Continuous purification of a clotting factor IX concentrate and continuous regeneration by preparative annular chromatography

Preparative continuous annular chromatography, a method to separate proteins in a truly continuous manner, was investigated in an industrial environment. Plasma-derived clotting factor IX concentrate was used as model protein. Separation of vitronectin, a common impurity in commercial available factor IX concentrates, from factor IX was studied and compared to conventional packed bed chromatography in batch mode. As sorbent, Toyopearl DEAE 650M was used. Regeneration was performed simultaneously with the purification of factor IX in continuous mode. All required parameters applied for preparative annular chromatography such as feed flow-rate and elution flow-rate were first estimated from experiments on conventional batch columns. Then preparative annular chromatography and conventional packed beds were compared regarding enrichment, purity and productivity. Three different process scenarios, the optimal batch process,the preparative annular chromatography process and the batch process equivalent to the preparative annular chromatography process were investigated. The productivity of the optimal batch process was higher than that of the preparative annular chromatography and batch process equivalent to the preparative annular chromatography process. Therefore the throughput could not be increased by the use of the continuous chromatographic system.     

Continuous chromatographic protein refolding

Column-based protein refolding requires a continuous processing capability if reasonable quantities of protein are to be produced. A popular column-based method, size-exclusion chromatography (SEC) refolding, employs size-exclusion matrices to separate unfolded protein from denaturant, thus refolding the protein. In this work, we conduct a comparison of SEC refolding with refolding by batch dilution, using lysozyme as a model protein. Lysozyme refolding yield was found to be extremely sensitive to the chemical composition of the refolding buffer and particularly the concentration of dithiothreitol (DTT) introduced from the denatured protein mixture. SEC refolding was not adversely affected by DTT carry-over as small contaminants in the denatured solution are separated from protein during the refolding operation. We also find that, contrary to previous reports, size-exclusion refolding on batch columns leads to refolding yields slightly better than batch dilution refolding yields at low protein concentrations but this advantage disappears at higher protein concentrations. As batch-mode chromatography would be the limiting step in a column based refolding downstream process, the batch column refolding method was translated to a continuously operating chromatography system (preparative continuous annular chromatography, P-CAC). It was shown that the P-CAC elution profile is similar to that of a stationary column, making scale-up and translation to P-CAC relatively simple. Moreover, it was shown that high refolding yields (72%) at high protein concentration (>1 mg ml(-1)) could be obtained.     

Continuous matrix-assisted refolding of proteins

A refolding reactor was developed for continuous matrix-assisted refolding of proteins. The reactor was composed of an annular chromatography system and an ultrafiltration system to recycle aggregated proteins produced during the refolding reaction. The feed solution containing the denatured protein was continuously fed to the rotating bed perfused with buffer promoting folding of the protein. As the protein passed through the column, it was separated from chaotropic and reducing agents and the refolding process took place. Native proteins and aggregates could be continuously separated due to different molecular size. The exit stream containing aggregates was collected, concentrated by ultrafiltration and recycled to the feed solution. The high concentrations of chaotropic and reducing agents in the feed solution enabled dissociation of the recycled aggregates and consequently were fed again to the refolding reactor. When the initial feed mixture of denatured protein is used up, only buffer-containing chaotropic agents and recycled aggregates are fully converted to native protein. This process resulted in a stoichiometric conversion from the denatured protein to its correctly folded native state. The system was tested with bovine alpha-lactalbumin as model protein. Superdex 75 PrepGrade was used as size-exclusion medium. The yield of 30% active monomer in the batch process was improved to 41% at a recycling rate of 65%. Assuming that the aggregates can be redissolved and recycled into the feed stream in a quantitative manner, a refolding yield close to 100% is possible. The method can be also applied to other chromatographic principles suited for the separation of aggregates.     

Displacement chromatography of biomolecules

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.     

Large volume injection for preparative supercritical fluid chromatography

Summary A large volume injection system for preparative supercritical fluid chromatography is described. The method which is based on the solvent venting technique coupled with dilution of the sample solution consists of three steps. The first step is continuous dilution of the sample solution with liquid carbon dioxide at a controlled flow rate. The second step is solvent removal and solute trapping in a packed trap column. Combination of these two steps results in efficient solvent removal and the volume of sample which can be injected in a single injection becomes virtually unlimited. The third step is transfer and re-concentration of the solutes from the trap column on to the separation column with the pressures of both columns controlled independently; the final step is the separation. With this method, mass overloading behavior has been investigated and preparative separations performed.     

