Biological Ion Exchanger Resins: III. 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.     

Release characteristics of ion-exchange resins as buffers in low ionic strength nutrient solutions

The use of synthetic ion-exchange resins as buffers of nutrient ions is a potential mechanism for the control of ion concentrations in nutrient solutions. In this study equilibrium constants for two cation exchange resins and three anion exchange resins were determined at 25°C in low ionic strength systems. The measured constants were used to successfully predict the resin combinations required to achieve desired solution equilibrium concentrations. The effectiveness of these resins in buffering solution ion concentrations was evaluated by examining their release characteristics in circulating systems from which aliquots of solution were withdrawn and replaced with deionised water to simulate plant uptake. Buffering of NO₃ and SO₄ concentrations was effective when manual control of one anion was imposed. The cation resins were ineffective in buffering the concentrations of Ca and Mg with a tendency for the resins to retain most of the Ca and Mg in adsorbed form.     

Sorption of acid ribonuclease from Penicillium brevi-compactum by various ion-exchange resins

Sorption of acid ribonuclease from Penicillium brevi-compactum F-399 was studied. The effect of nature and structure of various ion-exchange resins on the sorption capacity and reversibility was determined. High rate and reversibility of the enzyme sorption on the strong base anion-exchange fiber TsM-A2 were demonstrated. It is suggested that sorption of acid ribonuclease of the TsM-A2 fiber proceeds as ion exchange and on carboxyl cation exchange resins as molecular sorption.     

Immobilization of glucose isomerase

The immobilization of glucose isomerase (D-xylose ketol isomerase, EC 5.3.1.5) by covalently bonding to various carriers and by adsorption to ion exchange resins was attempted in order to obtain a stable immobilized enzyme which can be used for continuous isomerization of glucose in a column. Of the covalent bonding methods, the colloidal silica-glutaraldehyde method showed the highest binding capacity and gave the most stable immobilized glucose isomerase. The Ludox HS-30 bound glucose isomerase column showed a half-life of 24 days and an enzyme usage of 0.07 units per gram of isomerized sugar (d.s, fructose 45%). Of the resins used, the macromolecular type or porous type strongly basic anion exchange resins showed the highest binding capacity and gave the most stable immobilized glucose isomerase. The Amberlite IRA-904 resine-bound glucose isomerase showed a half-life of 23 days and an enzyme usage of 0.06 units per gram of isomerized sugar (d.s., fructose 45%). Based on the ease of the immobilization process, the possibility of carrier reuse and the extensive use already achieved by ion exchange resins in the sugar industry, IRA-904 resin was selected as the candidate for commercialization.     

Systematic Separation of Human Urinary Peptides

Urinary peptides were roughly fractionated by combined columns of cation and anion exchange resins, and the peptides eluted from each column were further fractionated by a combination of various ion exchange resins and DEAE-cellulose column chromatography, paper chromatography and other methods. From the fractions adsorbed on cation exchange resin, 13 homogeneous peptides could be isolated, and from the ones adsorbed on anion exchange resin, 8 glycopeptides could be found. Their amino acid compositions were analyzed.

Although some fractions remain univestigated, an outline of the whole aspect of main urinary peptides has been clarified by this study.     

Formation of broad-spectrum antibiotics by cultures of the genus Micromonospora]

Data on the study of antibiotic production by the representatives of Micromonospora and the use of ion exchange resins for intensification of screening antibiotic-producing organisms among Micromonospora are presented. It was found that out of 172 strains of Micromonospora tested 92 (53.5 per cent) cultures produced antibiotics, 18 of which were active against gramnegative bacteria. The use of carboxylic ion exchange resins at early microbiological stages of the screening provided an increase in the frequency of finding broad spectrum antibiotics from 10.4 to 19.7 per cent.     

Kinetics and mass transfer for lactic acid recovered with anion exchange method in fermentation solution

An anion exchange method for lactic acid recovered from lactic acid-glucose solution in an ion-exchange membrane-based extractive fermentation system was examined. The exchange isotherms of anion exchange resins for lactic acid recovered were measured batchwise, and the exchange-desorption kinetics of lactic acid passing through the exchange column was investigated. The determined typical breakthrough and elution curves were measured and simulated by conventional mode. The mass transfer coefficients were identified by numberical method. The effects of the velocity of the fluid on the dynamics were studied. Aqueous NaOH solution was found to be the best solvent for elution. An experiment on anioun exchange from clarified lactic acid fermentation broth was carried out to obtain knowledge of the performance of the ion exchange system from a borth. The ion-exchange mass-transfer coefficient and efficiency from the fermentation broth is found to be lower when compared with aqueous solutions of pure lactic acid. The results show that the separation method with anion exchange resins may be used in the production of lactic acid by fermentation.(c) 1995 John Wiley & Sons, Inc.     

