Modeling of size-exclusion chromatography of electrolytes on non-ionic nanoporous adsorbents

A dynamic model has been developed for chromatographic separation of mixed electrolyte solutions with non-ionic nanoporous adsorbents. The thermodynamic equilibrium condition at the pore entrance is written in terms of mixing, electrostatic and size-exclusion effects. The model is tested against experimental data measured with three binary mixtures on hypercrosslinked polystyrene and nanoporous carbon. The selectivity of the nanoporous adsorbents can be explained by the size-exclusion of the electrolytes and enrichment of both electrolytes in frontal chromatographic runs can be correlated satisfactorily with the proposed model. The model is also used to demonstrate continuous separation in a simulated moving-bed (SMB) system.     

Optimization of azeotropic protein separations in gradient and isocratic ion-exchange simulated moving bed chromatography

The separation of dilute binary mixtures of proteins by salt aided ion-exchange simulated moving bed (SMB) chromatography is optimized with respect to throughput, desorbent consumption and salt consumption. The optimal flow-rate ratios are analytically determined via an adopted "triangle theory". Azeotropic phenomena are included in this procedure. The salt concentrations in the feed and recycled liquid are subsequently determined by numerical optimization. The azeotropic separation of bovine serum albumin and a yeast protein is used to illustrate the procedure. Gradient operation of the SMB is generally preferred over isocratic operation. A feed of azeotropic salt concentration can only be separated in a gradient SMB. Desorbent and salt consumption are always lower in gradient than in isocratic SMB chromatography.     

Less common applications of simulated moving bed chromatography in the pharmaceutical industry

Simulated moving bed (SMB) chromatography is often perceived in the pharmaceutical industry as chromatographic method for separating binary mixtures, like racemates. However, SMB can also be used for unbalanced separations, i.e. binary mixtures of varying compositions and multi-component mixtures. These less common application modes of isocratic SMB chromatography are exemplified for four different compounds (racemates and diastereomers) and discussed in view of the so-called 'triangle theory' from an industrial perspective.     

Two-step solvent gradients in simulated moving bed chromatography. Numerical study for linear equilibria

The application of gradients in simulated moving bed (SMB) chromatography has recently attracted interest as a method for further improving the performance of this continuous separation process. One possible implementation of gradients consists in setting the solvent strength in the desorbent stream higher than that in the feed stream. As a result, the components to be separated are more retained in the zones upstream of the feed position and more easily eluted in the zones downstream of the feed position. If a liquid mobile phase is used, gradients can be created by dosing different solvents into the feed and desorbent ports. In a closed-loop gradient SMB arrangement the solvent strength within the unit will depend on the two feed compositions and on the characteristic flow-rates of the process. In this work an equilibrium stage model describing a true moving bed process is used to analyze numerically the main features of a two-step gradient SMB process. The adsorption isotherms are assumed to be always linear under isocratic conditions. The relevant Henry constants depend in a nonlinear manner on the composition of the solvent. Based on numerical simulations the impact of the two inlet solvent compositions is demonstrated in terms of the size and shape of regions of applicable flow-rates. Different strategies of designing the process are discussed and compared with respect to maximizing productivities and minimizing desorbent requirements.     

Separation of lactose from human milk oligosaccharides with simulated moving bed chromatography

The successful separation of the disaccharide lactose from a complex mixture of human milk oligosaccharides (HMOS) with the continuous chromatography of simulated moving bed (SMB) technique is described. Since lactose is the main carbohydrate in human milk with well-known functions for the infant, it is necessary to separate it from the rest of the oligosaccharides to divide them into less complex fractions and analyse their partial unknown functions. For separation of lactose from HMOS two different stationary phases (size-exclusion gel as well as ion-exchange gel) were used. As the main result, it is shown that a size-exclusion gel with the particle size of 50-100 microm and porosity of 50 A was the preferred stationary phase for our separation process with almost complete lactose separation and stable conditions.     

