High performance liquid affinity chromatography: a new tool in biotechnology

Affinity chromatography: A review of trends and developments over the past 50 years

The field of affinity chromatography, which employs a biologically-related agent as the stationary phase, has seen significant growth since the modern era of this method began in 1968. This review examines the major developments and trends that have occurred in this technique over the past five decades. The basic principles and history of this area are first discussed. This is followed by an overview of the various supports, immobilization strategies, and types of binding agents that have been used in this field. The general types of applications and fields of use that have appeared for affinity chromatography are also considered. A survey of the literature is used to identify major trends in these topics and important areas of use for affinity chromatography in the separation, analysis, or characterization of chemicals and biochemicals.

Facile phenylboronate modification of silica by a silaneboronate

Macroscopic and colloidal silica surfaces were readily modified with alkoxysilaneboronate, IV, yielding silica surfaces with covalently bonded phenylboronic acid groups. XPS and neutron activation confirmed the presence of boron. The ability of these surfaces to specifically interact with polyols was demonstrated with polyol-coated latex and ARS, a dye that specifically couples to boronic acid groups immobilized on colloidal or macroscopic silica. This is a new, direct approach for introduction of phenylboronic acid groups onto silica surfaces.

Semiautomated high-sensitivity profiling of human blood serum glycoproteins through lectin preconcentration and multidimensional chromatography/tandem mass spectrometry

We describe an effective analytical approach to identify trace glycoproteins in a small volume of human serum. The system is based on automatable affinity enrichment through silica-based lectin microcolumns and a further separation of the retained glycoproteins on a reversed-phase liquid chromatography with superficially porous packing, operating at high temperature. The fractionated sample is further directed into a 96-well plate for trypsinization and LC-MS/MS analysis. Using a major-component depleted blood serum (16 microg total protein), we were able to identify 271 glycoproteins through this analytical system.

Effect of experimental conditions on strong biocomplimentary pairing in high-performance monolithic disk affinity chromatography

The effect of flow-rate on quantitatively determined binding parameters for several biocomplementary pairs in affinity mode high-performance monolithic disk affinity chromatography (HPMDAC) has been investigated using frontal analysis approach. Affinity interactions were evaluated from linearized adsorption isotherms and dynamic dissociation constants of the complexes K(diss.) and the theoretical adsorption capacities Q(max) were calculated. HPMDAC isolation of a typical protein trypsin from both buffered solution and artificial mixture as well as biospecific extraction of antibodies against bovine serum albumin and recombinant protein G from such complex mixtures as blood serum and cellular lysate were examined. Immobilized counterparts soybean trypsin inhibitor, bovine serum albumin, and human immunoglobulin G were used in chromatographic experiments. The maximum adsorption capacities obtained at different flow-rates were compared with those determined at static conditions. The dependence of quantitative parameters on the surface density of immobilized ligands has also been explored. Finally, a series of experiments was carried out to evaluate the dependence of dynamic affinity binding on temperature for two complementary pairs.

Reverse micellar extraction for downstream processing of proteins/enzymes

New developments in the area of downstream processing are, hopefully, to fulfill the promises of modern biotechnology. The traditional separation processes such as chromatography or electrophoresis can become prohibitively expensive unless the product is of high value. Hence, there is a need to develop efficient and cost-effective downstream processing methods. Reverse micellar extraction is one such potential and a promising liquid-liquid extraction technique, which has received immense attention for isolation and purification of proteins/enzymes in the recent times. This technique is easy to scale-up and offers continuous operation. This review, besides briefly considering important physico-chemical and biological aspects, highlights the engineering aspects including mass transfer, mathematical modeling, and technology development. It also discusses recent developments in reverse micellar extraction such as affinity based separations, enzymatic reactions in reverse micelles coupled with membrane processes, reverse micellar extraction in hollow fibers, etc. Special emphasis has been given to some recent applications of this technique.

Progress in monitoring, modeling and control of bioprocesses during the last 20 years

The paper gives a review on the recent development of bioprocess engineering. It includes monitoring of product formation processes by flow injection analysis, various types of chromatographic and spectroscopic methods as well as by biosensors. The evaluation of mycelial morphology and physiology by digital image analysis is discussed also. It deals with advanced control of indirectly evaluated process variables by means of state estimation/observer, with the use of structured and hybrid models, expert systems and pattern recognition for process optimization and gives a short report on the state of the art of metabolic flux analysis and metabolic engineering.

