Optimisation and scale-up of microwave assisted cyanation

A microwave enhanced palladium catalysed cyanation procedure was optimised for the final step of a production method for citalopram 2. The method was demonstrated on multigram batch scale for the synthesis of escitalopram (S)-2 and then in a stop-flow continuous process for citalopram.     

Industrial scale-up of countercurrent chromatography: predictive scale-up

This study describes how scale-up in countercurrent chromatography (CCC) can be simply predicted on a process scale CCC device by running a preliminary analytical-sized sample and having knowledge of the stationary-phase retention at scale-up conditions. Results have shown that simple experimentation can lead within a day to a process with the capability of several kilograms per day (tons per year) compound yield, and that this is feasible with benchtop CCC units.     

Performance and scale-up of adsorptive membrane chromatography

Separation efficiency and scalability of Pall Corporation's new Mustang stacked membrane chromatographic devices were investigated, using both the 10-ml and l(-1) models and comparing the responses of tracer pulses obtained for conventional and reverse-flow operation. Tracers included AMP, lysozyme, and thyroglobulin, which vary in relative molecular mass from less than 1000 up to 650000. Both devices showed marked insensitivity to tracer size and flow-rate and gave sharper peaks than would have been expected from conventional 15-microm bead packings. However, reverse-flow peaks were always significantly sharper than those for conventional operation, and the differences were ascribed primarily to non-uniform header residence times. Numerical simulations of the macroscopic flow confirmed that this was indeed the case. This problem was much less pronounced for the l(-1) device so scale-up is conservative.     

Polymeric supports for affinity chromatography and high-performance affinity chromatography

Affinity chromatography is the most selective chromatographic method for the purification of biologically active materials. It is based on the biospecific interaction of the substrates with a ligand, which is chemically immobilized onto a suitable matrix (support). Different matrices provided by natural and synthetic polymers are used for the preparation of affinity supports. In this communication we describe and compare the properties of various supports based on polysaccharides, polyacrylamides and inorganic materials. In particular, we discuss the utility of different silica derivatives (especially primary hydroxyl silica) for the immobilization of ligands and high-performance affinity chromatography.     

High-performance affinity chromatography

High-performance affinity chromatography is a new technique for the fast and efficient purification of biologically active molecules. It combines the biospecificity of affinity chromatography with the high speed and resolution obtained in high-performance liquid chromatography. In particular, the immobilization of ligands to different silica derivatives and their suitability for high-performance affinity chromatography are discussed.     

Recent progress on the industrial scale-up of counter-current chromatography

The pharmaceutical industries are looking for rapid methods of purification and predictable scale-up for their drug development process that will cut their costs and enable them to reduce the time to market. In this paper, recent progress is reviewed in the development and demonstration of two types of industrial scale centrifugal liquid-liquid chromatography: hydrostatic and hydrodynamic. Industrial scale hydrostatic processes by Partus Technologies and Armen Instrument are just emerging. Results demonstrating scalability are presented for hydrodynamic processes by Dynamic Extractions. The review concludes that the time is now right, with this appropriate commercial support, for high performance counter-current chromatography to emerge as a major enabling technology for industry.     

Mechanistic modeling of cation exchange chromatography scale-up considering packing inhomogeneities

In process development and characterization, the scale-up of chromatographic steps is a crucial part and brings a number of challenges. Usually, scale-down models are used to represent the process step, and constant column properties are assumed. The scaling is then typically based on the concept of linear scale-up. In this work, a mechanistic model describing an anti-Langmuirian to Langmuirian elution behavior of a polypeptide, calibrated with a pre-packed 1 ml column, is applied to demonstrate the scalability to larger column volumes up to 28.2 ml. Using individual column parameters for each column size, scaling to similar eluting salt concentrations, peak heights, and shapes is experimentally demonstrated by considering the model's relationship between the normalized gradient slope and the eluting salt concentration. Further scale-up simulations show improved model predictions when radial inhomogeneities in packing quality are considered.     

High-performance affinity chromatography of DNA

The octadecamer of thymidylic acid, (dT)18, was synthesized with a primary amino group on the 5'-terminal phosphate and this was covalently coupled to 300 A pore macroporous silica. Coupling was performed inside a prepacked column to an activated N-hydroxysuccinimidyl ester silica. The (dT)18-silica column successfully separates mixtures of adenine oligomers differing in length by one nucleotide. The dependence upon salt concentration, temperature and length for elution of oligonucleotides was determined. Methods were also developed to selectively elute such columns using either salt or temperature gradients.     