Impact of adsorption isotherm parameters on the performance of enantioseparation using simulated moving bed chromatography

Often there are several chromatographic systems, i.e., combinations of mobile and stationary phases, available to solve a certain separation problem. Essential differences of these chromatographic systems are the separation factors and the efficiencies. For preparative applications in addition also the column saturation capacities and solubility limits are of importance. The impact of all these parameters appears to be rather well understood for conventional overloaded elution chromatography using a single column. In the last years the continuous simulated moving bed (SMB) process was increasingly used as a powerful alternative to batch elution since increased productivities and reduced solvent consumptions could be realised. However, the selection of suitable chromatographic systems is more sophisticated for this process. In this paper five different chromatographic systems capable of separating the enantiomers of mandelic acid are compared based on the achievable productivities using SMB chromatography. For these five systems the adsorption isotherms have been determined experimentally. Subsequently, an analysis of the SMB process was performed numerically using a well-established model.     

Size-exclusion chromatographic protein refolding: fundamentals, modeling and operation

Size-exclusion chromatography (SEC) has proven its capability to refold a variety of proteins using a range of gel filtration column materials, demonstrated in the growing body of experimental evidence. However, little effort has been allocated to the development of mechanistic models describing size-exclusion chromatographic refolding reactors (SECRR). Mechanistic models are important since they provide a link between process variables like denatured and reduced protein feed concentration (C_f,D&;R), flow rate, column length, etc., and performance indicators like refolding yield (Y_N), thereby opening the possibility for in silico design of SECRRs. A critical step, in the formulation of such models, is the selection of an adequate reaction mechanism, which provides the direct link between the separation and the refolding yield. Therefore, in this work we present a methodology using a SEC refolding reactor model, supported by a library of reaction mechanisms, to estimate a suitable reaction scheme using experimental SEC refolding data. SEC refolding data is used since it provides information about the mass distribution of monomers and aggregates after refolding, information not readily available from batch dilution refolding data alone. Additionally, this work presents (1) a systematic analysis of the reaction mechanisms considered using characteristic time analysis and Damköhler maps, revealing (a) the direct effect of a given reaction mechanism on the shape of the SEC refolding chromatogram (number of peaks and resolution) and (b) the effect that the competition between convection, refolding and aggregation is likely to have on the SEC refolding yield; (2) a comparison between the SECR reactor and the batch dilution refolding reactor based on mechanistic modeling, quantitatively showing the advantages of the former over the latter; and (3) the successful application of the modeling based strategy to study the SEC refolding data of an industrially relevant protein. In principle, the presented modeling strategy can be applied to any protein refolded using any gel filtration material, providing the proper mass balances and activity measurements are available.     

Preparative size-exclusion chromatography for purification and characterization of colloidal quantum dots bound by chromophore-labeled polymers and low-molecular-weight chromophores

We explore the use of preparative size-exclusion chromatography (SEC) and high-performance liquid chromatography (HPLC) to purify quantum dots (QDs) after surface modification. In one example, in which Bio-Beads (S-X1) were used as the packing material for the preparative SEC column, CdSe QDs treated with a functional coumarin dye could be separated from the excess free dye by using tetrahydrofuran (THF) as the mobile phase. This column was unable to separate polymer-coated QDs from free polymer (M ∼ 8000) because of the relatively low cutoff mass of the column. Here a preparative HPLC column packed with TOYOPEARL gel allowed the effective separation of polymer-bound QDs from the excess free polymer by using N-methyl-2-pyrrolidinone (NMP) as the mobile phase. When other solvents such as absolute ethanol, acetonitrile, THF, and THF–triethylamine mixtures were used as the eluent, QDs stuck to the column. While NMP was an effective medium to remove excess free polymer from the QDs, it was difficult to transfer the purified QDs to more volatile solvents and maintain colloidal stability.     

