Rapid and high throughput separation technologies--steady state recycling and supercritical fluid chromatography for chiral resolution of pharmaceutical intermediates

The SSR and SFC techniques were used for the enantiomeric resolution of three pharmaceutical intermediates at various sample scales. The separation conditions, the sample purities and yields, the productivities and the solvent consumptions were discussed in three case studies in this paper. In case (I), the SSR process was used for a low selectivity resolution of 2.0 kg of pharmaceutical intermediate. By using this separation process, a productivity of 750 g racemate/kg stationary phase/day was achieved, while solvent usage was minimized ( approximately 200 l/kg racemate). Case (II) pertained to the effectiveness of the SSR process. Productivity using SSR techniques increased by a factor of 4.5, while solvent usage decreased by a factor of 4.1 when compared to the productivity and solvent usage of batch HPLC. Case (III) compared SFC purification to HPLC purification. The SFC process was more effective in terms of an increase in productivity and a reduction in solvent usage. Based on these results, it appears that SSR and SFC are very useful choices at the early stage of the drug development for a high throughput and a rapid turn around of samples.     

Optimizing the separation of gaseous enantiomers by simulated moving bed and pressure swing adsorption

The resolution of racemic gas mixtures by simulated moving bed (SMB) and pressure swing adsorption (PSA) is investigated by dynamic simulation and optimization. Enantiomer separation of inhalation anesthetics is important because there is evidence that the purified enantiomers may have different pharmacological properties than the racemate. The model parameters reported in an experimental investigation performed elsewhere are used to study the feasibility of this separation using SMB and PSA configurations. Both processes were modeled in gPROMS^® as systems of differential algebraic equations. Operating conditions are optimized such that the feed throughput and product recovery for each process were maximized subject to equal constraints on the pressures and superficial gas velocities. SMB was found to be capable of resolving racemic feed mixtures with purity and recovery exceeding 99%. On the other hand, PSA was also able to provide a single purified enantiomer with low recovery of about 30% which may limit its application to enantiomer separation. Nevertheless, PSA consumes less desorbent, and achieves higher throughput at the sacrifice of lower recovery.     

Streamlined,two-column,simulated countercurrent chromatography for binary separation

We report on a numerical and experimental study of two-column versions of streamlined, multicolumn, semi-continuous chromatography for binary separation. The systems combine a flexible node design, cyclic flow-rate modulation, and relayed operation of the inlet/outlet ports to extend the mass-transfer zone over the largest possible length, while keeping it inside the system at all times. One advantage of these streamlined designs is the simplicity of their physical realization: regardless of the number of columns, they only require two pumps to supply feed and desorbent into the system, while the flow rates of liquid withdrawn from the system are controlled by material balance using simple two-way valves. In one case, an extra pump is needed to recirculate the fluid in closed-loop. A rigorous model-based optimization approach is employed in the optimal design of the cycles to generate solutions that are physically realizable in the experimental set-ups. The optimized schemes for two-column operation supply fresh feed into the middle of the system where the composition of the circulating fluid is closest to that of the feedstock fluid, and recover the purified products, extract and raffinate, alternately at the downstream end of the unit, while desorbent is continuously supplied into the upstream end of the system. By internally recycling part of the non-pure cut fraction, the scheme with a step of closed-loop recycling significantly reduces its solvent consumption. The feasibility and effectiveness of the reported two-column processes have been verified experimentally on the linear separation of nucleosides by reversed phase subject to 99% purity constraints on both products. It is shown that our processes compare favorably against single-column batch chromatography, steady-state recycling, and four-column, open-loop SMB, for the same amount of adsorbent; they are also better than the four-column, closed-loop SMB at high feed throughputs.     

