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.     

Application of an SPR-based receptor assay for the determination of biologically active recombinant bone morphogenetic protein-2

Human bone morphogenetic protein-2 (hBMP-2) is a member of the human transforming growth factor- superfamily. Biologically active bone morphogenetic protein-2 (BMP-2) is a dimeric protein that binds in the first step of the signal transduction cascade to specific receptors on the cell-surface. This specific interaction of the dimeric protein with the extracellular ligand-binding domain (ECD) of the receptor was used to develop a receptor-based assay based on an optical biosensor system (Biacore 2000, Biacore AB, Uppsala, Sweden). The ECD of the BMP-receptor type IA, tagged with the Fc part of IgG (BMPR-IA-Fc), was immobilised on the surface of a dextran-protein A-coated sensor chip. Calibration curves were obtained with purified and biologically active recombinant hBMP-2 (rhBMP-2) that showed a linear range from approximately 5 to 250 nM rhBMP-2. Moreover, this assay was used to quantitatively follow the generation of biologically active protein during the renaturation from unfolded and reduced monomers to biologically active dimers. A refolding mixture containing renatured dimeric rhBMP-2 and not correctly folded monomers, was used as the sample solution without any further pre-treatment. It was proven that only the biologically active dimers were recognised by the immobilised receptor, so the generation of biologically active rhBMP-2 during the renaturation process could be monitored directly and rapidly. Furthermore, the results from the optical sensor obtained during the renaturation process showed a good correlation with the data obtained by non-reducing SDS-PAGE analysis carried out at the end of the renaturation process. These data show that the disulphide-bonded dimer corresponds to the biologically active protein capable of binding the BMP-receptor type IA.     

Recombinant protein purification using gradient assisted simulated moving bed hydrophobic interaction chromatography. Part II: process design and experimental validation

In the first part of this work adsorption isotherm parameters were acquired to describe the migration of recombinant streptokinase in Butyl Sepharose columns at different salt concentrations. Based on these results, a simulated moving bed (SMB) chromatographic process was designed and realised, which exploits a two-step salt gradient and allows the continuous separation of streptokinase from contaminants present in a clarified Escherichia coli cell lysate solution. This second part describes the design of the three-zone open-loop gradient SMB process applying both equilibrium theory and an equilibrium stage model and presents results of a series of experiments aiming to obtain pure streptokinase. Moreover, the potential of the SMB process and the design approach are evaluated.     

镍掺杂石墨相氮化碳的熔盐辅助微波法制备及光催化固氮性能

采用熔盐辅助微波法制备了可见光下具有优越光催化固氮性能的镍掺杂石墨相氮化碳.采用X射线衍射(XRD)、扫描电镜(SEM)、氮气吸附-脱附、紫外-可见光谱(UV-Vis)、X射线光电子能谱(XPS)、荧光光谱(PL)、程序升温脱附(TPD)和电化学阻抗谱(EIS)等手段对催化剂进行了表征.结果表明,熔盐辅助微波法使氮化碳催化剂从层状结构变为纳米颗粒状,并相互紧密堆积形成很多二次孔,增大了催化剂的比表面积.同时,在催化剂制备过程中,熔盐包裹住了催化剂原料,避免了镍离子与氧气的接触,使镍离子呈现出活性的Ni(Ⅰ)—N态和非活性的氧化镍态2种存在形式.Ni(Ⅰ)—N作为反应活性中心,能有效捕获光电子,提高电子-空穴分离效率,促进电子从掺杂镍离子向N2分子的迅速转移,实现氮气分子的活化,进而提高固氮性能.     

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.     

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.     

重组人干扰素-γ的制备与鉴定

用聚乙二醇200疏水相互作用色谱固定相(PEG200-STHIC)分别在色谱柱和色谱饼上完成了一步复性并同时纯化来源于大肠杆菌(E.coli)表达的重组人干扰素-γ(rhIFN-γ)。为了能使色谱分离方法用于不同来源的rhIFN-γ的纯化,对rhIFN-γ在反相色谱、离子交换色谱、固定化镍离子亲和色谱上的保留行为也进行了研究。色谱柱纯化的rhIFN-γ收集液经排阻色谱除盐和冷冻干燥得到rhIFN-γ干粉。用基质辅助激光解吸电离飞行时间质谱对rhIFN-γ干粉进行了测定,rhIFN-γ单体的相对分子质量为17184.0,二聚体的相对分子质量为34204.4。用细胞病变抑制法(CPEI)测定rhIFN-γ干粉的比活性为9.5×108 IU/mg。用十二烷基硫酸钠-聚丙烯酰胺凝胶电泳（SDS-PAGE）测定rhIFN-γ干粉的纯度高于95%。用色谱柱复性并同时纯化rhIFN-γ的质量回收率达到93.7%,纯度高于95%,比活性为4.3×107 IU/mg。结果表明,采用PEG200-STHIC色谱柱复性并同时纯化rhIFN-γ是一种十分高效的方法。     

