Mesoporous zirconium titanium oxides. Part 2: Synthesis, porosity, and adsorption properties of beads

Mesoporous zirconium titanium mixed-oxide beads having disordered wormhole textures and mole fractions of Zr (x) ranging from x=0.25 to 0.67 have been prepared. The bead preparation method combined the forced hydrolysis of mixtures of zirconium-titanium alkoxides in the presence of long-chain carboxylates with external gelation. Uniformly sized beads could be produced in the size range 0.5-1.1 mm by varying the droplet size and viscosity of the mixed-oxide sol, thus making them suitable for large-scale column chromatographic applications. The beads exhibited narrow pore size distributions with similar mean pore diameters of around 3.7 nm. The specific surface areas of the beads were linked to the Zr mole fraction in the precursor solution and were generally greater than 350 m2/g for x=0.5. A combination of scanning transmission electron microscopy and X-ray absorption fine structure analysis indicated that the pore walls of the beads were composed of atomically dispersed Zr and Ti to form a continuous network of Zr-O-Ti bonds. Mass transport in the beads was evaluated by monitoring the kinetics of vanadate and vanadyl adsorption at pH 10.5 and 0.87, respectively.

The effect of the pore structure and zeta potential of porous polymer monoliths on separation performance in ion-exchange mode

Most often, in bioseparations involving charged macromolecules, the chromatographic systems have low Reynolds and high Peclet numbers. For such systems, an expression is developed and presented in this work for evaluating the throughput in polymeric monoliths where ion-exchange adsorption occurs, as a function of (i) the pressure drop along the length of the monolith, (ii) the functional form and width of the throughpore-size distribution of the monolith, and (iii) the magnitude of the zeta potential on the surface of the throughpores of the monolith. Gaussian and log-normal throughpore-size distributions whose mean throughpore-size and standard deviation values are based on experimentally measured throughpore-size distribution data by mercury porosimetry employed on polymeric monoliths are used in this work, and their effect on the throughput relative to that obtained from a polymeric monolith having a uniform throughpore-size distribution is studied for different values of the ratio of the standard deviation to the mean throughpore-size. The results indicate that relatively modest increases in the throughput, when compared with the throughput that could be achieved in a polymeric monolith having a uniform throughpore-size distribution, could be obtained in polymeric monoliths having disperse throughpore-size distributions, and the magnitude of the increase becomes larger when the disperse distribution is skewed to larger throughpore sizes. Furthermore, the results of this work indicate that, under certain conditions, relatively modest increases in the throughput of a charged analyte could also be achieved by altering the value of the zeta potential on the surface of the throughpores of the monolith. Due to the difficulties inherent in controlling the functional form and width of the throughpore-size distribution during the synthesis of polymeric monoliths, it would appear to be more practical to increase the value of the throughput of a charged analyte by altering the value of the zeta potential through prudent selection of the ion-exchange surface functional groups and fine-tuned with the pH of the mobile phase. Thus, for ion-exchange chromatography systems, the zeta potential could be considered an important parameter for column designers and operators to manipulate, since its alteration could increase the through-put of a charged analyte in polymeric monoliths or in columns packed with charged particles.

Construction by Molecular Dynamics Modeling and Simulations of the Porous Structures Formed by Dextran Polymer Chains Attached on the Surface of the Pores of a Base Matrix: Characterization of Porous Structures

Significant increases in the separation of bioactive molecules by using ion-exchange chromatography are realized by utilizing porous adsorbent particles in which the affinity group/ligand is linked to the base matrix of the porous particle via a polymeric extender. To study and understand the behavior of such systems, the M3B model is modified and used in molecular dynamics (MD) simulation studies to construct porous dextran layers on the surface of a base matrix, where the dextran polymer chains and the surface are covered by water. Two different porous polymer layers having 25 and 40 monomers per main polymer chain of dextran, respectively, are constructed, and their three-dimensional (3D) porous structures are characterized with respect to porosity, pore size distribution, and number of conducting pathways along the direction of net transport. It is found that the more desirable practical implications with respect to structural properties exhibited by the porous polymer layer having 40 monomers per main polymer chain, are mainly due to the higher flexibility of the polymer chains of this system, especially in the upper region of the porous structure. The characterization and analysis of the porous structures have suggested a useful definition for the physical meaning and implications of the pore connectivity of a real porous medium that is significantly different than the artificial physical meaning associated with the pore connectivity parameter employed in pore network models and whose physical limitations are discussed; furthermore, the methodology developed for the characterization of the three-dimensional structures of real porous media could be used to analyze the experimental data obtained from high-resolution noninvasive three-dimensional methods like high-resolution optical microscopy. The MD modeling and simulations methodology presented here could be used, considering that the type and size of affinity group/ligand as well as the size of the biomolecule to be adsorbed onto the affinity group/ligand are known, to construct different porous dextran layers by varying the length of the polymeric chain of dextran, the number of attachment points to the base matrix, the degree of side branching, and the number of main polymeric chains immobilized per unit surface area of base matrix. After the characterization of the porous structures of the different porous dextran layers is performed, then only a few promising structures would be selected for studying the immobilization of adsorption sites on the pore surfaces and the subsequent adsorption of the bioactive molecules onto the immobilized affinity groups/ligands.

