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Total plasma homocysteine as part of the routine aminogram by ion-exchange chromatography.

Ion-exchange chromatography (IEC) with ninhydrin post-column derivatisation is the only technique available for the assay of total, (free plus bound), cysteine and homocysteine which also enables the routine measurement of all other commonly occurring amino acids. IEC assay of total cysteine and homocysteine typically involves incubating buffered plasma for 60 minutes at 37 degrees C with dithiothreitol (DTT), but these assay conditions significantly extend total analysis time and compromise other amino acid values, notably glutamine and glutamate. However, it is possible to carry out the DTT reduction in plasma virtually instantaneously and without additional buffering, thus preserving the integrity of other diagnostically important amino acids. Assay precision is adequate for cardiovascular risk assessment.

Amino Acids↗

Direct capture of plasma factor VIII:C by ion exchange chromatography.

An ion exchange medium, DEAE-Fractogel 650M, can be used to capture factor VIII (FVIII) directly from plasma. Previous reports have focussed on the use of this medium to capture FVIII from cryoprecipitate. In this report, citrate phosphate dextrose plasma was batch-stirred with DEAE-Sephadex A50, filtered, diluted, loaded onto a column packed with DEAE-Fractogel TSK 650M, and chromatographed. Most of the unwanted proteins flowed through the gel unadsorbed. Bound FVIII was eluted by increasing the ionic strength of the buffer. A citrate-based buffer gave an overall FVIII:C yield of 670 IU/kg plasma with a specific activity of 0.68 IU FVIII:C/mg protein. This process gave a higher yield of FVIII:C but significantly more prothrombin complex factors than cryoprecipitation. This method is a promising alternative to cryoprecipitation of FVIII.

Buffers↗

Multivariate discrimination for phenylketonuria (PKU) and non-PKU hyperphenylalaninemia after analysis of newborns' dried blood-spot specimens for six amino acids by ion-exchange chromatography.

Ion-exchange HPLC was developed for testing dried blood-spot specimens from newborns. The method is suitable for quantitative confirmatory testing of abnormal specimens detected in the New York State Newborn Screening Program. Positive specimens were initially identified among all New York State newborns with semiquantitative bacterial inhibition assays (BIA) for aminoacidopathies, including phenylketonuria (PKU) and non-PKU hyperphenylalaninemia (HP), maple syrup urine disease, and homocystinuria. A selection of 1346 specimens from routine BIA screening, including 131 newborns with PKU or persistent HP, were tested by HPLC. Of 179 BIA results that were falsely positive, 98 (55%) were also falsely positive by HPLC in which the Phe/Tyr ratio was the discriminator and the threshold was set to attain 100% sensitivity. Investigation of three multivariate discriminatory methods revealed that linear discriminant analysis excluded all but 35 (20%) of the BIA false-positives.

Amino Acids↗

Influence of wax coatings on release rate of anions from ion-exchange resin beads.

Ion-exchange resin beads were coated with various waxes to improve and control their release. The in vitro release rates of benzoate ions from the coated-resin beads were then investigated using a rotating sieve basket technique. The dramatic differences in release rates observed with the different waxes can be discussed in terms of the wax to resin ration and the solubility characteristics of the waxes. The initial release rates can be expressed in terms of a mathematical expression previously reported for the diffusion of ions in ion-exchange resins, thereby aiding in the elucidation of the effect of the waxes on release.

Anion Exchange Resins↗

Pressurized-flow anion-exchange capillary electrochromatography using a polymeric ion-exchange stationary phase.

The feasibility of using capillary columns equipped with silica frits and packed with a polymer-based anion exchanger (Dionex AS9-HC) for CEC separations of inorganic anions has been investigated. Experiments using a conventional 25 cm packed bed, and mobile phase flow that is a combination of hydrodynamic and electroosmotic flow were used to demonstrate that by varying the applied voltage (electrophoresis component) or the concentration of the competing ion in the mobile phase (ion-exchange component), considerable changes in the separation selectivity could be obtained. Using an artificial neural network, this separation system was modelled and the results obtained used to determine the optimum conditions (9 mM perchlorate and--10 kV) for the separation of eight inorganic anions. When a short (8 cm) packed bed was used, with detection immediately following the packed section, the separation of eight test analytes in under 2.2 min was possible using pressure-driven flow and a simple step voltage gradient. A more rapid separation of these analytes was obtained by only applying high voltage (-30 kV), where many of the same analytes were separated in less than 20 s and with a different separation selectivity to that obtained in conventional ion-exchange or capillary electrophoresis separations.

