Protein adsorption and transport in agarose and dextran-grafted agarose media for ion exchange chromatography.

This work examines the relationship between the physical properties of agarose and dextran-grafted agarose cation exchangers and protein adsorption equilibrium and rates. Four different sulfopropyl (SP) matrices were synthesized using a neutral agarose base material--two based on a short ligand chemistry and two obtained by grafting 10 and 40kDa dextran polymers. The pore accessibility, determined by inverse size exclusion chromatography (iSEC) with dextran probes, decreases dramatically as a result of the combined effects of crosslinking, dextran grafting, and the introduction of ionic ligands, with pore radii decreasing from 19nm for the base matrix to 6.1nm for the 40kDa dextran-grafted SP-matrix. In spite of this reduction, while the adsorption isotherms were similar, protein uptake rates were greatly increased with the dextran-grafted SP-matrices, compared to SP-matrices based on the short ligand chemistry. The effective pore diffusivities were 4-10 times higher than free solution diffusivity for the dextran-grafted matrices, indicating that the charged dextran grafts result in enhanced protein mass transfer rates.

[1]  G. Carta,et al.  Particle‐size distribution effects in batch adsorption , 2003 .

[2]  J. V. Van Alstine,et al.  An exclusion mechanism in ion exchange chromatography. , 2006, Biotechnology and bioengineering.

[3]  Howard Brenner,et al.  The Constrained Brownian Movement of Spherical Particles in Cylindrical Pores of Comparable Radius: Models of the Diffusive and Convective Transport of Solute Molecules in Membranes and Porous Media , 1977 .

[4]  J. Thömmes Investigations on protein adsorption to agarose-dextran composite media. , 1999, Biotechnology and bioengineering.

[5]  Alois Jungbauer,et al.  Chromatographic media for bioseparation. , 2005, Journal of chromatography. A.

[6]  Douglas M. Ruthven,et al.  Principles of Adsorption and Adsorption Processes , 1984 .

[7]  W. Deen Hindered transport of large molecules in liquid‐filled pores , 1987 .

[8]  G. Carta,et al.  Protein Adsorption on Cation Exchangers: Comparison of Macroporous and Gel‐Composite Media , 1996 .

[9]  M. Léonard New packing materials for protein chromatography. , 1997, Journal of chromatography. B, Biomedical sciences and applications.

[10]  E. Boschetti Advanced sorbents for preparative protein separation purposes , 1994 .

[11]  A. Liapis,et al.  The Coupling of the Electrostatic Potential with the Transport and Adsorption Mechanisms in Ion-Exchange Chromatography Systems: Theory and Experiments , 2005 .

[12]  C. Horváth,et al.  Surface and pore diffusion in macroporous and gel-filled gigaporous stationary phases for protein chromatography. , 2002, Journal of chromatography. A.

[13]  Abraham M Lenhoff,et al.  Pore size distributions of ion exchangers and relation to protein binding capacity. , 2006, Journal of chromatography. A.

[14]  Thomas Linden,et al.  Mechanism and kinetics of protein transport in chromatographic media studied by confocal laser scanning microscopy. Part I. The interplay of sorbent structure and fluid phase conditions. , 2003, Journal of chromatography. A.

[15]  Magnus Östberg,et al.  Apparent pore size distributions of chromatography media , 1996 .

[16]  W. Müller New ion exchangers for the chromatography of biopolymers , 1990 .

[17]  Susan Budavari,et al.  The Merck index , 1998 .

[18]  A. Lenhoff,et al.  Determination of pore size distributions of porous chromatographic adsorbents by inverse size-exclusion chromatography. , 2004, Journal of chromatography. A.

[19]  M. T. Tyn,et al.  Prediction of diffusion coefficients of proteins , 1990, Biotechnology and bioengineering.

[20]  P. Dephillips,et al.  Pore size distributions of cation-exchange adsorbents determined by inverse size-exclusion chromatography. , 2000, Journal of chromatography. A.

[21]  Giorgio Carta,et al.  Protein Mass Transfer Kinetics in Ion Exchange Media: Measurements and Interpretations , 2005 .

[22]  G. Carta,et al.  Characterization of protein adsorption by composite silica-polyacrylamide gel anion exchangers I. Equilibrium and mass transfer in agitated contactors , 1996 .

[23]  A. Lenhoff,et al.  Nondiffusive mechanisms enhance protein uptake rates in ion exchange particles , 2003, Proceedings of the National Academy of Sciences of the United States of America.

[24]  K. Fujita,et al.  Fabrication of Hard Dextran DEAE: Adsorption Equilibria of BSA , 1999 .

[25]  Don W. Green,et al.  Perry's Chemical Engineers' Handbook , 2007 .

[26]  Giorgio Carta,et al.  Characterization of protein adsorption by composite silica-polyacrylamide gel anion exchangers II. Mass transfer in packed columns and predictability of breakthrough behavior , 1996 .

[27]  J. Porath,et al.  Agar derivatives for chromatography, electrophoresis and gel-bound enzymes: I. Desulphated and reduced cross-linked agar and agarose in spherical bead form , 1971 .

[28]  Steven M. Cramer,et al.  Steric mass‐action ion exchange: Displacement profiles and induced salt gradients , 1992 .

[29]  A. Striegel,et al.  Modern size-exclusion liquid chromatography , 1979 .

[30]  A. Ljunglöf,et al.  Ligand Distributions in Agarose Particles as Determined by Confocal Raman Spectroscopy and Confocal Scanning Laser Microscopy , 2003, Applied spectroscopy.

[31]  A. Lenhoff,et al.  Protein Adsorption Isotherms through Colloidal Energetics , 1999 .

[32]  J. A. Quinn,et al.  Restricted transport in small pores. A model for steric exclusion and hindered particle motion. , 1974, Biophysical journal.

[33]  Piero M. Armenante,et al.  MASS TRANSFER TO MICROPARTICLES IN AGITATED SYSTEMS , 1989 .

[34]  Jeffrey A. White,et al.  Agarose-dextran gels as synthetic analogs of glomerular basement membrane: water permeability. , 2002, Biophysical journal.

[35]  J. Lausmaa,et al.  Surface chemical analysis of carbohydrate materials used for chromatography media by time-of-flight secondary ion mass spectrometry. , 2004, Analytical chemistry.

[36]  A. Lenhoff,et al.  Effects of ionic strength on lysozyme uptake rates in cation exchangers. I: Uptake in SP Sepharose FF. , 2005, Biotechnology and bioengineering.

[37]  E. Müller Properties and Characterization of High Capacity Resins for Biochromatography , 2005 .

[38]  R. B. Henderson,et al.  The Role of Neighboring Groups in Replacement Reactions. VII. The Methoxyl Group , 1943 .

[39]  R. Scopes,et al.  Assay for determining the number of reactive groups on gels used in affinity chromatography and its application to the optimisation of the epichlorohydrin and divinylsulfone activation reactions , 1996 .

[40]  G. Carta,et al.  Radiotracer measurements of protein mass transfer: Kinetics in ion exchange media , 2006, Biotechnology journal.