Surface attachment of nitrifying bacteria and their inhibition by potassium ethyl xanthate

Ion exchange resins and glass microscope slides were used to investigate factors affecting attachment of nitrifying bacteria to solid surfaces and the effect of attachment on inhibition ofNitrobacter by potassium ethyl xanthate. The ammonium oxidizerNitrosomonas attached preferentially to cation exchange resins while the nitrite oxidizerNitrobacter colonized anion exchange resins more extensively. Colonization was always associated with growth, and the site of substrate (NH₄ ⁺ or NO₂ ^–) adsorption was the major factor in attachment and colonization. The specific growth rate of cells colonizing either ion exchange resin beads or glass surfaces was greater than that of freely suspended cells, butNitrobacter populations colonizing glass surfaces were more sensitive to the inhibitor potassium ethyl xanthate. The findings indicate that surface growth alone does not protect soil nitrifying bacteria from inhibition by potassium ethyl xanthate and explain different patterns of inhibition for ammonium and nitrite oxidizers in the soil.     

An exclusion mechanism in ion exchange chromatography

Protein dynamic binding capacities on ion exchange resins are typically expected to decrease with increasing conductivity and decreasing protein charge. There are, however, conditions where capacity increases with increasing conductivity and decreasing protein charge. Capacity measurements on two different commercial ion exchange resins with three different monoclonal antibodies at various pH and conductivities exhibited two domains. In the first domain, the capacity unexpectedly increased with increasing conductivity and decreasing protein charge. The second domain exhibited traditional behavior. A mechanism to explain the first domain is postulated; proteins initially bind to the outer pore regions and electrostatically hinder subsequent protein transport. Such a mechanism is supported by protein capacity and confocal microscopy studies whose results suggest how knowledge of the two types of IEX behavior can be leveraged in optimizing resins and processes.     

Separation of bivalent anti-T cell immunotoxin from Pichia pastoris glycoproteins by borate anion exchange

A major problem encountered in the large-scale purification of the bivalent anti-T cell immunotoxin, A-dmDT390-bisFv(G4S), from Pichia pastoris supernatants was the presence of host glycoproteins exhibiting similar charge, size, and hydrophobicity characteristics. We overcame this problem by employing borate anion exchange chromatography. The borate anion has an affinity for carbohydrates and imparts negative charges to these structures. We found that at a concentration of sodium borate between 50 and 100 mM, the nonglycosylated immunotoxin did not bind to Poros 50 HQ anion exchanger resin, but glycoproteins, including aggregates related to the immunotoxin, did. By using this property of the immunotoxin in the presence of sodium borate, we successfully developed a 3-step purification procedure: (i) Butyl-650M hydrophobic interaction chromatography, (ii) Poros 50 HQ anion exchange chromatography in the presence of borate, and (iii) HiTrap Q anion exchange chromatography. The final preparation exhibited a purity of greater than 98% and a yield of greater than 50% from the supernatant. Previously, boronic acid resins have been used to separate glycoproteins from proteins. However, combining borate anion with conventional anion exchange resins accomplishes the separation of the immunotoxin from glycoproteins and eliminates the need to evaluate nonstandard resins with respect to good manufacturing practice guidelines.     

Preparation and Evaluation of Differently Sulfonated Styrene–Divinylbenzene Cross-linked Copolymer Cationic Exchange Resins as Novel Carriers for Drug Delivery

The differently sulfonated styrene–divinylbenzene cross-linked copolymer cationic exchange resins were prepared by oil-in-water polymerization and varied degrees of sulfonation. Several characteristics of the obtained resins were evaluated, i.e., Fourier transform infrared spectra, the ion-exchange capacity, microscopic morphology, size, and swelling. The resin characteristics were altered in relation to the degree of sulfonation, proving that differently sulfonated resins could be prepared. The behavior of chlorpheniramine (CPM) loading and in vitro release in the USP simulated gastric (SGF) and intestinal fluids (SIF) of the obtained resins were also evaluated. The CPM loaded in the resinates (drug-loaded resins) increased with the increasing degree of sulfonic group and hence the drug binding site in the employed resins. The CPM release was lower from the resins with the higher degree of sulfonic group due to the increase in the diffusive path depth. The CPM release was obviously lower in SGF than SIF because CPM, a weak base drug, ionized to a greater extent in SGF and then preferred binding with rather than releasing from the resins. In conclusion, the differently sulfonated resins could be utilized as novel carriers for drug delivery.     