Anion Exchange Resins↗

Intercalation of gaseous thiols and sulfides into Ag+ ion-exchanged aluminum dihydrogen triphosphate.

Ag(+) ion-exchanged layered aluminum dihydrogen triphosphate (AlP) with the interlayer distance of 0.85 nm was synthesized by the ion-exchange of proton in triphosphate with Ag(+) ion. The amount of exchanged Ag(+) ion depended on the concentration of AgNO(3) aqueous solution. Ag(+) ion-exchanged AlP adsorbed gaseous thiols and sulfides into the interlayer region. The adsorption amounts of thiols were more than those of sulfides, thiols with one mercapto group > thiol with two mercapto groups > sulfides, and depended on the amount of exchanged Ag(+) ion in the interlayer region. The thiols with one mercapto group were intercalated to expand the interlayer distance of Ag(+) ion-exchanged AlP, whereas there was no expansion in the adsorption of sulfide. In the case of thiol with two mercapto groups, there was observed contraction of the interlayer distance through the bridging with Ag(+) ions of the upper and lower sides of the interlayer region.

Adsorption↗

Quantitative determination of semisynthetic cephamycins in human serum and urine by ion-exchange, reversed-phase and ion-pair chromatography.

High-performance liquid chromatographic methods have been developed for the determination of semisynthetic cephamycins: cefoxitin, cefmetazole and cefminox in human serum and urine samples. Serum samples spiked with each cephamycin were combined with an equal volume of methanol to remove proteins and, after centrifugation, and aliquot of the supernatant was analysed by ion-exchange, reversed-phase and ion-pair chromatography with hexadecyltrimethylammonium bromide as the ion-pairing agent. Urine samples were diluted, filtered and analysed by same chromatographic procedure. The cephamycins were detected by their ultraviolet absorbance (265-272 nm). It was possible to determine concentrations of cephamycins to 0.2 micrograms/ml in serum 2 micrograms/ml in urine samples with a good level of reproducibility and accuracy.

Anti-Bacterial Agents↗

Quantification of Ca2(+)-dependent protease activities by hydrophobic and ion-exchange chromatography.

Hydrophobic and ion-exchange chromatography were compared for yield of Ca2(+)-dependent proteases and their inhibitor in studies designed to quantify Ca2(+)-dependent proteases activity for comparative purposes. Ion-exchange (DEAE-Sephacel) proved superior to hydrophobic chromatography (Phenyl-Sepharose). Under the proper conditions, DEAE-Sephacel effectively separated low-calcium-requiring form of Ca2(+)-dependent protease (CDP-I) and CDP inhibitor. Characterization of the assay system for components of the Ca2(+)-dependent proteolytic system separated by ion-exchange chromatography indicated that proteolytic degradation of casein by Ca2(+)-dependent proteases was linear with time for up to 60 min at 25 degrees C and that it was linear up to .4 to .45 units of activity. Therefore, we recommend that, after identification of fractions containing Ca2(+)-dependent protease (CDP-I or CDP-II), these fractions be pooled, and reassayed at a volume that yields values of less than .45 units of activity. Unlike CDP-I and CDP-II, CDP inhibitor lost its activity rapidly with frozen storage (frozen in liquid nitrogen, then stored at -70 degrees C); therefore, inhibitor should be assayed in fresh (unfrozen) samples only.

Animals↗

5. Analytical methods: physiochemical assays. Use of ion exchange chromatography in steroid analysis.

Ion exchange chromatography (IXC) has been utilized in many different ways in the field of steroid analysis already for more than thirty years. Steroid conjugates can be extracted and fractionated on anion exchangers by virtue of their anionic nature, and in the same way the weakly acidic phenolic steroids are separated from the neutral ones. Anionic and cationic contaminants are removed by IXC during purification of the samples, and further, the use of lipophilic ion exchangers allow the simultaneous reversed phase chromatographic elimination of neutral lipids. Finally, certain steroids with specific functional groups can be selectively fractionated by ion exchangers converted to a suitable form. The high capacity and flexibility of IXC has made it a technique of choice in the purification of biological samples for the multicomponent analysis of steroids by GC or GC-MS during the last decade.