Enantioseparation of 1-phenyl-1-propanol by supercritical fluid-simulated moving bed chromatography

The enantioseparation of 1-phenyl-1-propanol through the supercritical fluid-simulated moving bed (SF-SMB) process is studied. Non-linear isotherms were measured on an analytical column, and used together with the triangle theory for SMB design to select operating conditions for the SF-SMB. Experiments were carried out on a pilot-scale SF-SMB plant at conditions that corresponded to the non-linear range of the isotherm. Under conditions of low feed concentration, complete separation (extract purity = 99.5%; raffinate purity = 98.4%) was achieved. Under conditions of larger feed concentration, the best separation corresponded to an extract purity of 98.0% and a raffinate purity of 94.0%, and yielded a productivity of 110 g of racemate per kg stationary phase per day.     

Modification of a commercial chiral stationary phase influences on enantiomer separations using simulated moving bed chromatography

Chromatographic enantiomer separations using high-performance chromatography and the simulated moving bed (SMB) principle have become a practically useful method for obtaining optical isomers. The carbamate derivatives of amylose coated onto silica particles are very effective chiral stationary phases (CSPs). Several lots of Chiralpak AS, and its successor, Chiralpak AS-V, were compared by laser diffraction, microscopic imaging and pulse injections with increasing amounts of various racemates in order to determine the loading capacity and the competitive adsorption isotherms. Software simulations allowed to assess the possible effects due to the observed variations between the CSPs on the performance of a pilot SMB unit. The obtained results were verified by two multi-kilogram separations performed under current good manufacturing principles (cGMP) guidelines employing the two CSPs. The results of the two production runs are discussed in the light of the recently introduced "triangle theory" which allows to account for the overload conditions prevailing under preparative chromatographic conditions and to predict optimal operating conditions. Under optimized conditions the enantiomer separation of 1.4 kg racemate/kg stationary phase per day with purities >99.6% for the target enantiomer have been achieved.     

Identification of nitrate ester explosives by liquid chromatography-electrospray ionization and atmospheric pressure chemical ionization mass spectrometry

A new continuous chromatographic process (VARICOL) has been presented recently. The basic principle of the new VARICOL process consists of an asynchronous shift of the inlet/outlet lines in a multi-column system on a recycle loop. This process has been used to perform the separation of the optical isomers of the SB-553261 racemate. In this paper, we illustrate that for this specific separation, the VARICOL process is more efficient than the well-known SMB process.     

模拟移动床色谱法拆分甲霜灵对映体

模拟移动床(SMB)色谱作为一种精确、高效的制备色谱技术引起研究者的极大关注。本文以EnantioPak OD填料为手性固定相,正己烷-乙醇(70 : 30, v/v)为流动相,在四区模拟移动床上手性拆分甲霜灵外消旋体。采用旋光检测器研究甲霜灵异构体在手性柱上的洗脱顺序;探讨进样浓度、进样流速、各区流速和切换时间等条件对手性分离甲霜灵外消旋体的影响,并与制备色谱进行比较。结果表明:S-(+)-甲霜灵先于R-(-)-甲霜灵被流动相洗脱,R-(-)-甲霜灵在色谱柱上的保留强于S-(+)-甲霜灵;在线性和非线性条件下,模拟移动床都能很好地拆分甲霜灵外消旋体,在优化SMB工艺条件下,S-(+)-甲霜灵和R-(-)-甲霜灵的光学纯度都大于99%;在样品质量浓度为15 mg/mL的条件下,模拟移动床色谱分离的样品量显著高于制备色谱,而流动相消耗仅为后者的1/9。这对于发展大规模色谱拆分甲霜灵工艺具有良好的指导意义。     

Optimization of steady state recycling parameters utilizing polarimetry in chiral separations

Processing gram to kilogram quantities of target analytes has led to the exploration of several high-throughput separation techniques. Among those investigated is steady state recycling (SSR). Similar to simulated moving bed (SMB) fractions are collected from the leading and trailing edges of a chromatographic profile while sample material is injected into the interior. Purifying large amounts of sample in the semi-preparative stage is ideal for these groups. SSR allows for development of methods capable of separating 50 g to kilograms and even greater amounts of product efficiently. Using polarimetry to optimize the SSR method further improves the efficiency of method development, providing comprehensive data leading to incisive development decisions. Accurate sample injection allowed continual 99% enantiomer separation after polarimetry optimization. We have developed an efficient SSR optimization methodology that offers rapid development of chiral separation by SSR.     