Time-resolved fluorescence of tryptophans in yeast hexokinase-PI: effect of subunit dimerization and ligand binding

Time-resolved and steady-state fluorescence measurements have been performed on monomeric and dimeric forms of yeast hexokinase-PI. Observation of similar emission spectra and fluorescence decay parameters for both the forms of the enzyme suggests that tryptophan residue(s) are not likely to be present at the subunit-subunit interface and the process of dimerization does not perturb the local environment of tryptophan(s). The fluorescence decay of tryptophans in enzyme could be fitted to a bi-exponential function with two lifetime components, tau1 approximately 2.2 ns and tau2 approximately 3.9 ns. Binding of glucose, which is known to convert the 'open' conformation of the enzyme to a 'closed' active conformation, results in approximately 30% reduction in emission intensity and a selective decrease in tau1 from approximately 2.2 to approximately 1.1 ns. These effects can be reversed by the addition of trehalose 6-phosphate (an inhibitor of yeast hexokinase), suggesting that the trehalose 6-phosphate inhibits the enzyme by binding to its 'open' inactive conformation rather than competing with glucose to bind to the 'closed' active conformation. Binding of nucleotide ligands (ATP, ADP and adenyl-(beta,gamma-methylene)-diphosphate (AMPPCP)) to the monomeric or dimeric form of enzyme quenched the steady-state fluorescence by approximately 4-8%, but had no measurable effect on the distribution of lifetimes or on their magnitudes. Addition of nucleotides to the enzyme-glucose complex also did not produce any further change in fluorescence decay parameters. These results indicate that it is highly unlikely that the formation of a ternary enzyme-glucose-nucleotide complex from the binary enzyme-glucose complex is accompanied by a large conformational change in the enzyme, as has been surmised in some earlier studies.     

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.     

Separation of stereoisomers in a simulated moving bed-supercritical fluid chromatography plant

The combination of two techniques, simulated moving bed (SMB) and supercritical fluid chromatography (SFC), leads to an apparatus with unique features. Besides the known advantages of the SMB process, like reduced solvent consumption and its continuity, the use of supercritical carbon dioxide as the mobile phase offers an easy product recovery by depressurizing the supercritical fluid. Details of a SMB-SFC plant are presented for the first time. Due to the large number of process parameters a simulation of the SMB process is necessary to achieve optimal operating conditions. The most important thermodynamic information for a SMB process is the adsorption isotherms. Therefore, isotherms for two phytol isomers are measured and correlated. A fast dynamic model for the simulation of SMB is used to calculate the region of complete separation taking different column configurations and the compressibility of the mobile phase into account.     

Formation and Decomposition of the Methylplatinum(IV) Complex in the Mechanically Activated K2PtCl4 Powder–MeI Vapor System

Mechanical treatment of the K₂PtCl₄ solid salt in a vibrating mill results in Pt–Cl bond heterolysis to form coordinatively unsaturated Pt(II) complexes. At room temperature, the freshly treated K₂PtCl₄ salt absorbs methyl bromide and evolves methyl chloride to the gas phase. The reaction mechanism involves the following sequence of steps: the oxidative addition of methyl iodide to Pt(II) with the intermediate formation of Pt(IV) methyl complexes and the decomposition of the latter due to intramolecular reductive elimination with methyl chloride formation. The first step of the reaction of MeI with the preactivated surface of the K₂PtCl₄ salt is assisted by active sites, which are regenerated in each act of the chemical transformation of MeI into MeCl involving in the chain substitution of halogen in methyl iodide. The coordinatively unsaturated surface platinum complexes can act as such active sites. Due to their effective positive charge, they can provide electrophilic assistance to nucleophilic substitution. Chain termination is probably due to the coordination of the complex with a coordination vacancy and an interstitial chloride ion to the inactive K₂PtCl₄ complex.     