Trypsin and affinity chromatography.

Affinity adsorbents for trypsin which were prepared by immobilizing product-type ligands, that is, peptides having C-terminal arginine, proved to be effective not only for preparative purposes but also for basic research on molecular recognition. The properties of the binding site of trypsin were revealed by chromatographic experiments. Quantitative analysis based on the theory of frontal affinity chromatography proved to be extremely effective. As an extension of the product-type ligands, peptide argininals were also used and information on the mechanism of action of these inhibitors was obtained. Anhydrotrypsin, which lost the hydroxyl group of Ser183, was found to gain increased binding ability for product-type compounds. This inactivated enzyme was also used as an immobilized ligand and the unique affinity adsorbent thus prepared proved to be extremely effective for the separation of peptides and recombinant proteins based on their C-terminal structures. High-performance affinity chromatography of trypsin and related enzymes using a polymer-based support was also developed.     

Rapid linear scale-up of a protein separation by centrifugal partition chromatography

The scaling up of the separation of two proteins with an aqueous two-phase system (ATPS) from 176 mg with a 500 ml laboratory scale centrifugal partition chromatography (CPC) column to 2.2g with a 6.25 litre pilot-scale column is presented. A model sample system of a mixture of lysozyme and myoglobin was chosen for this study using an ATPS system comprising 12.5% (w/w) PEG-1000:12.5% (w/w) K2HPO4. It was found that the maximum sample concentration possible without precipitation was 2.2mg/ml for each constituent. The optimisation of rotor speed, mobile phase flow rate and sample loading was performed on a laboratory-scale device. It was found that a centrifuge speed of 2000 rpm (224 'g'), 10 ml/min mobile phase flow rate with a 43 ml (10% of active column volume) sample volume gave optimum operating conditions. This was linearly scaled up to pilot scale by increasing mobile phase flow rate, fraction size and sample loading in the ratio of the system capacities (i.e. 12.5:1). Flow rate was therefore increased from 10 ml/min to 125 ml/min, fraction size from 10 ml to 125 ml and sample loading from 43 ml to 500 ml. Rotor speed however was reduced from 2000 rpm on the laboratory device to 1293 rpm on the pilot-scale device to maintain the same 224 'g' field in each chamber, as the pilot-scale CPC unit has a larger rotor radius than the laboratory one. Resolution increased from Rs=1.28 on the 500 ml rotor to Rs=1.88 on the 6.25 litre rotor, giving potential throughputs in batch mode of over 40 g/day.     

一种凝血酶亲和色谱介质的制备方法

对凝血酶-琼脂糖亲和色谱介质的制备方法进行了研究。首先使用凝血酶和溴化氰活化的琼脂糖制备凝血酶-琼脂糖亲和色谱介质,然后用生色底物法考察亲和色谱介质上凝血酶的活性,以凝血酶活性为指标对最佳偶联条件进行了优化。结果表明最佳条件为使用pH 8.3的Na₂CO₃-NaHCO₃溶液(含0.5 mol/L NaCl)为缓冲溶液,凝血酶用量为每1 g色谱介质加入凝血酶200 U,室温反应10 h。在最佳条件下所制备的色谱介质有较好的稳定性,在4℃条件下存放40天,亲和介质上的凝血酶活性仍有70.6%保留。该亲和色谱介质可广泛用于含凝血酶抑制剂的天然药物筛选和分离纯化。     

Mathematical analysis of affinity membrane chromatography

A mathematical model including convection, diffusion and Freundlich adsorption is developed. To examine the validity of the model, the affinity membranes were prepared by coating chitosan on the nylon membranes, a ligand of poly-L-lysine was bound to the chitoan-coating membranes, and the adsorption behavior of bilirubin through the stacked affinity membranes was investigated. The agreements between the theoretical and experimental results are exceptional. Using our new model, we show that: (1) As Pe increases, the breakthrough curves become sharper. For Pe greater than 30, the effect of axial diffusion is insignificant; (2) As m increases, the time of total saturation is delayed and the loading capacity at the point of breakthrough is increased; (3) As n decreases, the time of total saturation is delayed and the loading capacity at the point of breakthrough is increased; (4) As r increases, both the time of total saturation and the loading capacity at the point of breakthrough are increased; (5) adsorption rate influences the time of total saturation strongly but contributes little to the loading capacity.     