Simulated moving bed chromatography for the separation of enantiomers

Simulated moving bed (SMB) chromatography, a continuous multi-column chromatographic process, has become one of the preferred techniques for the separation of the enantiomers of a chiral compound. Several active pharmaceutical ingredients, including blockbuster drugs, are manufactured using the SMB technology. Compared to single column preparative chromatography, SMB separations achieve higher productivity and purity, while reducing the solvent consumption. The SMB technology has found applications both at small and large scales. Design methods have been developed for robust operation and scale-up, using data obtained from analytical experiments. In the last few years, rapid developments have been made in the areas of design, improved process schemes, optimization and robust control. This review addresses these developments, as well as both the fundamentals of the SMB science and technology and some practical issues concerning the operation of SMB units. Particular emphasis is placed on the consolidation of the “triangle theory”, a design tool that is used both in the academia and industry for the design of SMB processes.     

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.     

Stability problems of polyether ether ketone and ethylene-tetrafluoroethylene copolymer tubing in simulated moving bed operation

Polymeric capillaries made from polyether ether ketone (PEEK) or ethylene-tetrafluoroethylene copolymer (Tefzel) are considered as highly inert and chemically resistant materials used as standard equipment in HPLC and simulated moving bed (SMB) applications. During several racemate separations using a SMB unit equipped with these tubes a formation of micro-holes was observed. All separations had in common that a high content of an alkane was used in the mobile phase. The patterns of damage and possible reasons causing the leakages of the capillaries are discussed. Polymeric tubing had to be replaced by stainless steel capillaries for the enantiomer separations in order to ensure safety of workers, GMP status of products and control leakages.     

PowerFeed operation of simulated moving bed units: changing flow-rates during the switching interval

A possible way to improve the separation performance of simulated moving bed (SMB) units is to change the internal and external liquid flow-rates during the switching period. This operation mode, referred to as PowerFeed, is examined in this work through a model analysis. Similar to the Varicol process, which allows for the asynchronous movement of the ports, the PowerFeed process exhibits more degrees of freedom than the classical SMB process and therefore allows more room for optimization. Using an optimization technique based on a genetic algorithm, all three processes have been optimized for a few case studies in order to determine their relative potentials. It is found that PowerFeed and Varicol provide substantially equivalent performances, which are however significantly superior to those of the classical SMB process.     

On-line enantiomeric analysis using high-performance liquid chromatography in chiral separation by simulated moving bed

An automated on-line enantiomeric analysis system comprising an analytical HPLC set-up with two UV detectors sharing the same light source has been employed to monitor the internal composition profile in chiral simulated moving bed chromatography. This monitoring scheme does not use a polarimeter. Using a sampling interface placed between two SMB columns, effluent samples are directed onto a high-efficiency analytical column at a sampling rate faster than the overall dynamics of the preparative unit to achieve on-line enantiomeric analysis of the composition profile. The other UV detector is placed in the SMB loop before the fraction collector to provide instantaneous measurement of the total enantiomeric concentration. The feasibility and effectiveness of the on-line enantiomeric monitoring scheme were assessed experimentally on the separation of Tr?ger's base racemate, using Chiralpak AD as stationary phase and methanol as eluent. It was found that robust monitoring of the concentration profiles of the individual enantiomers is best achieved when the enantiomeric purity obtained from the peak areas of the on-line enantiomer analysis chromatograms is combined with the on-line UV measurement of total enantiomeric concentration. The accuracy and robustness of the proposed on-line enantiomeric monitoring system open up promising perspectives for process control and dynamic optimization of the SMB.     