Chromatography, Gas↗

Analysis and degradation study of glyphosate and of aminomethylphosphonic acid in natural waters by means of polymeric and ion-exchange solid-phase extraction columns followed by ion chromatography-post-column derivatization with fluorescence detection.

The quantitative trace determination of glyphosate and its major metabolite, aminophosphonic acid (AMPA) in natural waters was achieved by means of ion-exchange chromatography. Fifty ml of natural water sample was preconcentrated by a two-step procedure: first the sample was percolated through a polymeric cartridge, LiChrolut EN, then through an anion-exchange column mechanism, and finally analyzed by ion-exchange chromatography followed by post-column reaction coupled to a fluorimetric detector. Linear calibration graphs were obtained between 5 and 200 micrograms l-1. Limits of detection ranged from 2 micrograms l-1 of glyphosate and 4 micrograms l-1 of AMPA. A study of the degradation of glyphosate in environmental waters under characteristic conditions was carried out to figure out the main degradation pathways of this compound. Half-lives of glyphosate varied from 60 h for ground water samples exposed to sunlight to 770 h for those stored under dark conditions.

Chromatography, Ion Exchange↗

Enhanced production of human epidermal growth factor by a recombinant Escherichia coli integrated with in situ exchange of acetic acid by macroporous ion-exchange resin.

A macroporous ion-exchange resin was adopted for the in situ exchange of acetic acid during human epidermal growth factor (hEGF) production by recombinant Escherichia coli JM101. The results of this study suggest that in situ exchange by macroporous resin can improve E. coli growth, decrease acetate accumulation and enhance hEGF production.

Acetic Acid↗

Purified haemoglobin preparations in the evaluation of HbA1c determination by ion exchange chromatography.

The use of ion exchange resins for the estimation of HbA1c in clinical samples rests on the assumption that HbA1c is effectively and efficiently separated from other N-terminally modified haemoglobins and from HbA0. To test this assumption, we applied highly purified preparations of HbA(1a+1b, HbA1c and HbA0 to ion exchange minicolumns, using conditions of application simulating actual blood samples and the first and second elution buffers provided by the manufacturer. The authenticity and purity of the applied haemoglobin preparations were documented by high performance liquid chromatography, gel electrophoresis and carbohydrate content. About 40% of the applied HbA(1a+1b) eluted in the first fraction; 45% eluted in the second fraction, and 10% to 15% required 1 mol/L NaCl to elute from the column. Of the applied HbA1c, 65-80% eluted where expected in the second fraction, about 20% required 1 mol/L NaCl to elute from the column, and the remainder eluted with HbA(1a+1b). Some 3-6% of pure HbA0 applied to minicolumns emerged in the second fraction, with the remainder eluting as expected after making the buffer 1 mol/L in NaCl. The results indicate that the fraction eluting from ion exchange minicolumn chromatography that is designated 'HbA1c' contains HbA(1a+1b), and that a substantial portion of the HbA1c in an applied sample does not elute in this fraction.

Chromatography, High Pressure Liquid↗

Theorization on ion-exchange equilibria: activity of species in 2-D phases.

