Selection of an optimal assay method for monitoring cyclosporine therapy.
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Biomedical subjects
Publications and source records attributed to S M Cramer.
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Displacement chromatography was used for the preparative-scale separation of peptides, antibiotics, and proteins. The feed components were both purified and concentrated during the separation processes. The components of a peptide mixture were separated on a reverse-phase analytical column using 2-(2-butoxyethoxy) ethanol as the displacer. The use of organic modifiers in the carrier along with an elevated column temperature of 45 degrees C enabled the efficient separation of relatively hydrophobic peptides by displacement chromatography. In addition, the throughput of the process was significantly increased by carrying out the separation at an elevated flow-rate with no adverse effect on product purity. The antibiotic cephalosporin C was isolated from impurities in a fermentation broth using 2-(2-butoxyethoxy)ethanol as the displacer along with a step change in column temperature. The proteins cytochrome c and lysozyme were purified on a weak cation-exchanger column using cationic polymers as the displacers. While polymers of 60 and 20 kilodaltons were both found to be good displacers for these proteins, only the lower molecular weight polymer was readily removed from the column by standard regeneration techniques.
A packed-bed enzyme reactor with immobilized carboxypeptidase Y was used in tandem with a displacement chromatograph for the preparation of N-benzoyl-L-arginyl-L-methioninamide, from N-benzoyl-L-arginine and L-methioninamide. The pumps and valves of the coupled enzyme reactor and displacement chromatograph were controlled by a microprocessor. The enzyme was immobilized on microparticulate amino-silica by glutaraldehyde and packed into a 60 X 4.6 mm I.D. column. The packed-bed reactor was used in the recirculating mode and components of the reaction mixture were subsequently separated by displacement chromatography on a 250 X 4.6 mm octadecyl-silica column using butoxyethoxyethanol as the displacer. Unreacted L-methioninamide was returned to the reaction mixture. Both the progress of the reaction and the extent of separation by displacement chromatography were monitored by high-performance liquid chromatographic analysis. The system was designed so that enzymatic peptide synthesis, separation by displacement chromatography, and column regeneration were carried out simultaneously by using two identical columns in parallel. An amount of 460 mg of N-benzoyl-L-arginyl-L-methioninamide having purity greater than 99% could be obtained in 24 h with this system. The tandem operation of the enzyme reactor and liquid chromatograph operated in the displacement mode offers a means for the synthesis and purification of peptides.
The assay of the complexed (ferrioxamine) and uncomplexed forms of deferoxamine, a strong iron(III) chelating agent, by reversed-phase high-performance liquid chromatography was investigated. Complex formation with trace amounts of iron in the chromatographic system hinders the assay of deferoxamine by causing appearance of unexpected peaks, reaction zones and variations in retention time. By purging the column with deferoxamine and using EDTA in the mobile phase, these adverse effects in the determination of deferoxamine were eliminated. No interference by iron contamination of the chromatographic system was found in the assay of ferrioxamine, which is facilitated by the strong absorption of the analyte at 430 nm.
Methotrexate from various commercial sources has been found to contain 0.5 to 48% (w/w) of the enantiomer D-methotrexate. The two methotrexate enantiomers were separated by using chiral high-performance liquid chromatography with an octadecyl silica column and a mobile phase containing L-proline and cupric nitrate. For the assay of D-methotrexate impurity in commercial methotrexate, L-methotrexate was hydrolyzed with carboxypeptidase G1, and the remaining D-methotrexate was quantitated by high-performance liquid chromatography. The biological effects of D-methotrexate were investigated and compared to that of L-methotrexate. D-Methotrexate was found to be a good inhibitor of dihydrofolate reductase from both murine and human tumor cells, but was a poor inhibitor of L1210 and CCRF-CEM cell growth. In animal experiments with dogs and mice, D-methotrexate was rapidly absorbed from the intestine and excreted by the kidneys.
Anisotropic polysulfone membranes were prepared with carboxypeptidase G1 embedded in the polymer structure. The enzymatically active flat and hollow-fiber membranes were obtained by precipitating the polymer from solution in an organic mixture in which an aqueous solution of the enzyme had been dispersed. The process has been found to be particularly suitable for the immobilization of enzymes in anisotropic hollow fibers that exhibited no detectable enzyme leakage upon perfusion. The pH profiles measured with the enzyme in free solution and in the embedded form were similar. Kinetic parameters of multitubular enzyme reactors were investigated by measuring the rate of hydrolysis of glutamate from folic acid or methotrexate at different flow rates and substrate concentrations. The relatively slow mass transfer in such reactors was found to affect strongly the observed kinetics. The results of in vitro experiments with 5000 fiber reactors suggest that hollow fiber cartridges prepared with such membranes have clinical potential for the extracorporeal removal of methotrexate from blood.