Separation of phosphomolybdate by affinity chromatography

A new method of separating phosphomolybdate from phosphoric esters and anhydrides using a small column of polyvinylpolypyrrolidone is introduced. When a mixture of phosphate compounds and ammonium molybdate (1–3%, pH 3-5) is poured onto such a column, inorganic orthophosphate (Pi)^p1 is selectively adsorbed onto the column material as phosphomolybdate, while other phosphate compounds, which do not react with molybdate, are drained through the column. Using radioisotopes, retention and recovery percentages were measured. At pH 3, 99.99% of Pi^p32 was retained in the column, while 97 ± 1% of ATP^p32 was recovered in the effluent. Retained Pi^p32 was eluted out later with 0.5 M ammonium hydroxide with a recovery percentage of 98 ± 1%. Unlike other methods of separating phosphomolybdate, the separation was little affected by the presence of reducing agents. The use of disposable columns, which can be prepared easily, packed ahead of time, and stored for later use, makes the radioisotopes assay convenient and contamination-free.     

Membrane-based receptor affinity chromatography.

Membrane-based receptor affinity chromatography (MRAC), which utilizes the molecular recognition between an immobilized receptor and its soluble protein ligand, has been developed for the purification of human interleukin-2 and related biomolecules. The multi-purpose affinity membrane used in this study consisted of a soluble form of interleukin-2 receptor (IL-2R) chemically bonded to hollow-fiber membranes in an oriented fashion. A model system involving anti-Tac-H (a humanized monoclonal antibody to IL-2R) was used to study the important factors influencing the performance of MRAC, including support morphology, mass transfer rate and adsorption kinetics. All three are shown to be highly efficient. MRAC has been successfully applied to the purification of anti-Tac-H, recombinant human interleukin-2 (rIL-2) and interleukin 2-Pseudomonas exotoxin fusion protein (IL2-PE40). Overall, MRAC was found to be a viable, scalable and extremely productive affinity purification method.     

Optimisation and robustness analysis of a hydrophobic interaction chromatography step

Process development, optimisation and robustness analysis for chromatography separations are often entirely based on experimental work and generic knowledge. The present study proposes a method of gaining process knowledge and assisting in the robustness analysis and optimisation of a hydrophobic interaction chromatography step using a model-based approach. Factorial experimental design is common practice in industry today for robustness analysis. The method presented in this study can be used to find the critical parameter variations and serve as a basis for reducing the experimental work. In addition, the calibrated model obtained with this approach is used to find the optimal operating conditions for the chromatography column. The methodology consists of three consecutive steps. Firstly, screening experiments are performed using a factorial design. Secondly, a kinetic-dispersive model is calibrated using gradient elution and column load experiments. Finally, the model is used to find optimal operating conditions and a robustness analysis is conducted at the optimal point. The process studied in this work is the separation of polyclonal IgG from BSA using hydrophobic interaction chromatography.     

核酸适配体亲和色谱的研究进展

核酸适配体亲和色谱是将核酸适配体作为色谱固定相上的亲和配体的一种新型色谱技术。核酸适配体是一种可以特异性地识别目标物的寡聚核苷酸,与免疫抗体相比,核酸适配体在筛选制备、稳定性及应用等方面都显示出独特的优点。本文介绍了核酸适配体亲和色谱在小分子、蛋白质和细胞的分离和分析中的应用,对核酸适配体亲和色谱的研究现状和发展前景进行了综述。     

Purfication of synthetic cardiotoxin by affinity chromatography

A polypeptide containing 60 amino acids with 4 disulphide bonds, synthesized by the solid-phase method, was highly purifed by anticardiotoxin-Sepharose affinity chromatography following gel filtration and CM-cellulose chromatography. The identification of the final product as cardiotoxin was confirmed by thin-layer chromatography on silica gel, polyacrylamide gel electrophoresis, amino acid analysis, circular dichroism spectra, N-terminal analysis and four biological tests.     

Determination of binding constants by affinity chromatography

This review summarizes developments in the use of affinity chromatography to characterize biospecific interactions in terms of reaction stoichiometry and equilibrium constant. In that regard, the biospecificity incorporated into the design of the experiment ensures applicability of the method regardless of the sizes of the reacting solutes. By the adoption of different experimental strategies (column chromatography, simple partition equilibrium, solid-phase immunoassay and biosensor technology protocols) quantitatiative affinity chromatography can be used to characterize interactions governed by an extremely broad range of binding affinities. In addition, the link between ligand-binding studies and quantitative affinity chromatography is illustrated by means of partition equilibrium studies of glycolytic enzyme interactions with muscle myofibrils, an exercise which emphasizes that the same theoretical expressions apply to naturally occurring examples of affinity chromatography in the cellular environment.