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An IgM anti-group B Streptococcus monoclonal antibody (4B9) was found to undergo irreversible heat-induced aggregation at 50 degrees C. A variety of excipients was tested for their ability to inhibit antibody aggregation. The amount of 4B9 aggregation, which was determined by analysis on a size-exclusion HPLC, was significantly reduced in the presence of low concentrations [between 0.1 and 1.0% (w/v)] of poly(vinylpyrrolidone) (PVP) molecules ranging in molecular weight from 10 to 40 kDa. When the PVP concentration was greater than 1.0%, antibody aggregation was enhanced, and with the highest molecular weight PVP, antibody precipitation occurred. HPLC was used to show that more PVP was associated with the 4B9 at 50 degrees C than at 25 degrees C. Differential scanning calorimetry revealed that PVP concentrations greater than 2.0% decreased the antibody thermal transition temperature. Enzyme-linked immunosorbent assays were used to assess the effects of PVP on the antigen binding capacity of 4B9 and on 4B9 quantitation. At 4 degrees C, PVP solutions of up to 5.0% had no effect on either 4B9 quantitation or antigen binding. At 50 degrees C, however, less 4B9 was detected in the 5.0% PVP solution. The heat stabilization of the 4B9 antibody by low concentrations of PVP can be explained by a weak binding of PVP to the native protein. The PVP may sterically interfere with protein-protein interactions, thus reducing aggregation. Higher concentrations of PVP lead to protein aggregation and precipitation, probably by a volume-exclusion mechanism.(ABSTRACT TRUNCATED AT 250 WORDS)

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Proteins are subject to a variety of physical and chemical reactions that lead to a loss of activity. These reactions are a particular problem in controlled-release devices, where temperatures and protein concentrations are high. Current approaches to increasing protein stability include the addition of saccharides, amino acids, or polymers. New synthetic polymers may be promising protein stabilizers because properties such as molecular weight and side-chain composition can be controlled. In this study, the stability of a murine monoclonal antibody, BR96, was evaluated in solution at 37 degrees C. The antibody was incubated in the presence of a series of synthetic polymers that included poly(glucosylethyl methacrylate) (GEMA) and copolymers of N-vinylpyrrolidone (NVP) and methyl methacrylate (MMA). Samples were taken periodically up to 30 days. The formation of precipitated antibody in particulate aggregates was measured with a Coulter counter, and the molecular-weight distribution of soluble antibody was measured by size-exclusion chromatography. Two trends were evident. First, with poly(GEMA) and copolymers of NVP and MMA, protein aggregation increased at higher polymer concentrations. Second, higher molecular weights of the poly(NVP) homopolymer also led to increases in protein aggregation. Effects of polymer hydrophobicity were more complex. A copolymer containing 9 mol% MMA caused immediate protein precipitation, while a copolymer containing 21 mol% MMA did not. The effects of the copolymer containing 21% MMA were strongly concentration dependent. At 1 wt%, the polymer reduced aggregation, but aggregation increased strongly between concentrations of 2 and 3 wt%.

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A series of hydrogels with large pores was synthesized by the precipitation polymerization of 2-hydroxyethyl methacrylate (HEMA) with crosslinking agent in aqueous solution. Such gels are potentially useful for the controlled release of large-molecular-weight species such as proteins. In this study, the release behavior of lysozyme and alpha-amylase from hydrogels formed from HEMA or HEMA with a comonomer was studied. It was found that the polymer composition affected the total amount of lysozyme released and its activity. Effects were smaller with alpha-amylase. Charged gels, containing a phosphate moiety, released larger amounts of lysozyme at a reduced rate as a result of charge-charge interactions.

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Immunoadsorption is a powerful and generalizable method for protein purification that exploits the fine specificity of antigen-antibody interactions. In spite of its potential utility, the more widespread process scale use of immunoadsorption has been limited by the high cost of the antibody and the lack of gentle elution schemes that completely preserve the activity of both the immunoadsorbent and the eluted product. In this report, we review common chemical elution strategies such as pH, ionic strength, chaotropic salts, denaturants, and organic solvents as well as physical techniques such as pressure, electrokinetics, and temperature. In general, selection of elution strategies has largely been an empirical art, balancing stability of the immunoadsorbent and the eluted product and efficiency. The limitations of the available choices demonstrate that more attention must be placed on the antibody. Techniques which assist in the identification or creation of new antibodies with improved binding properties and resistance to degradation, e.g., screening and/or rational protein engineering, are also discussed.

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Immunoaffinity purification has become an important technique in biotechnology. In this review the basic principles of immunoaffinity separations are described with respect to the stages of operation and potential application. The most commonly used support materials, activation procedures, and coupling chemistries are compared to one another for suitability in various applications. Individual operational steps for fixed bed immunoadsorbents including loading, washing, elution and regeneration are described in terms of both theory and practice. Factors influencing adsorbent stability are identified, and alternative operation and configuration strategies are discussed in light of their application to immunoaffinity systems.

RESUMEN

The limited life of immunoadsorbents used for the large-scale purification of biological macromolecules poses a significant limitation to the more widespread application of this technology. In this study, the binding activity of a monoclonal antibody (MAb) to bovine serum albumin (BSA) was measured as a function of pH, ionic strength, and varying concentrations of KSCN, ethylene glycol, or DMSO. Low pH (2.5) and 3 M KSCN each reduced the antibody binding constant below 6 x 10(5) L/mol, meeting criteria derived from a simple chromatographic model for identifying effective eluents. A panel of six MAb to BSA was exposed repeatedly to adsorption conditions and the two eluents. Four MAb lost less than 50% of their initial binding capacity over 100 cycles. The other two lost 75% of their initial capacity. One MAb was stable when exposed to low pH but lost binding capacity with KSCN. In all cases, the equilibrium constant was unchanged. The loss of capacity was also shown to be a strong function of antibody loading: at 14.5 mg/mL, 98% of the initial binding capacity of one MAb was lost within 40 cycles, versus 75% loss at 1 mg/mL. Antibody leakage and nonspecific adsorption of contaminants were not responsible for significant loss of antibody activity over time.

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