Separation of Nadolol Stereoisomers Using Chiralpak IA Chiral Stationary Phase

Chiralpak IA adsorbent is used for both analytical and preparative chromatographic separation of nadolol stereoisomers. The results include a complete screening of the mobile phase composition for both the baseline resolution of all four nadolol stereoisomers (analytical separation) and the simulated moving bed (SMB) pseudo‐binary separation of the most retained stereoisomer. The experimental results show that analytical baseline resolution of nadolol stereoisomers can be achieved using alcohol/hydrocarbon and alcohol/acetonitrile solvent mixtures. The 10%ethanol/90%acetonitrile mixture is presented as the one that presents baseline resolution with lower retention. For the preparative pseudo‐binary separation, pure ethanol, pure methanol, alcohol/acetonitrile, and alcohol/tetrahydrofuran mixtures proved to allow good separation results. The 100%methanol/0.1%diethylamine solvent composition was selected to perform the experimental SMB separation. Using a 10 g/L total feed concentration, the more retained stereoisomer was recovered at the extract outlet stream with 99.5% purity, obtaining a system productivity of 1.98 gL^?1 h^?1 and requiring a solvent consumption of 3.13 L/g of product. Comparing these results with the ones recently presented by Ribeiro et al. (2013), this work shows that the Chiralpak IA chiral adsorbent is an interesting alternative to Chiralpak AD for the separation of nadolol stereoisomers at both analytical and preparative scales. Chirality 28:399–408, 2016. © 2016 Wiley Periodicals, Inc.     

Separation of Nadolol Stereoisomers by Chiral Liquid Chromatography at Analytical and Preparative Scales

The separation of the four nadolol stereoisomers on Chiralpak® AD by chiral liquid chromatography was carried out at both analytical and preparative scales. A screening of possible mobile‐phase compositions was performed using different alcohol–hydrocarbon mixtures. The results obtained confirm the use of 20:80:0.3 ethanol‐hexane‐diethylamine reported by McCarthy (1994) but introduce other possibilities for the complete resolution of the four nadolol stereoisomers at analytical scale, namely, the mixtures 30–40:70–60:0.3 ethanol‐heptane‐diethylamine. Additionally, this work describes how retention and resolution depend on the ethanol content in hexane and heptane mixtures. The separation of nadolol stereoisomers is also carried out at preparative scale and different alcohol–hydrocarbon compositions are proposed, depending on the target component to be obtained. Particularly, this work presents the experimental separation of the more retained nadolol stereoisomer (RSR‐nadolol) by simulated moving bed (SMB) chromatography using an 80:20:0.3 ethanol‐heptane‐diethylamine mobile phase. For a 2 g/l feed concentration, RSR‐nadolol is 100% recovered at the extract outlet stream, 100% pure, and with a system productivity of 0.65 g_{RSR‐nadolol}/(l_bed^.h) and a solvent consumption of 9.6 l_solvent/g_{RSR‐nadolol}. Chirality 25:197–205, 2013. © 2013 Wiley Periodicals, Inc.     

Ultra‐performance convergence chromatography with tandem mass spectrometry‐assisted method for rapid enantioseparation and determination of fluazifop‐butyl in tobacco and soil

A quick, green, and sensitive method for chiral separation and determination of fluazifop‐butyl enantiomers in tobacco and soil was established by ultra‐performance convergence chromatography with tandem mass spectrometry (UPC²‐MS/MS). The baseline separation was obtained on an ACQUITY UPC² Trefoil CEL2 column in 4 minutes with CO₂ and methanol as mobile phase. Column temperature, auto back pressure regulator pressure (ABPR), and modifier solvent were optimized to obtain the best separation efficiency. Under the optimal conditions, the recoveries of both enantiomers were 82.8% to 99.5% with relative standard deviations (RSDs) less than 5.5% at three different concentration levels in two matrices. Good coefficients of determination (R² ≥ 0.9976) were achieved over the concentration range of 10 to 500 ng/mL. The limits of detection (LODs) for all enantiomers in the two matrices varied from 1.6 to 2.1 μg/kg, and the limits of quantification (LOQs) did not exceed 7.0 μg/kg. The proposed method was then successfully applied to analyze authentic samples, confirming that it was a green, convenient, and reliable strategy for the analysis of fluazifop‐butyl enantiomers in tobacco and soil.     

