing the overall process yield and product purity in boronic acid particles was found to be the binding pH. Basic pH values promoted higher purities while resulting in decreased yields due to the competing effects of molecules such as glucose and lactate present in the cell culture supernatant. After optimization, the particles were successfully used in a multi-cycle purification process of the mAb from the CHO feedstock. Boronic acid particles were able to achieve an average overall yield of 86% with 88% removal of CHO host cell proteins (HCP) when the binding was performed at pH 7.4, while at pH 8.5 these values were 58% and 97%, respectively. In both cases, genomic DNA removal was in excess of 97%. Comparatively, Protein A particles recorded an average overall yield of 80% and an HCP removal greater than 99%. The adsorption of the mAb to the boronic acid particles was shown to be mediated by strong affinity interactions. Overall, boronic acid based purification processes can offer a cost-effective alternative to Protein A as the direct capturing step from the mammalian cell culture.


Subject(s)
Antibodies, Monoclonal/isolation & purification , Boronic Acids/chemistry , Chromatography, Affinity/methods , Magnets/chemistry , Adsorption , Animals , Antibodies, Monoclonal/chemistry , Antibodies, Monoclonal/metabolism , Boronic Acids/metabolism , CHO Cells , Chromatography, Affinity/instrumentation , Cricetinae , Cricetulus , Electrophoresis, Polyacrylamide Gel , Humans , Hydrogen-Ion Concentration
3.
J Chromatogr A ; 1218(43): 7821-7, 2011 Oct 28.
Article in English | MEDLINE | ID: mdl-21937050

ABSTRACT

In this work, we systematically evaluated the potential of using boronic acid functionalized magnetic particles in the capturing of human immunoglobulin G under typical mammalian cell culture conditions. For comparison, Protein A coated magnetic particles were also used. The binding pH was found to significantly influence the adsorption isotherms of boronic acid particles with the higher capacities (0.216 g IgG/g support) being observed at pH 7.4. Comparatively, this value was 0.109 g IgG/g support, for Protein A particles under the same conditions. Both particles revealed very fast adsorption kinetics with more than 70% of the maximum binding capacity being achieved in a few seconds. The effect of glucose and lactate, which are known to interact with boronic acid, was evaluated. For glucose, the binding capacity was significantly influenced by the pH and decreased as pH increased. At pH 9.5, a 70% lower binding capacity was observed for glucose concentrations as low as 0.5 g/l. The effect of lactate was less pronounced and almost pH independent reaching at most 20% decrease in binding capacity. Nevertheless, the effect of both molecules was always lower at pH 7.4. The optimization of the elution conditions enabled complete recovery of bound IgG from boronic acid particles using 50mM Tris-HCl, 200 mM sorbitol, 200 mM NaCl at pH 8.5.


Subject(s)
Boronic Acids/chemistry , Chromatography, Affinity/methods , Culture Media/chemistry , Immunoglobulin G/chemistry , Magnets/chemistry , Adsorption , Boronic Acids/metabolism , Cell Culture Techniques , Chromatography, Affinity/instrumentation , Glucose/chemistry , Glucose/metabolism , Humans , Hydrogen-Ion Concentration , Immunoglobulin G/metabolism , Lactic Acid/chemistry , Lactic Acid/metabolism , Microspheres , Models, Biological , Sodium Chloride/chemistry , Sorbitol/chemistry , Staphylococcal Protein A/chemistry
4.
J Mol Recognit ; 23(6): 569-76, 2010.
Article in English | MEDLINE | ID: mdl-21038357

ABSTRACT

In this work, we investigated the feasibility of using phenyl boronate (PB) chromatography for the direct capture of monoclonal antibodies from a CHO cell supernatant. Preliminary results, using pure protein solutions have shown that PB media can bind to human antibodies, not only at strong alkaline conditions but also at acidic pH values. In fact, antibodies have been found to bind in the pH range 5.5-8.5. On the other hand, insulin and human serum albumin did not bind at alkaline pH but at lower pH, which reflects the importance of non-specific interactions with the matrix. Different binding and eluting buffers were evaluated for the capture of immunoglobulin G (IgG) from a CHO cell supernatant and the most promising results were obtained using 20 mM 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid at pH 8.5 as binding buffer and 1.5 M Tris-HCl as eluting buffer. Using a step elution, all IgG was recovered in the elution pool with a maximum purification factor of 56. A gradient elution allowed a further increase of the final purity, yet achieving a slightly lower yield. IgG recovery was around 85% and the purification factor was 76. The highest purity was obtained when the pH of the cell supernatant feed was previously adjusted to 8.5. Starting from an initial protein purity of 1.1% and high-performance liquid chromatography (HPLC) purity of 2.2%, after PB adsorption, a final protein purity of 85% and a HPLC purity of 88% was achieved.


Subject(s)
Antibodies, Monoclonal/isolation & purification , Boronic Acids/pharmacology , Chromatography, Affinity/methods , Culture Media, Conditioned/chemistry , Adsorption , Animals , Antibodies, Monoclonal/chemistry , Antibodies, Monoclonal/metabolism , Antibodies, Monoclonal/pharmacokinetics , Antibody Affinity , Boronic Acids/chemistry , Boronic Acids/metabolism , CHO Cells , Cell Culture Techniques , Chromatography, High Pressure Liquid/methods , Cricetinae , Cricetulus , Culture Media, Conditioned/metabolism , Feasibility Studies , Humans , Protein Binding , Substrate Specificity
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