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In-line respeciation: an ion-exchange ion chromatographic method applied to the separation of degradation products of chemical warfare nerve agents in soil.

The natural background of anions encountered when analyzing soil samples by ion chromatography (IC) present significant problems in the separation, detection and quantification of isopropyl methylphosphonic acid (IMPA) and methylphosphonic acid (MPA), the degradation products of sarin, a chemical warfare nerve agent. Using chemically-suppressed IC with conductivity detection, a commercially available ion-exchange column, and an isocratic binary eluent system, IMPA and MPA were determined in aqueous extracts of soil at sub-ppm (microgram/g) concentrations without the need for gradient elution or organic solvent eluent modifiers. Common soil anions such as chloride, nitrate, sulfate and phosphate do not interfere with the analysis method due to the composition of the binary eluent allowing for greater mobilization of multivalent anions (e.g., MPA, carbonate, and sulfate) while monovalent anions (e.g., IMPA and nitrate) are relatively unaffected. Carbonate is selectively removed by in-line respeciation to bicarbonate.

Chemical Warfare Agents↗

Difference in monoamine oxidase activity measured by either liquid ion exchange or ion exchange resin chromatography in rat and cat brain.

Cat and rat brain monoamine oxidase (MAO) activity was measured with a radioisotopic procedure and two extraction methods. Results indicated an underestimation of MAO activity when liquid ion exchange chromatography (LIEC) was used instead of an ion exchange chromatographic method (IEC) to separate the different products of the deaminated tyramine, phenylethylamine, or serotonin. MAO produced aldehydic products which may be found in the incubation medium and may be extracted with the substrate in the chloroform phase by the LIEC method. In cat brain, the resulting underestimation of the MAO activity was prevented by the addition of nicotinamide adenine dinucleotide (10(-3) M) in the incubation medium or by allowing a 2-h period between the end of incubation and the LIEC extraction procedure. In the rat brain, the same result was obtained by the addition of an equimolar mixture of nicotinamide adenine dinucleotide and nicotinamide adenine dinucleotide phosphate in reduced form (NAD-NADPH, 10(-3) M). Using the IEC method, the NAD decreased only the deamination of tyramine and serotonin in rat brain. This study suggests that the use of an IEC method to evaluate MAO activity is more accurate for the estimation of the enzymatic activity.

Animals↗

Improved brine recycling during nitrate removal using ion exchange.

Ion exchange technology is currently the best for removing nitrate from drinking water. However, problems related to the disposal of spent brine from regeneration of exhausted resins must be overcome so that ion exchange can be applied more widely and economically, especially in small communities. For this purpose, a novel spent brine recycling system using combined biological denitrification and sulfate reduction processes was developed for more efficient reuse of brine. A granular activated carbon (GAC) adsorption column was introduced as an additional step to prevent contamination of resins by bio-polymers and dissolved organics present in the bio-reactor effluent. Two upflow sludge blanket reactors (USBRs) were operated in series for 166 days to provide denitrification and sulfate reduction. The denitrification reactor provided a nitrate removal efficiency of 96% at a nitrate-N loading rate of 5.4 g NO3(-)-N/l d. The sulfate reduction efficiency of the sulfate reduction reactor remained approximately 62% at a sulfate loading rate of 1.8 g SO4(2-)/l d. Five ion exchange columns containing A520E resins were repeatedly operated in up to 25 cycles of service and regeneration using five kinds of brine: one virgin 3% NaCl and four differently recycled spent brines. Throughput decreased remarkably when the biologically recycled brine was not treated with the GAC column, probably due to the presence of bio-polymers and dissolved organic compounds. The sulfate reduction reactor placed after the denitrification step increased the bicarbonate concentration, which could be used as a co-regenerant with chloride. The inclusion of the sulfate reduction reactor into the conventional brine recycling system allowed more efficient reuse of brine, resulting in both reduced salt consumption and brine discharge.

Adsorption↗

Removal of natural organic matter by ion exchange.

Ion exchange is an effective method for removing humic substances from drinking water supplies. We have explored a range of anion exchangers for removal of natural organic matter (NOM), both as isolated from surface waters and after fractionation into four fractions based on hydrophobic and hydrophilic properties. Resins of open structure and high water content are confirmed as the better performers, being very efficient at removal of any charged material, especially that of smaller molecular size. Quaternary ammonium resins containing polar groups are especially effective. The presence of a neighbouring OH group close to the quaternary nitrogen, heteroatoms in the bridge between the exchange site and the polymer backbone, a secondary amino group as the exchange site, or a low ratio of carbon to quaternary nitrogen is beneficial. A suitable balance of polar and non-polar regions in the resin structure appears to be required. Weakly basic amino groups may have a greater affinity for hydrophilic counter ions than quaternary ammonium groups, but generally there are fewer charged sites in the resin at neutral pH. Nevertheless, weak base resins have NOM uptakes nearly as high as strong base resins of similar water content. Water content was found to be the most important parameter, though the effect was less pronounced for strong base resins. For weak base resins of low charge density a non-electrostatic mechanism involving hydrogen bonding of the undissociated acidic species in the NOM to the unprotonated amino groups on the resins is proposed.

Hydrogen-Ion Concentration↗

Complexation ion-exchange chromatography of some metal ions on papers impregnated with Ti(IV)-based inorganic ion exchangers.