Improving the performance of nadolol stereoisomers' preparative separation using Chiralpak IA by SMB chromatography

The pseudobinary preparative separation of nadolol stereoisomers is performed by simulated moving bed chromatography (SMB). Using the Chiralpak IA adsorbent, a new 25:75:0.1 (v/v/v) methanol‐acetonitrile‐diethylamine solvent composition was selected to perform the experimental SMB separation and compare it with the previous results obtained using pure methanol. Using a 2 g L^?1 total feed concentration of an equimolar mixture of the four stereoisomers of nadolol, the more retained component was fully recovered (100% purity and 100% recovery), with a system productivity of 0.77 g L^?1 hour^?1 and a solvent consumption of 9.62 L g^?1. Comparing these results with the ones previously reported using 100:0.1 methanol‐diethylamine solvent composition, this work shows that the 25:75:0.1 methanol‐acetonitrile‐diethylamine is a better alternative for the preparative separation of nadolol stereoisomers by SMB chromatography. These results are confirmed by simulation of the SMB operation for higher feed concentrations, by comparing the performances of the two solvent compositions using the data obtained experimentally through the measurement of the adsorption equilibrium isotherms and the kinetic data obtained for both solvents. The new experimental and simulation results stress out that the performance of the preparative separation can be improved by a careful selection of the solvent composition.     

Comparison of two matrices for selective recovery of C595 diabody fragment (dbFv) from Escherichia coli lysates

A comparative study of the performance of two types of adsorbent (Streamline Quartz Base and Upfront Matrices), derivatized with the same affinity ligand (RPAP) to recover C595 diabody fragment (dbFv) from Escherichia coli lysates has been undertaken. Both streamline and Upfront Matrices are characterized by a particle size range of 100–300 μm. Streamline has a density of 1.20 g cm⁻³ and ligand concentration of 0.85 μmol ml⁻¹. Upfront has a density of 1.35 g cm⁻³ and ligand concentration of 0.83 μmol ml⁻¹. The release of C595 dbFv from E. coli cells was achieved by a chemical lysis method. The recovery performance of both adsorbents was evaluated in terms of operational productivity and elution yield of C595 dbFv in packed bed (clarified feedstock) and expanded bed (unclarified and clarified feedstock) chromatography systems. Streamline and Upfront adsorbents exhibited diabody operational productivities of 131 and 202 mg l⁻¹, respectively, with an elution yield of 92 and 94%, respectively, in packed bed operation. Streamline and Upfront adsorbents exhibited diabody operational productivities of 54.5 and 123.7 mg l⁻¹, respectively, with an elution yield of 89 and 92%, respectively, in expanded bed operation.     

Preparative separation of the saponin lancemaside a from Codonopsis lanceolata by centrifugal partition chromatography

Introduction. Lancemaside A is a saponin that inhibits decreases in blood testosterone level and thus prevents or ameliorates symptoms associated with male climacteric disorder. Our initial attempt to preparative isolation of lancemaside A from the saponin fraction of Codonopsis lanceolata roots by a preparative HPLC did not give a clear result. Objective. To develop a simple and efficient method for the preparative isolation of lancemaside A from the hot water extract of C. lanceolata roots using centrifugal partition chromatography (CPC). Methodology. The saponin fraction obtained from the hot water extract of C. lanceolata roots was used as the sample for preparative‐scale separation of lancemasides by CPC using n‐hexane:n‐butanol:methanol:0.1% aqueous formic acid (3:4:1:6, v/v) as the two‐phase solvent system. The upper phase (organic phase) of the two‐phase solvent system was used as the mobile phase, and 0.5 g of saponin fraction was applied for separation by CPC. Each fraction that was separated by CPC was analysed by HPLC, and the fractions containing each of the separated compounds were pooled together, and then were purified by simple preparative HPLC. Results. The demonstrated separation sequence, hot water extraction, DIAION HP‐20 column chromatography, CPC and preparative HPLC, yielded lancemaside A, foetidissimoside A and astersaponin Hb in their pure forms. Conclusion. The simple and efficient method for the preparative isolation of lancemaside A along with two other saponins, foetidissimoside A and astersaponin Hb, from the saponin fraction of C. lanceolata was established using CPC.     