Analysis of aggregates of human immunoglobulin G using size-exclusion chromatography,static and dynamic light scattering

Large aggregates (Mr: 10(6)-10(7) g/mol) of human immunoglobulins are present in extremely small concentrations in IgG preparations (<0.1%). Traces of large protein aggregates cannot be determined by conventional size-exclusion chromatography (SEC) using UV detection due to limitations in sensitivity. The conventional analysis of IgG by SEC is limited to dimers and oligomers. Using light scattering it is possible to determine significant differences concerning the aggregate composition and the extent of protein aggregation in samples of different process steps. Two different pilot preparations were analyzed by SEC with UV and static light scattering detection and compared to dynamic light scattering in the batch mode. The change of large aggregates could be monitored and data were corroborated by dynamic light scattering.     

Effect of steric exclusion on the separation of proteins by hydrophilic size-exclusion chromatography

On the basis of studying the retention and band broadening of proteins on the TSK SW column, diffusion coefficients (Ds) of solute in stationary phase were obtained which elucidate the hydrodynamic process of chromatographic resolution of proteins by hydrophilic size-exclusion chromatography (SEC). After calculating the correlation between Ds and the molecular weight of the solute, the molecular dimensions of proteins in the process of chromatographic separation can be predicted. Deviations in diffusion coefficient of a protein from the calculated value reflect differences of measured molecular dimensions from molecular volumes predicted from the calibration curve of the SEC column. This study illustrates a convenient method for estimating the purity of proteins by SEC. Deviations from 2 lambda dp (where dp is the particle diameter) in the intercept of the theoretical plate height (H) versus flow-rate (U) curve from the band broadening equation H = CsU + 2 lambda dp + f(alpha M)T (where CsU represents mass transfer resistance caused by solute diffusion in the stationary phase and f(alpha M)T an added term for polydisperse solutes as proposed by Knox and McLennan [Chromatographia, 10 (1977) 75]) reflect impurities in the proteins.     

Präparative Hochdruck-Säulenflüssigkeits-Chromatographie

Several aspects of the apparatus and column technology of modern preparative column liquid chromatography are described together with a review of the present state of the art. We can state: one can today so construct and fill preparative high-speed columns that the separation and isolation of individual components from mixtures in quantities sufficient for tentative identification (spectroscopic and CHN analysis c. 1 mg), structural elucidation, or mechanical, physical, electrical and last but not least, biological tests (ca. 100 mg) is possible. Additionally, by optimal use of “scale up” columns one can provide an additional tool, which may be used for research and development on the gram scale and may be described as a modern time- and money-saving technique. Unfortunately, up until now, only few systematic studies and applications which make full use of the preparative possibilities of modern column chromatography have been published. Only a few of the instrument manufacturers and accessory suppliers are active in this area. For this reason, compared to the rate of development in analytical aspects, the development of commercial preparative equipment is less well advanced. There remain, therefore, several questions open regarding apparatus and operation of such preparative columns, e.g. batch versus continuous operation, or maximum attainable diameter of columns.     

Preparative high-performance liquid chromatography with reversed phase packed glass columns

An efficient system for preparative reversed-phase separations with packed glass columns is described. The advantage of this system is the use of relatively simple and inexpensive equipment. Column performance, load capacity, effect of the feed volume and the feed concentration on peak broadening are shown. The influence of the selectivity and the capacity factors on column load have been measured. The effect of the column dimensions is demonstrated by means of practical applications. The loading capacity of a column depends on the thermodynamic proporties of the separation system used. It is therefore not expedient in preparative chromatography to correlate the loading capacity of a column by means of grams dissolved per grams of adsorbent.     

Dispersive mixing and intraparticle partitioning of protein in size-exclusion chromatographic refolding