On-line monitoring of enantiomer concentration in chiral simulated moving bed chromatography

Simulated moving bed chromatography is a key technology for the pilot and production scale separation of enantiomers of chiral chemical species. Product quality control is probably the most important issue in this kind of separation at both scales, and for this it is clear that on-line monitoring of absolute enantiomer concentrations plays a major role. In this work, an on-line system consisting of a UV detector and a polarimeter in series is used to monitor the composition of the extract and raffinate streams of a laboratory SMB unit. The model system adopted is the separation of the enantiomers of the Tr?ger's base on microcrystalline cellulose triacetate (CTA) using ethanol as mobile phase. The technique is effective and accurate, thus providing promising perspectives for SMB process control and dynamic optimization.     

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.     

Enantioseparation of a chiral epoxide by simulated moving bed chromatography using Chiralcel-OD

Summary The feasibility of using simulated moving bed (SMB) chromatography for the chiral separation of a racemic epoxide with Chiralcel-OD as the stationary phase is demonstrated on a semi-preparative scale. Operating conditions for the separation are chosen with the help of a simple chart that depicts visually the interrelationships between the system flow rates and the SMB design criteria. The 12 column (each 100 mm×16 mm ID) SMB system continuously resolved the racemic mixture at a rate of 11.5 g/24 hr into streams with 95% and 94.4% e.e. (enantiomeric excess). A comparison of the SMB process with an optimized multiple-injection conventional chromatographic separation showed similar specific production rates for both methods, but a seven-fold lower solvent consumption for the SMB.     

Gas phase SMB for propane/propylene separation using enhanced 13X zeolite beads

A gas phase simulated moving bed technology using improved 13X zeolite beads and isobutane as desorbent is assessed for the separation of propane/propylene. Adsorption equilibrium (via gravimetric method) and dynamics (via breakthrough curves) were determined in order to validate the mathematical model used to describe the adsorption process. Simulation results have shown that it is possible to separate propylene from a mixture with propane using gas phase SMB technology. The results indicate that high purity propylene (99.99 % desorbent free basis) can be recovered up to 99.96 % with a productivity of 17.6 mol kg^?1 h^?1, with propane being also recovered at high levels (99.98 %) and high purity (99.89 % desorbent free basis). Comparing the SMB simulation results obtained for this new 13X zeolite beads with those obtained with a commercial 13X zeolite characterized elsewhere, it was found that the productivity of the process was raised by 25 %, with half desorbent consumption.     

Simulated Moving-Bed Liquid Chromatography with Three Zones for Continuous Desalting of Organic Compounds

Aqueous solutions of DL-β-phenylalanine from a biotechnological process have been desalted by simulated moving bed preparative liquid-chromatography (SMB LC). During the design of a laboratory-scale continuous procedure four kinds of reversed-phase polymeric resin were compared. A suitable adsorbent was chosen and operating conditions were subsequently optimized by using equilibrium data obtained experimentally; productivity of the amino acid was used as the optimization target function. This enabled improvement of operating conditions determined in the first step of the procedure.     

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.     

Chiral separation by two-column,semi-continuous,open-loop simulated moving-bed chromatography

A two-column version of a multicolumn, semi-continuous, open-loop chromatograph for chiral separation is presented and validated experimentally. The heart of the process is a flexible node design and cyclic flow-rate modulation that succeed at keeping the mass-transfer zone inside the system without resorting to any recycling technique. One advantage of this streamlined design is the simplicity of its physical realization: regardless of the number of columns, it only requires two pumps to supply feed and desorbent into the system, while the flow rates of liquid withdrawn from the system are controlled by material balance using simple two-way valves. A rigorous model-based optimization approach is employed in the optimal cycle design to generate a solution that is physically realizable in the experimental apparatus. The optimized scheme for two-column operation supplies fresh feed into the system where the composition of the circulating fluid is closest to that of the feedstock fluid, and recovers the purified products, extract and raffinate, alternately at the downstream end of the unit while desorbent is supplied into the upstream end of the system. The feasibility and effectiveness of the two-column process are verified experimentally on the separation of reboxetine racemate, a norepinephrine re-uptake inhibitor, under overloaded conditions. Our set-up employs an automated on-line enantiomeric analysis system, comprising an analytical HPLC set-up with two UV detectors to monitor the composition profile at the downstream end of one of the columns; this monitoring system does not use a polarimeter.