Continuous production of α-peptide using immobilized recombinant yeast cells: A model for continuous production of foreign peptide by recombinant yeast

α-Peptide, a portion of Escherichia coli β-galactosidase, was cloned downstream of the yeast α-factor promoter and the signal peptide by one of the authors. In this study, we utilized recombinant yeast cells, transformed the α-peptide secretion vector and attempted continuous production of α-peptide as a model of foreign peptide production. The continuous production of α-peptide was performed by using immobilized recombinant yeast cells on a column reactor, after characterizing the secretion, using minimal and complex medium. Utilizing minimal medium, with a productivity of 100 000 U h⁻¹ l⁻¹, α-peptide was continuously produced for more than 200 h. We then attempted to improve the productivity of α-peptide by alternating minimal and complex medium. Utilizing this medium changing method, 1.4 times higher α-peptide was produced during 150 h of operation compared with that achieved only by feeding minimal medium.     

Use of a new pirkle-type chiral stationary phase in analytical and preparative subcritical fluid chromatography of pharmaceutical compounds

Good results have been obtained with use of the new bonded chiral stationary phase Whelk-O 1 in analytical and preparative subcritical fluid chromatography. A wide variety of enantiomeric pairs of compounds with different functional groups that are of pharmaceutical and biological interest have been resolved. This Pirkle-concept CSP appears to be more rugged than cellulosic phases (e.g., Chiralcel) with regards to solvents and pressure. In comparing the usefulness of the column for SFC versus HPLC chiral analysis, we have observed a clear superiority of SFC in terms of higher speed and efficiency of analysis, and faster method development. This is consistent with our experience with Chiralcel CSPs. With the Whelk-O 1 we have shown that the effects of temperature and modifier on SFC separations are similar to what has been reported for most other CSPs. We also observed a unique selectivity advantage of SFC for verapamil. We had good success with using a 1-in. diameter column packed with Whelk-O 1 to perform preparative SFC separations of a number of enantiomeric mixtures. The advantages of preparative SFC over preparative HPLC will be discussed. The feasibility of preparative SFC is dependent on how well we meet the practical challenges such as sample introduction issues, special hardware requirements due to the high pressure, and fraction collection issues. © 1994 Wiley-Liss, Inc.     

Ethanol production by whole cell immobilization using lignocellulosic materials as solid matrix

Amongst four carriers used, rice-straw was found to be superior in terms of ethanol production. The maximum productivity (17.84 gl⁻¹ h⁻¹) corresponded to a dilution rate of 0.39 h⁻¹, the ethanol concentration being 45.80 gl⁻¹. A multistage rhomboidal bioreactor was found to partially overcome the disruption effect caused by the generation of a large volume of carbon dioxide in the column. Increases in productivity of about 12.55% and 3.6%, respectively, were achieved using rhomboidal and tapered bioreactors as compared to the cylindrical bioreactor. It was observed that the generation time of cells, in both the immobilized and free states, was around 2.5 h. The ethanol yield (Y_p/s) in the lower part of the reactor was less in comparison with other zones, where the substrate utilization efficiency was relatively higher.     