Simultaneous measurement of dopamine and its metabolites, 5-hydroxytryptamine, 5-hydroxyindoleacetic acid and tryptophan in brain tissue using liquid chromatography and electrochemical detection

An assay has been developed for brain tryptophan using reverse-phase liquid chromatography with electrochemical detection. The method simultaneously assays dopamine (DA) and its metabolites, dihydroxyphenylacetic acid (DOPAC) and homovanillic acid (HVA), as well as 5-hydroxytryptamine (5-HT) and 5-hydroxyindoleacetic acid (5-HIAA). The method does not require elution from ion exchange resins. After deproteinization and centrifugation samples are injected directly onto the chromatographic column. It was found that small changes in mobile phase pH markedly influenced the retention time of tryptophan while elution of the indoleamines and catecholamines did not change. The assay of these endogenous compounds in a single injection proved not expedient but inexpensive. Values obtained using alumina and ion exchange resins yielded comparable values.     

Hydrolysis of methyloleate using immobilized lipase from Chromobacterium viscosum

Various lipases were screened for their hydrolytic efficiency towards methyloleate. Lipase from Chromobacterium viscosum gave highest hydrolysis efficiency of 92% in 24?h. Different cation exchange resins were screened to immobilize lipase from Chromobacterium viscosum. A weakly acidic macroreticular type resin, IRC-50 having carboxyl end group functionality gave highest activity yield of 18.8%. Strongly acidic cation exchange resins with sulphonic functionality and macroreticular type did not give much activity yield when compared to weakly acidic non macroreticular type resins. It was observed that end group functionality and structure of the matrices plays an important role in obtaining highest activity yield. For a specific water concentration, the hydrolysis ratio reached 85% in less than 7?h when the substrate to enzyme ratio was 4. As the ratio is increased above 4, the availability of water at the interface has become a limitation for obtaining maximum hydrolysis.     

Enhanced production of periplasmic interferon alpha-2b by Escherichia coli using ion-exchange resin for in situ removal of acetate in the culture

The possibility of using in situ addition of anion-exchange resin for the removal of acetate in the culture aimed at improving growth of E. coli and expression of periplasmic human interferon-α2b (PrIFN-α2b) was studied in shake flask culture and stirred tank bioreactor. Different types of anion-exchange resin were evaluated and the concentration of anion-exchange resin was optimized using response surface methodology. The addition of anion-exchange resins reduced acetate accumulation in the culture, which in turn, improved growth of E. coli and enhanced PrIFN-α2b expression. The presence of anion-exchange resins did not influence the physiology of the cells. The weak base anion-exchange resins, which have higher affinity towards acetate, yielded higher PrIFN-α2b expression as compared to strong anion-exchange resins. High concentrations of anion-exchange resin showed inhibitory effect towards growth of E. coli as well as the expression of PrIFN-α2b. The maximum yield of PrIFN-α2b in shake flask culture (501.8 μg/L) and stirred tank bioreactor (578.8 μg/L) was obtained at ion exchange resin (WA 30) concentration of 12.2 g/L. The production of PrIFN-α2b in stirred tank bioreactor with the addition of ion exchange resin was about 1.8-fold higher than that obtained in fermentation without ion exchange resin (318.4 μg/L).     

Artifact-inducing enrichment of ethylenediaminetetraacetic acid and ethyleneglycoltetraacetic acid on anion exchange resins

Multivalent metal chelators, ethylenediaminetetraacetic acid (EDTA) and ethyleneglycoltetraacetic acid (EGTA), are used extensively during protein purification. Both strong (Q) and weak (DEAE) anion exchange resins were found to adsorb surprisingly large quantities of EDTA and EGTA that elute from the resin at NaCl concentrations of approximately 240 mM (EDTA) and 140 mM (EGTA). The EDTA/EGTA elution and saturation parameters were determined for five commonly used anion exchange resins. The resulting concentration of eluted EDTA was 10- to 200-fold higher than that originally present in the sample or in the mobile phase. Samples from fractions containing such a high concentration of EDTA were found to inhibit Mg²⁺-dependent polymerase chain reaction (PCR). EDTA binding to the anion exchange resins could saturate the resin, decrease its binding capacity, and displace weakly bound proteins such as green fluorescent protein (GFP). Several steps are suggested to minimize on-column EDTA concentration, including column equilibration in the absence of any EDTA, lower concentrations (0.1–0.5 mM) of EDTA, monitoring eluate absorbance at 280 nm as well as at 215 nm, adding EDTA back into fractions eluting before the EDTA peak, and performing blank column runs to control for the effect of changes in EDTA concentration in downstream assays.     