Recombinant protein purification using gradient-assisted simulated moving bed hydrophobic interaction chromatography. Part I: selection of chromatographic system and estimation of adsorption isotherms

The design of gradient simulated moving bed (SMB) chromatographic processes requires an appropriate selection of the chromatographic system followed by the determination of adsorption isotherm parameters in the relevant range of mobile phase conditions. The determination of these parameters can be quite difficult for recombinant target proteins present in complex protein mixtures. The first part of this work includes the estimation of adsorption isotherm parameters for streptokinase and a lumped impurity fraction present in an Escherichia coli cell lysate for a hydrophobic interaction chromatography (HIC) matrix. Perturbation experiments were carried out using a Butyl Sepharose matrix with purified recombinant protein on buffer equilibrated columns as well as with crude cell lysate saturated columns. The Henry constants estimated for streptokinase were found to exhibit in a wide range a linear dependence on the salt concentration in the mobile phase. These parameters were applied in subsequent investigations to design a simulated moving bed (SMB) process capable to purify in a continuous manner recombinant streptokinase from the E. coli cell lysate.     

Refolding human lysozyme produced as an inclusion body by urea concentration and pH gradient ion exchange chromatography

Summary A new dual-gradient ion exchange chromatographic method was developed to improve the refolding yield of human lysozyme produced inEscherichia coli as an inclusion body. The dissolved and stretched polypeptide chain in a concentrated non-ionic denaturant was adsorbed onto an ion exchange column and induced to refold by gradually decreasing the denaturant concentration and increasing pH in the flowing buffer. The dual gradients of denaturant concentration and pH provided a gradual change of the solution environment along the chromatographic column for the protein to refold, resulting in enhanced activity yield and purity. A post-separation was also studied using size-exclusion chromatography to remove protein aggregates and mis-folded proteins after the refolding step.     

Continuous voltage gradients and their application to true moving bed electrophoresis

Gradient elution has been practiced in chromatographic separations for many years. The application of discontinuous "step" gradients in simulated moving bed (SMB) chromatography has been very successful in increasing both processing rates and column productivity, resulting in a reduction in the number of SMB columns required. With the advent of the field gradient focusing techniques, electrophoresis has gained the ability to apply a continuous electric field gradient to a true moving bed (TMB) electrophoretic separation. Application of a spatial gradient allows a large degree of control of the product concentrations inside the separation unit as well as a large increase in product throughput. A model of moving bed electrophoretic separations has been developed that demonstrates the potential advantages of applying a continuous gradient to the moving bed process. These advantages include the reduction of detrimental peak tailing and the ability to decrease the concentrations of the compounds being separated in comparison with commonly used step gradient elution.     

Step gradients in 3-zone simulated moving bed chromatography. Application to the purification of antibodies and bone morphogenetic protein-2

The simulated moving bed (SMB) technology is a proven tool for efficient separation of binary mixtures. However, relying on isocratic conditions limits the applicability of the classical SMB approach when considering the field of bioseparations. Here, the use of gradients opens up new possibilities. A gradient in a SMB process can be established by using different solvent strengths in the incoming feed and desorbent streams, resulting in two internal plateaus of elution strength. Thus, compared to the conventional process, the overall amount of solvent needed can be reduced, productivity can be increased and more concentrated product streams can be obtained. In this contribution, two case studies will be presented. At first, the separation of bovine IgG from lysozyme will be analyzed as a model system. Antibodies are a common target substance in bio-chromatography, as therapeutic monoclonal antibodies are among the most promising biopharmaceuticals. Using adsorption data obtained from single-column experiments, an appropriate SMB process was designed and implemented. The second target component is the active dimeric form of the bone morphogenetic protein-2 (BMP-2). This protein was isolated from a renaturation solution, which also contained its inactive monomeric form as well as other undefined proteins from the bacterial production strain. A 3-zone open-loop gradient-SMB approach was used successfully for both separations.     

Optimization strategy for simulated moving bed systems

Simulated moving bed (SMB) systems are of rising interest in the purification of pharmaceuticals or specialty chemicals (racemic mixtures, proteins, organic acids, etc.). This is particularly due to their advantage in solvent reduction, obtained productivity and purities as well as investment costs in comparison to eluent chromatography. This paper evolved from the need for a readily available algorithm in order to find optimal operating conditions for SMB chromatography systems with nonlinear or coupled adsorption isotherms. The herein developed algorithm is based on a semi-deterministic two-step approach. First, optimal operating conditions with regard to an objective function are found by knowing adsorption measurements only. In a second step actual SMB results are used to adapt the initial isotherm measurements and match the simulation with the experiment. The algorithm is verified on a bench-scale SMB unit applied for the separation of a racemic epoxide with Chiralcel-OD as stationary phase. The developed algorithm improved the productivity of the investigated experimental design by 24%.     