Chiral separation of flurbiprofen enantiomers by preparative and simulated moving bed chromatography

This study presents the chiral resolution of flurbiprofen enantiomers by preparative liquid chromatography using the simulated moving bed (SMB) technology. Flurbiprofen enantiomers are widely used as nonsteroidal anti‐inflammatory drugs, and although demonstrate different therapeutic actions, they are still marketed as a racemic mixture. The results presented here clearly show the importance of the selection of the proper solvent composition for the preparative separation of flurbiprofen enantiomers. Chiral SMB separation is carried out using a laboratory‐scale unit (the FlexSMB‐LSRE®) with six columns, packed with the Chiralpak AD® stationary phase (20 μm). Results presented include the experimental measurement of equilibrium and kinetic data for two very different solvent compositions, a traditional high hydrocarbon content [10%ethanol/90%n‐hexane/0.01% trifluoroacetic acid (TFA)] and a strong polar organic composition (100%ethanol/0.01%TFA). Experimental data, obtained using the two mobile phase compositions, are used to predict and optimize the SMB operation. After selecting 10%ethanol/90%n‐hexane/0.01%TFA as the most appropriate solvent composition, three feed concentrations of racemic flurbiprofen were considered. Using 40 g/l of racemic flurbiprofen feed solution, the purities for both outlet streams were above 99.4%, the productivity was 13.1 g_feed/(L_bed h), and a solvent consumption of 0.41 L_solvent/g_feed was achieved. Chirality, 2011. © 2011 Wiley‐Liss, Inc.     

Preparative and analytical separation of the zopiclone enantiomers and determination of their affinity to the benzodiazepine receptor binding site

We report the preparative separation of rac-zopiclone using malic acid as the resolving agent. Furthermore, two different methods for the analytical determination of zopiclone enantiomers by HPLC on chiral stationary phases are described. The benzodiazepine receptor binding of the isolated enantiomers was investigated. Half-maximal inhibitory concentrations of (+)- and (?)-zopiclone were 21 or 1,130 nmol/liter, respectively, indicating a more than 50 times higher affinity of the (+)-enantiomer toward the receptor. © 1993 Wiley-Liss, Inc.     

Preparative chromatographic separation: Simulated moving bed and modified chromatography methods

Chromatography has been the method of choice for the separation of complex biological mixtures for analytical purposes, particularly for the last fifty years. Its use has recently been extended to preparative separation where the productivity relative to the amount of resin and solvent used is a matter of concern. To overcome the inherent thermodynamic inefficiency of batch chromatography, as exemplified by the partial temporal usage of the resin and dilution of the product with the solvent, chromatography has been continually modified by separation engineers. Column switching and recycling represent some of the process modifications that have brought high productivity to chromatography. Recently, the simulated moving bed (SMB) method, which claims a high separation efficiency based on counter-current moving bed chromatography, has become the mainstay of preparative separation, especially in chiral separation. Accordingly, this paper reviews the current status of SMB, along with several chromatographic modification, which may be helpful in routine laboratory and industrial chromatographic practices.     

Chiral Separation of G‐type Chemical Warfare Nerve Agents via Analytical Supercritical Fluid Chromatography

Chemical warfare nerve agents (CWNAs) are extremely toxic organophosphorus compounds that contain a chiral phosphorus center. Undirected synthesis of G‐type CWNAs produces stereoisomers of tabun, sarin, soman, and cyclosarin (GA, GB, GD, and GF, respectively). Analytical‐scale methods were developed using a supercritical fluid chromatography (SFC) system in tandem with a mass spectrometer for the separation, quantitation, and isolation of individual stereoisomers of GA, GB, GD, and GF. Screening various chiral stationary phases (CSPs) for the capacity to provide full baseline separation of the CWNAs revealed that a Regis WhelkO1 (SS) column was capable of separating the enantiomers of GA, GB, and GF, with elution of the P(+) enantiomer preceding elution of the corresponding P(–) enantiomer; two WhelkO1 (SS) columns had to be connected in series to achieve complete baseline resolution. The four diastereomers of GD were also resolved using two tandem WhelkO1 (SS) columns, with complete baseline separation of the two P(+) epimers. A single WhelkO1 (RR) column with inverse stereochemistry resulted in baseline separation of the GD P(–) epimers. The analytical methods described can be scaled to allow isolation of individual stereoisomers to assist in screening and development of countermeasures to organophosphorus nerve agents. Chirality 26:817–824, 2014. © 2014 The Authors. Chirality published by John Wiley Periodicals, Inc.     