A calorimetric study of the different thermal behaviour of DNA in the isotropic and liquid-crystalline states

A difference between the thermal behaviour of the isotropic and liquid-crystalline state of sonicated DNA in aqueous salt solution containing poly(ethyleneglycol)(PEG) has been demonstrated. On cooling, a different degree of renaturation of thermally denaturated DNA is observed between samples which form the isotropic state and more concentrated samples which on cooling form the cholesteric state.     

The role of iron(II) phthalocyanine as a catalyst in Wacker oxidation of 1-decene

The Wacker oxidation of 1-decene to 2-decanone by dioxygen catalyzed by Pd(OAc)₂, hydroquinone and iron(II) phthalocyanine (FePc) in acidic aqueous dimethylformamide gives high yield m 40 min at room temperature. The major factors controlling the activity of the multi-component catalyst are the structure and morphology of the FePc, which were analyzed by IR spectroscopy, X-ray powder diffraction, scanning electron microscopy and BET surface area measurement. The dimeric μ-oxo(1) form of FePc is highly active, has higher surface area, and is less crystalline than the inactive monomeric β-FePc. The rate of oxidation using the most active catalyst is limited by the solubility of 1-decene in aqueous DMF.     

Separation of D‐psicose and D‐fructose using simulated moving bed chromatography

Simulated moving bed (SMB) processes have been widely used in the sugar industries with ion‐exchange resin as a stationary phase. D ‐Psicose, a rare monosaccharide known as a valuable pharmaceutical substrate, was synthesized by the enzymatic conversion from D ‐fructose. The SMB process was adopted to separate D ‐psicose from D ‐fructose. Before the SMB experiment, the reaction mixture including D ‐psicose and D ‐fructose was treated by a deashing process to remove contaminants, such as buffers, proteins, and other organic materials. Four columns packed with Dowex 50WX4‐Ca²⁺ (200–400 mesh) ion‐exchange resins were used in the four‐zone SMB. Single‐step frontal analysis was performed to estimate the isotherm parameters of each monosaccharide. The operating conditions of the SMB process were determined based on the Equilibrium Theory. According to the simulation of the SMB process, the purity and yield of extract product (D ‐psicose) achieved were 99.04 and 97.46%, respectively and those of raffinate product (D ‐fructose) were 99.06 and 99.53%, respectively. Under the optimized operating condition, complete separation (extract purity = 99.36%, raffinate purity = 99.67%) was achieved experimentally.     

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.     

Improving performance of a five-zone simulated moving bed chromatography for ternary separation by simultaneous use of partial-feeding and partial-closing of the product port in charge of collecting the intermediate-affinity solute molecules

The performance of a five-zone simulated moving bed (SMB) chromatographic process for ternary separation has been improved to a certain extent in previous researches by applying either a partial-feeding (PF) or a partial-closing of the extract-2 port (PCE(2)) to its operation. To make a further improvement, the strategy of applying both PF and PCE(2) simultaneously to the five-zone SMB operation was proposed in this study. The results from both equilibrium-theory analysis and detailed simulation proved that the proposed strategy, which was called PF-PCE(2) in this article, had the benefit of a synergy between the individual merits of PF and PCE(2) in the five-zone SMB performance. As a consequence, the PF-PCE(2) mode could surpass the PF and the PCE(2) modes by a wide margin and the standard mode by a much wider margin in the aspects of ternary-separation performance and throughput. For the separation system considered, the PF-PCE(2) mode was found to achieve more than 100% improvement, compared to the standard mode. Furthermore, such advantage of the PF-PCE(2) over all the other modes was greater as the selectivity between the intermediate-affinity and the highest-affinity components was reduced.     

Simulated moving bed technology with a simplified approach for protein purification. Separation of lactoperoxidase and lactoferrin from whey protein concentrate

Simulated moving bed (SMB) technology is a continuous chromatographic technique proven to have many advantages compared to conventional batch chromatography, such as: raised productivity and product concentration, reduced buffer consumption as well as more efficient use of raw material. In this study a 20 column SMB process for the separation of lactoperoxidase and lactoferrin from whey protein concentrate (WPC) was developed. A simplified approach with data from a single column experiment was used when designing the process. The SMB process data were compared to a theoretical scale-up of the breakthrough experiment reflecting the same 20 column set-up run in non-moving bed mode. The outcome of the comparison is a 48% raise in productivity, a 4.3 times decrease in buffer consumption, 6.5 times raise in target protein concentration with a raw material utilization which is slightly better for the SMB process.     