Comparison of the chromatographic behavior of monolithic capillary columns in capillary electrochromatography and nano-high-performance liquid chromatography

Porous monoliths based on N,N-dimethylacrylamide (DMAA) or methacrylamide (MAA) were prepared inside fused silica capillaries as stationary phases for nano-chromatography. The columns were characterized in terms of flow rate and backpressure and showed, e.g. differences as a function of the salt concentration added to the polymerization mixture. When the columns were investigated for the separation of uncharged (polar hydroxylated aromatic compounds) and charged (amino acids) analytes under pressure driven conditions (pLC), differences to the previously observed behavior under voltage driven conditions (CEC) were observed. Whereas the non-charged analytes showed similar behavior in both cases--thus, corroborating the previous assumption of a mainly chromatographic separation mode driven by hydrophilic interactions in CEC--the charged amino acids did not. Assuming that the separation was governed by chromatographic phenomena in the pLC mode and by both chromatographic and electrophoretic effects in the CEC mode, the experiments allowed deconvoluting the two contributions. In particular, the charged amino acids appeared to interact with the stationary phases mainly by electrostatic interactions modified by some hydrophilic effects.

On the nature of the forces controlling selectivity in the high performance capillary electrochromatographic separation of peptides

In this minireview, the nature of the forces controlling selectivity in the high performance capillary electrochromatographic (HP-CEC) separation of peptides has been examined. For uncharged and charged peptides, a synergistic interplay occurs in HP-CEC systems between adsorptive/partitioning events and electrokinetically driven motion. Moreover, at high field strengths, both bulk electrophoretic migration and surface electrodiffusion occur. Thus, the migration behavior of peptides in different HP-CEC systems can be rationalized in terms of the combined consequences of these various processes. Moreover, in HP-CEC, the buffer electrolyte interacts with both the peptide analytes and the sorbent as bulk phenomena. These buffer-mediated processes control the solvational characteristics, ionization status and conformational behavior of the peptides as well as regulate the double-layer properties of the sorbent, and the ion flux and electro-osmotic flow characteristics of the HP-CEC system per se. These buffer electrolyte effects mediate mutual interactions between the peptide and the sorbent, irrespective of whether the interaction occurs at the surface of microparticles packed into a capillary, at the surface of a contiguous monolithic structure formed or inserted within the capillary or at the walls of the capillary as is the case with open tubular HP-CEC. Diverse molecular and submolecular forces thus coalesce to provide the basis for the different experimental modes under which HP-CEC can be carried out. As a consequence of this interplay, experimental parameters governing the separation of peptides in HP-CEC can be varied over a wide range of conditions, ensuring numerous options for enhanced selectivity, speed, and resolution of peptides. The focus of the peptide separation examples presented in this minireview has been deliberately restricted to the use of HP-CEC capillaries packed with n-alkyl-bonded silicas or mixed-mode strong ion exchange sorbents, although other types of sorbent chemistries can be employed. From these examples, several conclusions have been drawn related to the use of HP-CEC in the peptide sciences. These observations confirm that variation of a specific parameter, such as the pH or the content of the organic solvent modifier in the buffer electrolyte, simultaneously influences all other physicochemical aspects of the specific HP-CEC separation. Peptide selectivity in HP-CEC thus cannot be fine-tuned solely through the use of single parameter optimization methods. In this context, HP-CEC differs significantly from the analogous reverse phase high performance liquid chromatography (RP-HPLC) procedures with peptides. Rather, more sophisticated multiparameter optimization procedures, involving knowledge of (a) the field strength polarity, (b) its contour and flux characteristics, (c) effects of buffer electrolyte composition and pH, (e) the influence of the temperature, and (f) the impact of the sorbent characteristics, are required if the full capabilities offered by HP-CEC procedures are to be exploited. In this minireview, the HP-CEC migration behavior of several different sets of synthetic peptides has been examined, and general guidelines elaborated from these fundamental considerations to facilitate the interpretation and modulation of peptide selectivity in HP-CEC.