Refolding enables bioprocesses predicated on proteins expressed as inclusion bodies in Escherichia coli. Optimization of size-exclusion chromatography (SEC) refolding is a significant challenge because a wide range of factors, including the choice of gel media, the column dimensions and configuration, affect the final yield in a protein-specific manner. In this study, we investigated these factors by relating them to dispersive mixing and partitioning of refolding molecules within the SEC pore structure. Lysozyme was refolded using SEC resins giving different column dispersion and chromatography resolution. Despite a low separation resolution, the desalting SEC resin Sephadex G-25 resulted in a refolding yield that was 12-30% higher than those obtained with Superdex 75 and Superdex 200. This finding supported the notion that SEC refolding was enhanced by dispersive mixing, which was increased by a wide particle size distribution of the Sephadex G-25 used. Column dispersion was further improved by strategically placing an inlet gap before the packed resin beds, leading to a 20% increase in refolding yield. Refolding yield in Superdex 75 was 20% higher than that in Superdex 200 under conditions giving similar dispersive mixing. This yield enhancement is expected to be protein-specific since Superdex 75 was chosen to specifically maximize partitioning of lysozyme molecules within the resin particles, reducing the likelihood of aggregation during refolding. The highest refolding yield (65%) was achieved using a Sephadex G-25 column with a 15 mm inlet gap, suggesting that desalting systems optimized for dispersive mixing might be an economical and generic alternative for preparative SEC protein refolding.     

Rapid ion-exchange chromatography for preparative separation of proteins. Application to porcine and bovine carbonic anhydrases

A method of rapid ion-exchange chromatography of DEAE-cellulose for preparative purposes is described. Basically, the flow-rate is increased by applying an air pressure on the column. By this technique it is possible to purify gram quantities of protein in 2-4 h with acceptable resolution. In preparations of bovine and porcine carbonic anhydrases the elution times were reduced by a factor of about ten compared to those of conventional methods. The enzymes purified in this way showed a high degree of homogeneity. The method should be generally applicable in protein purification, and especially advantageous in purification of unstable proteins where time-consuming separations often give rise to low yields of active material.     

Separation of proteins of nuclear ribonucleoprotein particles by high-performance liquid chromatography

High-performance liquid chromatography (h.p.l.c.) is used to fractionate the proteins of the 30–40 S nuclear ribonucleoprotein particles. The major core proteins of the particles are eluted from a SynChropak AX-300 anion-exchange column before the more acidic higher-molecular-weight minor particle proteins. Each of the three major core proteins which can be separated from the other particle proteins by preparative polyacrylamide gel electrophoresis are eluted from the SynChropak AX-300 column as one peak. Isoelectric focusing separates each of these three apparently homogeneous peaks into a series of charge isomers ranging in isoelectric pH (pI) from 5.5 to 9.0. The core proteins of the ribonucleoprotein particles have a strong affinity to each other and form aggregates. The elution of each of the charge isomers of the three major proteins in one peak and their elution from an anion exchanger before the elution of the more acidic higher-molecular-weight minor proteins of the nuclear ribonucleoprotein particles is explained by the formation of these aggregates. The separation of the total proteins of the nuclear ribonucleoprotein particles by h.p.l.c. is similar to the separation which can be obtained by preparative electrophoresis but the l.c. technique is simpler, substantially quicker, and adaptable to large-scale preparation.     

A Method of Correcting for Flow-Rate Fluctuations in Size Exclusion Chromatography Calculations: Applications to Methylene Chloride/Hexafluoroisopropanol Solvent System

Abstract

The mixture of methylene chloride/hexafluoroisopropanol (70/30, v/v) is an excellent polyester solvent, but its low boiling point causes unstable flow when it is used for size exclusion chromatography (SEC). In high-performance SEC experiments, retention time is normally used to measure elution volume; however, unstable flow makes it difficult to calibrate an SEC column set or calculate molecular weight parameters from a chromatogram. We have devised a simple and inexpensive method to compensate for the effect of unstable flow in SEC calculations. A calibration marker injected along with each sample is used to indicate flow-rate variations. The ratio of the sample retention time to the marker retention time is invariant to flow-rate changes and is used in place of retention time as a measure of elution volume in the universal calibration technique. Calibrating a column set and analyzing chromatograms by this method result in a large improvement in the accuracy and precision of calculated molecular weight parameters.     