Removal of lipopolysaccharides from protein-lipopolysaccharide complexes by nonflammable solvents

During the recovery of recombinant proteins from gram negative bacteria, many of the methods used to extract proteins from cells release lipopolysaccharides (LPS, endotoxin) along with the protein of interest. In many instances, LPS will co-purify with the target protein due to specific or non-specific protein-LPS interactions. We have investigated the ability of alkanediols to effect the separation of LPS from protein-LPS complexes while the complexes are immobilized on ion exchange chromatographic resins. Proteins were complexed with fluorescently labeled LPS and bound to ion exchange resin. Alkanediol washes of the resins were preformed and the proteins eluted. Column eluates were monitored for LPS and protein by fluorescence and UV spectroscopy, respectively. Alkanediols were effective agents for dissociating LPS from protein-LPS complexes. The efficiency of LPS removal increased with increasing alkanediol chain length. The 1,2-alkanediol isomers were more effective than terminal alkanediol isomers in the separation of LPS from protein-LPS complexes, while the separation of LPS from protein-LPS complexes was more efficient on cation exchangers than on anion exchangers. In addition, it was noted during these investigations that the 1,2-alkanediols increased the retention time of the proteins on the ion exchange resins. Alkanediols provide a safer alternative to the use of other organics such as alcohols or acetonitrile for the separation of LPS from protein due to their lower toxicity and decreased inflammability. In addition, they are less costly than many of the detergents that have been used for similar purposes.     

A method for the determination of glucose synthesis in isolated bovine hepatocytes

A simple method for determining glucose synthesis from radiolabeled precursors in isolated bovine hepatocytes using ion exchange resins is presented. This method allows processing of multiple small volume samples using suspensions of anion and cation exchange resins rather than traditional stacked column separation methods. Hepatocytes were isolated from calf liver by collagenase perfusion of the caudate lobe and were incubated with (14)C-labeled lactate or propionate as gluconeogenic substrates. Glucose synthesis was determined in an aliquot of cell suspension that was vortexed with a slurry of anion exchange (acetate form) resin, followed by a slurry of cation exchange resin. Newly synthesized, labeled glucose was recovered in the supernatant after centrifugation and quantitated by scintillation counting. Using this procedure, more than 98% of the unused labeled precursor was bound to the ion exchange resin and essentially 100% of a labeled glucose tracer was recovered in the supernatant. Pretreatment of hepatocyte suspensions with glucose oxidase was shown to eliminate the accumulation of radioactivity in the supernatant, thus confirming the specificity of this technique for measurement of newly synthesized glucose. This method was sensitive to changes in the rate of hepatic gluconeogenesis that resulted from changes in substrate concentration or the addition of glucagon or fatty acids to the hepatocyte incubations.     

Purification of bovine hemoglobin via fast performance liquid chromatography

Bovine hemoglobin (bHb) was purified from bovine red blood cells (bRBCs) via anion exchange chromatography preceded by dialysis. This is a fast and effective way to obtain bHb from bRBCs using Q Sepharose XL, a strong anion exchange resin. This resin had double the binding capacity for bHb compared to three other anion exchange resins that were studied in this work. Methemoglobin levels remained below 2% with bHb concentrations between 0.7 and 1.7 mM. The high purity of bHb was confirmed via SDS-PAGE and size exclusion chromatography (SEC).     

Nuclear magnetic resonance chemical shifts of potassium ions (39K) on ion exchange resins and in muscle

Chemical shifts of potassium (39K) were calculated from frequencies of beat patterns measured by a pulsed NMR method. This method indicates large chemical shifts for 3 molar KNO3 and 6 molal KI in good quantitative agreement with the steady state NMR measurements of previous investigators. 39K on two wet ion exchange resins and 39K in fresh muscle show insignificant chemical shifts relative to 0.1 M KCl solution. Previous studies showed marked shortening of NMR relaxation times (T1 and T2) for 39K in ion exchange resins and in muscle compared to free solution. These results seem to indicate that even though potassium on resins and in muscle experiences high electric field gradients, these have relatively little effect on the chemical shift of potassium, which may be correlated with the low pK values of the anionic groups in the resins and muscle.     

Remediation of depleted soils by addition of ion exchange resins

Parallel investigations with fertility were carried out in standard garden soil with ion exchange substrate BIONA 111 as well with mixtures in different proportions. The ion exchange substrate was a mixture of ion exchange resins saturated in certain proportions with a complete set of biogenic ions. Plant productivity in the ion exchange substrate in a 6-week vegetation period was 950 g/kg of the green biomass compared with 29 g/kg in soil. Productivity linearly depended on the mass fraction of the ion exchange substrate in the mixtures with the garden soil. Addition of 1% of the ion exchange substrate is sufficient for starting vegetation in completely depleted soil and barren sand. Addition of different ionic forms of ion exchange resins (K⁺, Ca²⁺+Mg²⁺+K⁺, NO₃⁻, NO₃⁻+H₂PO₄²⁻+SO₄²⁻) caused pronounced positive effects on soil productivity though these effects were less significant than those of ion exchange substrate. Addition of ion exchange substrates can be an efficient means for remediation of destroyed soils and fruitless rocks.