Fast isolation of protein receptors from streptococci G by means of macroporous affinity discs

A fast affinity method for the semi-preparative isolation of recombinant Protein G from E. coli cell lysate is proposed. Rigid, macroporous affinity discs based on a glycidyl methacrylate-co-ethylene dimethacrylate polymer were used as chromatographic supports. The specific ligands (here human immunoglobulin G, hIgG) were immobilized by the one-step reaction between native epoxy groups of the polymer surface and epsilon-amino groups of the IgG molecules. No intermediate spacer was necessary to reach full biological activity of the ligand. The globular affinity ligands are located directly on the pore wall surface and are thereby freely accessible to target molecules (here Protein G) migrating with the mobile phase through the pores. It is shown that the conditions chosen for the hIgG immobilization do not involve an active site of the protein and thus do not bias the formation of the affinity complex. Chromatographically determined constants of dissociation of hIgG-Protein G affinity complexes confirm the high selectivity of this separation method. Two different aspects of the affinity separation are discussed, which differ mostly in terms of scale. In disc chromatography, high volumetric flow velocities are possible because of the small backpressure. Since in addition the mass transfer is more efficient, it becomes possible to achieve very short analysis times. The discs proposed can be used in a single-step enrichment of Protein G from lysates of non-pathogenic E. coli. Gel electrophoresis data are used to demonstrate the high degree of purity achieved for the final product.

Exploitation of a monoclonal antibody for weak affinity-based separation in capillary gel electrophoresis

Weak biospecific recognition has been established for affinity separation in high performance liquid chromatography (HPLC). The use of weak affinity chromatography (WAC) has been limited previously by the insufficient separation efficiency achieved, allowing only some 1000 plates/m to be obtained. However, it has been shown that chiral drug separation can be performed with capillary affinity gel electrophoresis (CAGE) at considerably improved efficiency as compared with traditional chromatographic procedures. Our present study demonstrates the potential of weak affinity monoclonal antibodies as a generic method for immunologically based separations in capillary electrophoresis. Monoclonal antibodies were polymerized within a silica capillary and were used for the separation of structurally similar carbohydrate antigens. The results indicate that weak biospecific interactions can be utilized in a CAGE format to produce highly selective separation of the alpha- and beta-forms of p-nitrophenyl-labeled maltose. It remains to be seen, however, how efficient weak affinity separation in CAGE can be compared with affinity HPLC protocols. Details of typical separations and of the preparation of the antibody gel are presented.

Chromatography in the downstream processing of biotechnological products

Chromatography techniques are essential for the isolation and purification of most of the high value products of modern biotechnology. The economically sensible and technically satisfactory downstream processing of a therapeutic protein, usually involves a number of chromatographic steps. Its development and optimization require considerable knowledge of the various physico-chemical and engineering aspects of biochemical chromatography. This review addresses the various modes of chromatography and the design of chromatographic separation processes from a biotechnologist's point of view. Strategies for optimizing the structure of the downstream process are outlined and scaling up consideration are discussed. The importance of the different chromatographic methods in research and development is estimated in an analysis of protein purification schemes recently published in the literature. Finally, examples of the application of chromatographic procedures for process scale product purification in the biotechnological industry are given.

Study of affinity supports based on reactive polymers immobilized on silica: affinity constant determination from isocratic zonal elution

Polymers bearing benzamidine moieties have been prepared from reactive copolymer containing chloroformate functions and deposited on porous silica matrices. These high-performance affinity chromatography supports were characterized by quantitative methods, which analyse the zonal elution behaviour of trypsin in the presence of a soluble competitor (L-arginine). The column loading capacity for trypsin was measured by the zonal elution method in mass overload conditions. On the basis of a Langmuir isotherm, the influence of the protein capacity and the concentration of the soluble ligand on the elution volume was studied for the determination of the binding constants. The plate heights determined for silica supports of various porosities and particle diameters show that the strong affinity interactions between trypsin and p-aminobenzamidine are mainly responsible for the low efficiencies observed.

Surface-modified membranes as a matrix for protein purification

Recently introduced membrane-based chromatographic supports for protein separation are available either with a coupled ligand, e.g., protein A, protein G or ion-exchange groups, or as activated matrices for coupling a desired ligand. The coupling conditions for protein A and immunoglobulin G to an epoxy-activated membrane were determined. The performance of the prepared affinity membranes was investigated using pure rabbit immunoglobulin G and protein A as a model system. For practical application monoclonal antibodies from cell culture supernatant were purified with a prepared protein A membrane and for comparison with a sulphonic acid ion exchange membrane.

New methods for separation and recovery of biomolecules

New methods and applications in the separation of biomolecules are reviewed, with an emphasis on the large-scale recovery of proteins. Highlights include the advent of flow-through particles in perfusion chromatography, which allows for very high flow rates, while retaining a high chromatographic efficiency.

Eupergit C as a carrier for high-performance liquid chromatographic-based immunopurification of antigens and antibodies

An immunoaffinity purification system using C30N and C1Z Eupergit C beads was developed and optimized. Poly- and monoclonal antibodies were purified using immobilized antigens and antigens were purified using immobilized antibodies. Antigens were used that possess enzymic activities and the efficiency of antigen binding was determined from the enzymic activity of the matrix-bound immunocomplexes. High-performance immunoaffinity purification using Eupergit C beads proved to be highly specific, reproducible, free from protein leakage and possessed a low degree of non-specific adsorption of tissue proteins. These characteristics of the system were illustrated by the isolation of immunoglobulin G from serum and of human decidua proteins from the decidua tissue and from seminal plasma. These proteins were obtained at high purity in a single purification step, as shown by sodium dodecyl sulphate-polyacrylamide gel electrophoresis.