The chromatographic behavior of 40 metal ions is studied on titanium (IV) arsenate, titanium (IV) phosphate-, titanium (IV) molybdate-, titanium(IV) tungstate-, and titanium(IV) selenite-impregnated papers in 0.1M oxalic, citric, and tartaric acid as mobile phases. Similar studies are carried out on Whatman No. 1 papers for comparison. The ion-exchange capacity of these papers is determined, and their selectivity for different cations is discussed. The mechanism of migration is explained in terms of ion-exchange, precipitation, and adsorption. The prediction of elution sequence from RF values is also checked. The average Ri is found to be almost linearly dependent on the charge of the metal ions. The effect of the pKa of complexing acids on average RF values of 3d series metal ions is explained. A number of binary and ternary separations are achieved.

Cation Exchange Resins↗

Biological ion exchanger resins. 3. Molecular interpretation of cellular ion exchange.

The cell is presented as a biological ion exchanger resin. The similarities between ion accumulating cells and ion exchanger resins are correlated. The kinetic characteristics of biological ion exchange are shown to be amenable to analysis by a model commonly used for ion exchanger resins. The theories of ion exchange equilibria currently in use with ion exchanger resins are reviewed with their suitability for adaptation to biological ion exchange in mind.

Biological Transport↗

Comparative studies on the isothermal characteristics of proteins adsorbed under batch equilibrium conditions to ion-exchange, immobilised metal ion affinity and dye affinity matrices with different ionic strength and temperature conditions.

In these investigations, the influence of a range of experimental parameters on the isothermal characteristics of hen egg white lysozyme (HEWL) and human serum albumin (HSA) adsorbed to several different adsorbents has been examined. The adsorbents were selected to encompass the same basic types of silica support matrices, but with the ligand properties and surface characteristics adjusted so that the dominant mode of interaction between the protein and the ligand involved either electrostatic binding (i.e. as ion-exchange interaction with polyaspartic acid immobilised onto glycidoxypropyl-modified Fractosil 1000), mixed-mode binding with both hydrophobic and electrostatic effect contributing to the protein-ligand interaction (i.e. as dye-affinity interactions with Cibacron Blue F3G-A immobilised onto Lichroprep DIOL or onto glycidoxypropyl-modified Fractosil 1000), or lone pair coordination binding (i.e. as immobilised metal ion affinity (IMAC) interactions with Cu2+ ions complexed with iminodiacetic acid immobilised onto glycidoxypropyl-modified Fractosil 1000). In each case, the adsorbents exhibited similar ligand densities and had the same particle size ranges and silica surface pretreatment. The effect of the ionic strength of the adsorption buffer and temperature on the isothermal adsorption behaviour under batch equilibrium binding conditions of the two test proteins were determined. Consistent with previous observations with soft gel ion exchangers and triazine dye-based adsorbents that are used in packed bed chromatographic systems, the capacities of the silica-based ion-exchange adsorbents, as well as the Cibacron Blue F3G-A dye affinity adsorbents, for both HSA and HEWL were reduced as the salt concentration was increased under batch equilibrium binding conditions. Moreover, with both of these classes of adsorbents, as the ionic strength was increased under constant temperature conditions, the isothermal adsorption dependencies progressively approximated more closely a Langmuirean model of independent binding site interactions, typical of a mono-layer binding process. In contrast, with the silica-based immobilised metal ion affinity adsorbents as the ionic strength was increased the adsorption behaviour appeared to follow a Freundlich model, indicative of positive cooperativity in the binding process. In parallel experiments, the effect of changes in temperature under iso-ionic strength conditions was examined. With increasing temperature, different patterns of isothermal adsorption behaviour for both test proteins were observed, with the magnitude of these trends depending on the type of interaction involved between the immobilised ligand and the protein. Utilising first order Van't Hoff relationships to analyse the experimental data for these protein-ligand interactions, the apparent changes in enthalpy and entropy for these interactions have been derived from the dependency of the change in the apparent Gibbs free energy on 1/T.

Adsorption↗

Rapid separation of proteins and their higher-molecular fragments by means of Spheron ion-exchanges.

Ion-exchange derivatives are described. of a hydrophilic rigid macroporous glycolmethacrylate gel called Spheron, suitable for rapid high-performance liquid chromatography (HPLC) of proteins and their fragments. Their flow parameters are compared with those of ion exchange derivatives of cellulose and polydextran. The conditions for work with them are described (regeneration, cycling, equilibration, column packing) as well as the construction of a simple apparatus for medium-pressure ion exchange chromatography of proteins. The efficiency of these ion exchangers for the separation of proteins is illustrated with examples of chromatography of an artificial mixture of serum albumin, chymotrypsinogen and lysozyme. Chromatography of cyanogen bromide fragments of serum albumin and the A and B chains of oxidized insulin showed that the method can be applied in chromatography on higher molecular protein fragments. A review of all proteins, including technical enzymes, which have already been chromatographed on Spheron ion exchangers is also given. The prospects of Spheron ion exchangers for HPLC of proteins and their fragments are briefly discussed.

Acrylates↗

Biological ion exchanger resins. II. QUERP water and ion exchange selectivity.

Biological selectivity is shown to vary with medium osmotic strength and temperature. Selectivity reversals occur at 4 degrees C and at an external osmolality of 0.800 indicating that intracellular hydration and endosolvent (intracellular water) structure are important determinants in selectivity. Magnetic resonance measurements of line width by steady-state nuclear magnetic resonance (NMR) indicate a difference in the intracellular water signal of 16 Hz between the K form and Na form of Escherichia coli, providing additional evidence that changes in the ionic composition of cells are accompanied by changes in endosolvent structure. The changes were found to be consistent with the thermodynamic and magnetic resonance properties of aqueous electrolyte solutions. Calculation of the dependence of ion-pairing forces on medium dielectric reinforces the role of endosolvent structure in determining ion exchange selectivity.

Biological Transport↗