Chromatographic study of the conformational behavior of graft copolymers with a broad distribution of grafting densities in dilute solutions in selective solvents for grafts

A graft copolymer of poly(4-methylstyrene-graft-2-vinylpyridine) was prepared by the living “grafting onto” method. Its molecular weight and composition was analyzed by size-exclusion chromatography, liquid chromatography under limiting conditions of desorption, ¹H NMR, and light scattering. The results indicated a non-negligibly broad distribution of grafting density. Its conformational behavior was studied by reversed phase liquid chromatography with gradient elution. Targeted studies provided two discrete base-line separated fractions. Their compositions were estimated by pyrolysis gas chromatography. The results suggest that distinct chain conformations (differing in grafting density and interacting differently with stationary phase) exist in studied solutions and can be separated by well-tuned chromatographic techniques. Experimental data were analyzed and interpreted on the basis of theoretical and computer studies of the conformational behavior of graft copolymers in selective solvents.     

Shortcut method for evaluation and design of a hybrid process for enantioseparations

Hybrid processes for enantioseparations have a considerable potential for reducing investment and operational costs. An example is the combination of simulated moving bed (SMB) chromatography and selective crystallisation. However, the design of integrated processes is a difficult task. A shortcut method is presented that can serve as a tool for design and estimation of the potential of such processes. The approach requires only limited experimental data and thus allows for systematic parameter studies. The method is based on the determination of the purity-performance characteristic of the SMB process and rigorous application of mass balances. The use of relative mass fluxes allows derivation of simple algebraic expressions for essential process parameters. The significant potential of combining SMB and crystallisation is demonstrated for the example of the separation of mandelic acid enantiomers.     

Coupling of simulated moving bed chromatography and fractional crystallisation for efficient enantioseparation

An optimised coupling of liquid chromatography and fractional crystallisation is suggested for efficient enantioseparation. As a first stage, a chromatographic separation, preferably simulated moving bed (SMB) chromatography, is applied to achieve an enantiomeric enrichment sufficient for a subsequent crystallisation. First results of the experimental and modelling work for the model system (+)-/(-)-mandelic acid in an aqueous solution are described. Chromatographic investigations involve the estimation of adsorption isotherms on a suitable chiral stationary phase and the simulation and optimisation of a corresponding SMB process. From the ternary phase diagram measured for the (+)-/(-)-enantiomer/ solvent system, the conditions required to crystallise a pure enantiomer from an asymmetric mixture can be derived. The productivity gains achievable from the combined process compared to the application of chromatography alone are discussed.     

Novel simulated moving-bed method for reduced solvent consumption

Simulated moving-bed (SMB) chromatography is attractive for reducing sorbent and solvent consumption relative to fixed-bed systems. In this contribution, we describe a novel and versatile method for further reducing solvent consumption in the case of reversed-phase chromatography. The method is based on the variation of the distribution coefficients of solutes to be separated upon varying the composition of a multi-component mobile phase. If the solvent strength of the desorbent is set higher than the solvent strength of the feed, the components will have smaller distribution coefficients in the extraction section of the SMB and hence will be more easily eluted. This will result in a lower desorbent flow and possibly also in a shorter desorbent zone, and, ultimately, in more concentrated products. The so-called "Triangle-method" by Storti et al. [AIChE J., 39 (1993) 471] to obtain the region of complete separation, is extended for this novel SMB method. Theoretical evaluation of the proposed methodology supports the anticipated solvent reduction relative to fixed-bed RP-HPLC for the cases of the purification of the polyketide antibiotic nystatin and the separation of bovine insulin from porcine insulin.     

Multidimensional chromatographic separation of estrogen receptors

Analyses of estrogen and progesterone receptors in biopsies of breast carcinoma play a vital role in the selection of patients likely to respond to hormone manipulation. Sucrose density gradient centrifugation has been the reference method in the determination of estrogen receptors in human breast carcinoma cytosols. To reduce assay time and circumvent prolonged manipulation of labile receptor preparations, high performance liquid chromatography techniques in the size-exclusion and ion-exchange modes were compared as potential alternate methods for the rapid separation of receptor isoforms. Multidimensional analyses were performed by reapplying estrogen receptor isoforms obtained from high performance size-exclusion and ion-exchange chromatography to sucrose density gradients and vice versa. This confirmed that the estrogen-binding components identified by high performance liquid chromatography appear to correspond to estrogen receptor species from sucrose density gradients.     