Ion-exchange reactions are naturally occurring at soil and sediment/water interphases, determining soil fertility and water quality. These ion-exchange reactions with inorganic and organic exchangers are applied to chemical analysis, recovery of useful ions from low-grade ores (potentially from sea water), water purification including the preparation of "ultrapure" water, production of foods and medicines, therapy, and other uses. It is important to theorize about or to model ion-exchange reactions for quantitative explanations of ion-exchange phenomena and for efficient operation of ion-exchange processes. This paper describes the modeling of ion-exchange equilibria for hydroxyl sites on metal oxides and carboxyl sites in resins with monovalent cations (alkali metal ions), a monovalent anion (nitrate ion), and divalent heavy metal ions. The procedure of modeling is as follows: the stoichiometry and material balance equations of the respective ion-exchange reactions were established based on findings here and by others. The equilibrium conditions were given by the Frumkin equation, where the mass-action relation is modified with lateral interactions between species at the interphase. The model equations were fitted to the measured data and model parameter values were determined by nonlinear regression analysis. The formation of bonds between ions and exchanger sites was evaluated by the equilibrium constant and the suppression of bond formation by electrostatic, geometric, and other lateral interactions was evaluated by the interaction constant. It was established that the properties of ions are determined by the valence, size, and hydration state of the ions. Monovalent ions (anions and cations) react with oxide surface hydroxyl and resin carboxyl sites as hydrated ions and form loose ion-site pairs by a weak electrostatic bond (nonspecific adsorption). However, the lateral interactions are large because of a large polarization of the ion-site pairs. When the monovalent cations are dehydrated to react with carboxyl sites in narrow resin nanopores, the bond formation is difficult because energy for dehydration is necessary. The suppressive lateral interactions here are small because of a small polarization of the dehydrated ion-site pairs that are in direct contact. Divalent heavy metal ions react with oxide hydroxyl sites by replacing their hydrated water molecules and form ion-site pairs in direct strong contact (specific adsorption). The bond formation becomes easier with increasing charge density of the ions evaluated by the charge/radius ratio, agreeing with the order of these ions to form hydroxo complexes in solution. The suppressive lateral interaction is, however, small for ions with large charge densities, because a strong contact bond reduces the polarization of ion-site pairs by neutralization. The properties of exchangers are functions of the molecular and pore environments around the functional groups. The acid-base nature of oxide surface-hydroxyl groups is determined by the electronegativity of surrounding lattice metal ions, and that of resin carboxyl groups by the electron-repelling effect of adjacent methyl groups. Pores in oxides have diameters sufficient to accommodate hydrated ions, and the suppression is large because of repulsion from ions adsorbed on opposite pore walls (across-pore interaction). Pores in resins differentiate ions that can access or not access sites on the internal surfaces of the pores. Narrow nanopores with diameters less than those of the hydrated ions require ions to dehydrate before they can enter. The ion-exchange reactivity here is small, as described above for dehydrated monovalent ions. In wide nanopores where hydrated ions can enter, bond formation is easier, but suppression is greater because of a larger polarization of hydrated ion-site pairs and also of the across-pore interaction. Macropores have diameters much larger than those of the hydrated ions and the bond formation is the same as that in wide nanopores, but the suppression is smaller because of the absence oe of the absence of the across-pore interaction. Finally, this paper attempts a formulation of activity coefficients of exchanging sites and adsorbed ion-site pairs and compares the proposed activity coefficients of interphase species with that of solution species given by the Debye-Hückel equation.

Journal Article↗

Modelling gradient elution of bioactive multicomponent systems in non-linear ion-exchange chromatography.

A theoretical framework for the ion-exchange behaviour of bioactive substances in non-linear ion-exchange chromatogaphy is described. The aim of the study was the creation of a model basis to support a process design for production-scale ion-exchange chromatography. The theory can be applied to a whole variety of biological substances, such as amino acids, polysaccharides, peptides and proteins and either isocratic or gradient elution can be carried out. The influence of the eluent concentration on the ion-exchange as well as on the characteristic charge was considered. Experimental measurements showed a strong non-linear ion-exchange equilibrium with a transition from a Langmuir-type to a sigmoidal isotherm at higher eluent concentrations. Hereby, the compound binds to the surface though it is not ionic. Therefore, the model considered the possibility of ion-exchange as well as adsorption. A simplified distribution of the counter-ions based on the Gouy-Chapman theory with a discrete distribution of the counter-ions was used. The theory was extended by a selectivity in the double layer to allow specific adsorption. Calculations of adsorption-elution cycles showed, in agreement with the experimental observations, the development of non-linear elution profiles with a desorption fronting. As a result, the column loading and the eluent concentration were varied. The effect of contaminants, in this case sodium ions, was investigated and included in the model. Finally, the model was extended to multicomponent systems to investigate the effect of side components on the retention behaviour. The development of the characteristic elution profiles and the effect of the column loading on the separation are discussed. Calculated concentration profiles along the column at discrete time steps were used to reveal the influence of side components and the underlying separation mechanism. The simulations provided a new insight into the phenomena involved in biochromatography and make convenient design concepts at least doubtful as the separation is in this case mainly determined by the loading step and not by the choice of the elution gradient.

Adsorption↗