High gradient magnetic separation versus expanded bed adsorption: a first principle comparison

A robust new adsorptive separation technique specifically designed for direct product capture from crude bioprocess feedstreams is introduced and compared with the current bench mark technique, expanded bed adsorption. The method employs product adsorption onto sub-micron sized non-porous superparamagnetic supports followed by rapid separation of the loaded adsorbents from the feedstock using high gradient magnetic separation technology. For the recovery of Savinase® from a cell-free Bacillus clausii fermentation liquor using bacitracin-linked adsorbents, the integrated magnetic separation system exhibited substantially enhanced productivity over expanded bed adsorption when operated at processing velocities greater than 48 m h^–1. Use of the bacitracin-linked magnetic supports for a single cycle of batch adsorption and subsequent capture by high gradient magnetic separation at a processing rate of 12 m h^–1 resulted in a 2.2-fold higher productivity relative to expanded bed adsorption, while an increase in adsorbent collection rate to 72 m h^–1 raised the productivity to 10.7 times that of expanded bed adsorption. When the number of batch adsorption cycles was then increased to three, significant drops in both magnetic adsorbent consumption (3.6 fold) and filter volume required (1.3 fold) could be achieved at the expense of a reduction in productivity from 10.7 to 4.4 times that of expanded bed adsorption.     

Preparative Isolation and Purification of Hydroxyanthraquinones from Rheum tanguticum Maxim. on Normal Phase Silica Gel: Using a Flash Master Personal System

Abstract

A flash chromatography method for preparative separation and purification of five hydroxyanthraquinones from the Chinese medicinal herb Rheum tanguticum Maxim. ex Balf. was developed by using Flash Master Personal⁺ systems. The purities of the products, chrysophanol, physcion, emodin, aloe‐emodin, and rhein were all over 90%, determined by high performance liquid chromatography (HPLC). Their structures were ascertained by EI‐MS, ¹H‐ and ¹³C‐NMR data, and by co‐TLC and HPLC with the authentic samples available in our laboratory.     

Immobilized horse liver alcohol dehydrogenase as an on‐line high‐performance liquid chromatographic enzyme reactor for stereoselective synthesis

Horse liver alcohol dehydrogenase (HLADH) has been non‐covalently immobilized on an immobilized artificial membrane (IAM) high‐performance liquid chromatography (HPLC) stationary phase. The resulting IAM‐HLADH retained the reductive activity of native HLADH as well as the enzyme's enantioselectivity and enantiospecificity. HLADH was also immobilized in an IAM HPLC stationary phase prepacked in a 13 × 4.1 mm ID column to create an immobilized enzyme reactor (HLADH‐IMER). The reactor was connected through a switching valve to a column containing a chiral stationary phase (CSP) based upon p‐methylphenylcarbamate derivatized cellulose (Chiralcel OJR‐CSP). The results from the combined HLADH‐IMER/CSP and chromatographic system demonstrate that the enzyme retained its activity and stereoselectivity after immobilization in the column and that the substrate and products from the enzymatic reduction could be transferred to a second column for analytical or preparative separation. The combined HLADH‐IMER/CSP system is a prototype for the preparative on‐line use of cofactor‐dependent enzymes in large‐scale chiral syntheses. Chirality 11:39–45, 1999. © 1999 Wiley‐Liss, Inc.     