Experimental evaluation of the effect of a modified port‐location mode on the performance of a three‐zone simulated moving‐bed process for the separation of valine and isoleucine

The removal of isoleucine from valine has been a key issue in the stage of valine crystallization, which is the final step in the valine production process in industry. To address this issue, a three‐zone simulated moving‐bed (SMB) process for the separation of valine and isoleucine has been developed previously. However, the previous process, which was based on a classical port‐location mode, had some limitations in throughput and valine product concentration. In this study, a three‐zone SMB process based on a modified port‐location mode was applied to the separation of valine and isoleucine for the purpose of making a marked improvement in throughput and valine product concentration. Computer simulations and a lab‐scale process experiment showed that the modified three‐zone SMB for valine separation led to >65% higher throughput and >160% higher valine concentration compared to the previous three‐zone SMB for the same separation.     

Effect of the cooling rate on dimerization of C60(•-) in fullerene salt (DMI+)2·(C60(•-))·{Cd(Et2NCS2)2I-}

The salt (DMI(+))(2)·(C(60)(?-))·{Cd(Et(2)NCS(2))(2)I(-)} (1) containing fullerene radical anions, the anions of cadmium diethyldithiocarbamate iodide, and N,N'-dimethylimidazolium cations was obtained. Fullerenes are monomeric in 1 at 250 K and form three-dimensional packing in which each fullerene has nearly tetrahedral surroundings from neighboring fullerenes. Fullerenes with a shorter interfullerene center-to-center distance of 10.031(2) ? form spiral chains arranged along the lattice c axis. The convolution consists of four fullerene molecules. Dimerization realized in 1 within the spiral chains below 135 K manifests a strong dependence on the cooling rate. The "frozen" monomeric phase was obtained upon instant quenching of 1. This phase is stable below 95 K for a long time but slowly converted to the dimeric phase at T > 95 K. It exhibits a weak antiferromagnetic interaction of spins below 95 K (the Weiss temperature is -4 K), which results in the splitting of the electron paramagnetic resonance (EPR) signal into two components below 10 K. A disordered phase containing both C(60)(?-) monomers and singly bonded (C(60)(-))(2) dimers with approximately 0.5/0.5 occupancies is formed at an intermediate cooling rate (for 20 min). The position of each fullerene in this phase is split into three positions slightly shifted relative to each other. The central position corresponds to nonbonded fullerenes with interfullerene center-to-center distances of 9.94-10.00 ?. Two other positions are coincided to dimeric fullerenes formed with the right and left fullerene neighbors within the spiral chain. This intermediate phase is paramagnetic with nearly zero Weiss temperature due to isolation of C(60)(?-) by diamagnetic species and exhibits a strongly asymmetric EPR signal below 20 K. A diamagnetic phase containing ordered singly bonded (C(60)(-))(2) dimers can be obtained only upon slow cooling of the crystal for 6 h.     

Effect of the homogeneity of the column set on the performance of a simulated moving bed unit. II. Experimental study

Previous studies of the simulated moving bed (SMB) process assume identical characteristics of all the columns incorporated in a given unit. Due to the practical impossibility to manufacture identical columns, numerical applications of the theory to modeling and optimization use for each of the needed column parameter the average value for the entire column set. In this study, the effects of these simplifications on the actual productivity of the SMB process are evaluated by making exact calculations, i.e., by taking the differences in the porosity values into account. We apply a revised set of separation conditions previously introduced and derived from the equilibrium theory. Earlier theoretical results are compared to experimental results obtained in the study of the enantiomeric separation of Tr?ger's base on Chiralpak AD. Due to the nonLangmuirian character of the adsorption isotherms of these two compounds on the packing material used, the separation area cannot be determined analytically. As an alternative, a reliable numerical algorithm was used to scan a wider region and to define the separation area. The form of this area depends on the applied porosity values. A UV detector and a laser polarimeter located at one node of the SMB monitor on-line the internal concentration profiles. Excellent agreement between the calculated and the experimentally determined concentration profiles was obtained under nonlinear conditions. The influence of column-to-column variations on the performance of the SMB process was found to be more significant under nonlinear than under linear conditions.