High affinity, low molecular weight anionic displacers were successfully employed for the purification of antisense oligonucleotides. Several important structural characteristics were identified that contribute to the affinity of low molecular weight displacers to a hydrophilized polystyrene divinyl benzene anion exchanger. Sulfonic acid groups were found to possess higher affinity than carboxylic acid and phosphate functionalities, and nonspecific interactions (particularly hydrophobic interactions) were shown to play a major role in the retention process on this stationary phase material. Using this information, two high affinity, low molecular weight displacers were identified. These molecules are relatively inexpensive organic dyes that possess multiple sulfonic acid moieties, as well as aromatic functionalities, which increase nonspecific interactions with the stationary phase. These high affinity displacers, which can be readily detected, were then employed to displace several strongly retained antisense oligonucleotides that could not be displaced by previously established low molecular weight displacers. The displacement process resulted in very high purities of the antisense oligonucleotides. The results presented in this paper are significant in that they demonstrate that low molecular weight displacers for ion-exchange chromatography can possess equal to or greater affinities than their higher molecular weight counterparts, when nonspecific interactions with the stationary phase are exploited. In addition, the results illustrate the high resolutions possible with displacement chromatography and demonstrate an attractive technology for the process scale purification of oligonucleotides.
Protamine was investigated for its utility as a protein displacer in cation-exchange systems. Although the protamine solution contained several variants of the molecule, the high affinity of all of the components in this heterogeneous biopolymer enabled it to act as an efficient protein displacer. To facilitate parameter estimation of the protamine, a preliminary purification was carried out by preparative elution chromatography. Chromatographic parameters of both the feed proteins and protamine displacer were obtained for use in a multicomponent steric mass action ion-exchange displacement model. Model simulations were compared to displacement results under both moderate and intense induced salt gradient conditions. In both cases, excellent agreement was obtained between the displacement experiments and theoretical predictions. In addition, these studies serve to dramatize the importance of induced salt gradients in ion-exchange displacement systems.
This work investigates the utility of RPLC displacement chromatography for the purification of recombinant brain derived neurotrophic factor (rHu-BDNF) from its variants and E. coli. protein (ECP) impurities. The closely associated variants (six in total) differ by one amino acid from the native BDNF and thus pose a challenging separation problem. Several operational parameters were investigated to study their effects on the yield of the displacement process. The results indicated that the concentration of trifluoroacetic acid (TFA) in the buffer was a key factor in achieving the desired purification. Displacement chromatography on an analytical scale column resulted in extremely high purity and yield in a single chromatographic step. The process was successfully scaled-up with respect to particle and column diameter. The production rate of a pilot scale RPLC displacement process was shown to be 23 times higher than the combined production rates of the current preparative ion exchange and hydrophobic interaction gradient elution steps that are used to remove variant and ECP impurities, respectively.
An optimization framework based on the use of hybrid models is presented for preparative chromatographic processes. The first step in the hybrid model strategy involves the experimental determination of the parameters of the physical model, which consists of the full general rate model coupled with the kinetic form of the steric mass action isotherm. These parameters are then used to carry out a set of simulations with the physical model to obtain data on the functional relationship between various objective functions and decision variables. The resulting data is then used to estimate the parameters for neural-network-based empirical models. These empirical models are developed in order to enable the exploration of a wide variety of different design scenarios without any additional computational requirements. The resulting empirical models are then used with a sequential quadratic programming optimization algorithm to maximize the objective function, production rate times yield (in the presence of solubility and purity constraints), for binary and tertiary model protein systems. The use of hybrid empirical models to represent complex preparative chromatographic systems significantly reduces the computational time required for simulation and optimization. In addition, it allows both multivariable optimization and rapid exploration of different scenarios for optimal design.
A recent advance in the state of the art of displacement chromatography has been the development of selective displacement chromatography. In this process, the bioproduct of interest is selectively displaced while impurities with lower retention are eluted in the induced salt gradient and higher retained impurities are desorbed after the breakthrough of the displacer front. In this manuscript, selective displacement chromatography is employed to purify an antigenic vaccine protein (AVP) from an industrial process stream. Displacers were screened and an operating regime plot was employed to establish appropriate conditions for selective displacement. The selective displacement process was successful and resulted in AVP that was equivalent in purity to product obtained at commercial production scale after conventional step gradient chromatography. Methods used to characterize the purified protein include size-exclusion chromatography, SDS-PAGE, isoelectric focusing, N-terminal amino acid sequence analysis, and amino acid composition analysis. This is the first report of the purification of a commercially and pharmaceutically significant protein using selective displacement chromatography and thereby sets the stage for the implementation of selective displacement chromatography for the downstream processing of biologicals.