Analysis of polyethyleneoxide macromonomers by liquid chromatography along the critical adsorption line

Polyoxyethylene macromonomers are analyzed by one-dimensional liquid chromatography under different conditions, depending on the required information. These samples may contain polyethylene glycol (PEG) and the corresponding di(meth)acrylate besides the desired mono(meth)acrylate. The molar mass distribution (MMD) of the PEG and the monoester can be obtained by liquid adsorption chromatography (LAC) on a reversed-phase column in acetone–water with a gradient from 10% to 20% acetone. The MMD of the diesters can be obtained with isocratic elution by liquid chromatography at critical conditions (LCCC) on a reversed-phase column in 31% acetone, or using size-exclusion conditions for PEG and LAC conditions for the end groups, which is the case in 40–55% acetone. The absolute amount of the series with different functionality can be obtained by LCCC in ternary mobile phases consisting of acetone, methanol, and water along the critical adsorption line. Under such conditions, all series elute as narrow peaks (regardless their MMD), which can easily be integrated and quantified.     

Separation and determination of non-ionic surfactants of the nonylphenol polyglycol ether type by liquid chromatography

A normal-phase method for the separation and determination of non-ionic surfactants of the 4-nonylphenol polyglycol ether (NPEO) type by liquid chromatography is described, based on a LiChrosorb-Diol column and nonpolar linear gradient elution, with spectrophotometric detection at 275 nm. The method was applied to the determination of NPEO oligomers in the technical surfactants Arkopal N-20, N-40, N-60 and N-100 and in aqueous solutions from flotation processes. The relative standard deviations were 2.47–5.62%. The detection limits for nonylphenol polyglycol ether with 2, 4, 6, 8, 10, 13 and 15 ethoxy units were 51, 57, 64, 74, 85, 118 and 132 ng, respectively. The method can also be used for the determination of other alkylphenol polyglycol ethers. Reversed-phase LC with an octadecylsilica column was investigated and can be applied to the identification of the alkyl group present.     

Effect of mobile phase composition on the SMB processes efficiency. Stochastic optimization of isocratic and gradient operation

The solvent composition was adjusted in a theoretical study in order to maximize the efficiency of a simulated moving bed (SMB) process. The isocratic realization of the process as well as the solvent gradient mode were considered. The solvent composition and the flow rates were used as decision variables in a random search optimization algorithm known to be a reliable tool for nonlinear programming problems. The results of the optimization indicate that the optimal composition of the mobile phase depends strongly on the feed concentration. The asymmetry of the internal concentration profiles, which has a negative effect on the separation efficiency, can be partly damped by an increase of the solvent strength. In the cases studied the optimal solvent strength determined for concentrated feed streams is higher than that for diluted ones. Moreover, the optimum is strongly influenced by the value of the selectivity factor and its dependency on the mobile phase composition. Different results were obtained for cases, in which the separation factor increases with increasing the modifier concentration, than for cases, in which the separation factor decreases with increasing the modifier concentration. A similar analysis was performed for a solvent gradient SMB process, in which different solvents are used at the two inlet ports: a weak solvent in the feed stream and a strong solvent in the desorbent stream. Again the optimal mobile phase composition was strongly affected by the type of the isotherms and their non-linearity. The potential of a gradient SMB process in terms of increasing the productivity and reducing the eluent consumption is exemplified.     

Simulated moving bed process with cyclic modulation of the feed concentration

The improvement of the simulated moving bed (SMB) process based on the introduction of a cyclic modulation of the feed concentration is described. It is demonstrated that such a feed concentration gradient during the shifting cycle can improve the performance significantly. The productivity and the product concentrations can be increased while simultaneously the solvent consumption can be decreased compared to the conventional SMB process with constant feed parameters.     

Poppe plots for size-exclusion chromatography

Poppe plots provide a clear and unambiguous way to discuss the performance limits of separation systems. The effects of particle size, pressure drop and column permeability can be illustrated using such plots. The performance limits of size-exclusion chromatography are of interest, due to developments in combinatorial chemistry and high-throughput experimentation. In these fields, fast separations of high-molecular-weight analytes are required. In this paper, Poppe plots will be presented for size-exclusion chromatography. Because of the very high-reduced velocities encountered, the Poppe plots are found to be significantly different from those commonly observed in HPLC. Fast separations in size-exclusion chromatography are not as unfavourable as suggested by conventional theory. The results are based on experimental data obtained for a wide range of polystyrenes (1.7-3.25 kDa) using THF as mobile phase, but may be equally valid in other cases.