Molecular mass distribution analysis of ethyl(hydroxyethyl)cellulose by size-exclusion chromatography with dual light-scattering and refractometric detection

Dual low-angle light scattering and refractometric detection coupled to size-exclusion chromatography provided proof for the presence of a low amount of stable aggregates/particles in ethyl(hydroxyethyl)cellulose. Unlike the correct size-exclusion chromatographic behavior of the parent polysaccharide itself, the aggregates exhibit variable size-dependent weak retention as a function of flow-rate and of ionic strength of the aqueous mobile phase. Therefore, determination of the molecular mass of non-aggregated polymer is possible in aqueous mobile phase containing 0.1 M NaCl under conditions at which aggregates are completely adsorbed on the column packing irrespective of the flow-rate used. Flow-rate and ionic strength-dependent variations of aggregate behavior as well as model size-exclusion experiments with latex particles indicate that they partly carry a minute charge and have a compact structure. Their weak retention under the separation conditions used suggests a difference in their surface chemistry when compared with the dissolved polymer coils which exhibit a correct size-exclusion behavior.     

Determination of pituitary and recombinant human growth hormone molecular weights by modern high-performance liquid chromatography with low angle laser light scattering detection

The determination of molecular weight for pituitary and recombinant human growth hormone (p-hGH/Crescormon and r-hGH/Protropin) has been performed. This has involved on-line coupling of size-exclusion chromatography (SEC) and gradient elution, reversed-phase high-performance liquid chromatography (RP-HPLC) with low-angle laser light scattering (LALLS) detection. A 5-microns, 300 A, Delta-bond octyl column was used. Traditional specific refractive index increment (dn/dc) and refractive index (n) measurements have been performed in order to derive absolute weight-average molecular weight (Mw) information for p-hGH and r-hGH. Known concentrations of each protein have been separated using reversed-phase gradients utilizing acetonitrile with on-line LALLS determination of excess Rayleigh scattering factors. Accurate Mw data has been obtained for both proteins under conventional RP-HPLC gradient elution conditions. SEC data of both hGHs were found to be concentration, mobile phase, and column dependent for the particular analyses. Both medium- and high-resolution SEC-LALLS studies were performed, and all of these determinations further confirmed our RP-HPLC results. On-line LALLs provides certain advantages in identifying aggregates that may be present, even in medium-resolution SEC, where incomplete resolution occurs. The on-line coupling of modern RP-HPLC for biopolymers with LALLS detection represents a major step forward in the ability of bioanalytical chemists to determine the nature (monomer versus higher-order aggregate) of such materials. Other classes of biopolymers should prove suitable for studies with the same RP-HPLC-LALLS-UV approaches.     

Phosphatidylcholine isolation from egg yolk phospholipids by high-performance liquid chromatography

Cell membrane components have been increasingly recognized as important biochemicals in the fields of biochemistry and pharmacy due to their relationship with metabolite transport in the cells. Among the components, phosphatidylcholine (PC) is considered a valuable biochemical, because it is difficult to commercialize. PC demand has been largely increased in the fields of the nutrient, cosmetic and pharmacy industries, and so the development of a preparative chromatography process is critical to supply a low-cost PC. In this study, we investigated the HPLC separation of phospholipid originated from egg yolk, which contains 80% (w/w) PC and 15% (w/w) phosphatidylethanolamine. Column temperature, mobile phase composition and its flow-rate and kinds of stationary phase were varied to understand the effectiveness of PC separation. For studying the relationship between recovery yield and sample loading amount in HPLC, we performed overloading experiments. In this way, we successfully separated PC with over 99% purity and with 98% yield with the following HPLC operating conditions; pure methanol as a mobile phase, 2.0 ml/min flow-rate and 1000 mg/ml feed concentration in a KR-100-10SIL column.     

Short metal capillary columns packed with polymer-coated fibrous materials in high-temperature gas chromatography

The high-temperature gas chromatographic (GC) separation of several semivolatile compounds is studied with a short metal capillary column packed with fibrous material, having a polydimethylsiloxane coating thereon. Taking advantage of the excellent heat-resistance of the fiber and also the combination of the surface-deactivated metal capillary, a temperature-programmed separation up to 450 degrees C is successfully demonstrated for the separation of polymer standard samples. The average molecular weight of the commercially-available polymer standard samples for size exclusion chromatography (SEC) is estimated by high-temperature GC analysis and compared with the nominal value determined by a conventional SEC method. Although a slight deviation for the number-average molecular weight is observed between the GC and SEC analysis, the data for the weight-average molecular weight shows a good agreement in these methods. The results also suggest the future possibility of the fiber-packed metal capillary as a miniaturized GC column with an increased sample loading capacity.