Rifamycin B production by Nocardia mediterranei immobilized in a dual hollow fibre bioreactor

Continuous production of rifamycin B was studied using Nocardia mediterranei (ATCC 21789) immobilized in a dual hollow fibre bioreactor designed for cultivating aerobic cells. In the reactor operation the volumetric productivity based on the volume occupied by the immobilized cells was 108 mg l⁻¹ h⁻¹ when air was used for aeration and was 143 mg l⁻¹ h⁻¹ with pure oxygen. These corresponded to 22 and 30-fold increases over the productivity of the comparable batch system. These high productivities were due to the high cell mass density of 550 g l⁻¹. However, the specific productivity of the cell was 30–40% of that in the shake flask culture. As the residence time of medium in the reactor increased, pH of effluent rose to an alkaline region that was outside its optimum condition (pH 6.5–7.0) and the yield and productivity decreased.     

Enabling chiral separations in discovery chemistry with open‐access chiral supercritical fluid chromatography

Work from this paper details a novel walk‐up open‐access (OA) approach to enable chiral analytical method development and preparative separation of enantiomers in early discovery chemistry using supercritical fluid chromatography (SFC). We have demonstrated the success of this OA approach using immobilized chiral stationary phases (CSPs). After screening a diverse set of racemic drug candidates, we have concluded that a simplified OA chiral SFC platform can successfully purify approximately 60% of the analysed racemates. This streamlined OA workflow enables medicinal chemists with limited expertise in chiral method development to successfully and rapidly purify enantiomers for their projects using Waters UPC² and Prep100‐SFC instrumentation.     

Design of experiment assisted concurrent enantioseparation of bupropion and hydroxybupropion by high‐performance thin‐layer chromatography

A simple and efficient high‐performance thin‐layer chromatographic method was developed for chiral separation of rac ‐bupropion (BUP) and its active metabolite rac ‐hydroxybupropion (HBUP). Design of experiment (DoE)‐based optimization was adopted instead of a conventional trial‐and‐error approach. The Box–Behnken design surface response model was used and the operating variables were optimized based on 17 trials design. The optimized method involved impregnation of chiral reagent, L(+)‐tartaric acid, in the stationary phase with simultaneous addition in the mobile phase, which consisted of acetonitrile : methanol : dichloromethane : 0.50% L‐tartaric acid (6.75:1.0:1.0:0.25, v /v /v /v ). Under the optimized conditions, the resolution factor between the enantiomers of BUP and HBUP was 6.30 and 9.26, respectively. The limit of detection and limit of quantitation for (R)‐BUP, (S)‐BUP, (R,R)‐HBUP, and (S,S)‐HBUP were 9.23 and 30.78 ng spot⁻¹, 10.32 and 34.40 ng spot⁻¹, 12.19 and 40.65 ng spot⁻¹, and 14.26 and 47.53 ng spot⁻¹, respectively. The interaction of L‐tartaric acid with analytes and their retention behavior was thermodynamically investigated using van't Hoff's plots. The developed method was validated as per the International Conference on Harmonization guidelines. Finally, the method was successfully applied to resolve and quantify the enantiomeric content from marketed tablets as well as spiked plasma samples.     

Primary Production and Effects of Enrichment with Nitrate and Phosphate on Phytoplankton in the Barra Bonita Reservoir (State of São Paulo,Brazil)

Primary productivity of the phytoplankton was evaluated by the ¹⁴C and dissolved oxygen methods in December 1981 at the Barra Bonita Reservoir (São Paulo State, Brazil). The primary production varied between 0.17 to 14.51 mg C m⁻³h⁻¹ at 4 and 0 m depth, respectively. About 57 to 94% of the photosynthetic activity was due to phytoplankton > 50 μm. The highest value of assimilation rate (3.36 mg C mg Chl⁻¹h⁻¹) was found in the surface water. Dissolved nutrient concentrations were very high and consisted mainly of nitrate. Light penetration was low, the aphotic zone accounting for about 90% of the water column. Enrichment with nitrate and phosphate showed that both N and P stimulated the production of biomass (chlorophyll a), mainly due to the addition of phosphate. The enrichment experiment also indicated that phosphate addition has a significant stimulatory effect on the growth of Melosira sp. The limiting effect of light penetration on photosynthetic activity is more severe than that of nutrients.