A large-scale purification of paclitaxel from cell cultures of Taxus chinensis

A large-scale purification method was developed for producing paclitaxel, to guarantee high purity and yield from plant cell cultures. The complete method for mass production was a simple and efficient procedure, for the isolation and purification of paclitaxel from the biomass of Taxus chinensis, consisting of solvent extraction, synthetic adsorbent treatment, and two steps of precipitation, followed by two steps of high performance liquid chromatography (HPLC). The organic solvent extraction of biomass obtained crude extract containing paclitaxel. The use of synthetic adsorbent treatment and precipitation in the prepurification process allows for rapid and efficient separation of paclitaxel from interfering compounds and dramatically increases the yield and purity of crude paclitaxel for HPLC purification steps compared to alternative processes. This prepurification process serves to minimise solvent usage, size, and complexity of the HPLC operations for paclitaxel purification. The paclitaxel of over 99.5% purity can be simply obtained with high yield from crude paclitaxel by HPLC using reverse-phase separation on C18 as the first step and normal-phase separation on silica as the second step.     

纳豆激酶集成化分离技术

综述了纳豆激酶的分离纯化技术的研究现状和发展趋势。通过对常规分离技术的分析,重点讨论了集成化分离技术的应用及其优势,包括集成化双水相分配技术、扩张床吸附技术以及耐盐性混合模式吸附技术等分离方法。并指出集成化分离技术在生产纳豆激酶以及其他活性蛋白方面,具有广阔的应用前景。     

Very large scale monoclonal antibody purification: the case for conventional unit operations

Technology development initiatives targeted for monoclonal antibody purification may be motivated by manufacturing limitations and are often aimed at solving current and future process bottlenecks. A subject under debate in many biotechnology companies is whether conventional unit operations such as chromatography will eventually become limiting for the production of recombinant protein therapeutics. An evaluation of the potential limitations of process chromatography and filtration using today's commercially available resins and membranes was conducted for a conceptual process scaled to produce 10 tons of monoclonal antibody per year from a single manufacturing plant, a scale representing one of the world's largest single-plant capacities for cGMP protein production. The process employs a simple, efficient purification train using only two chromatographic and two ultrafiltration steps, modeled after a platform antibody purification train that has generated 10 kg batches in clinical production. Based on analyses of cost of goods and the production capacity of this very large scale purification process, it is unlikely that non-conventional downstream unit operations would be needed to replace conventional chromatographic and filtration separation steps, at least for recombinant antibodies.     

Magnetic particles for the separation and purification of nucleic acids

Nucleic acid separation is an increasingly important tool for molecular biology. Before modern technologies could be used, nucleic acid separation had been a time- and work-consuming process based on several extraction and centrifugation steps, often limited by small yields and low purities of the separation products, and not suited for automation and up-scaling. During the last few years, specifically functionalised magnetic particles were developed. Together with an appropriate buffer system, they allow for the quick and efficient purification directly after their extraction from crude cell extracts. Centrifugation steps were avoided. In addition, the new approach provided for an easy automation of the entire process and the isolation of nucleic acids from larger sample volumes. This review describes traditional methods and methods based on magnetic particles for nucleic acid purification. The synthesis of a variety of magnetic particles is presented in more detail. Various suppliers of magnetic particles for nucleic acid separation as well as suppliers offering particle-based kits for a variety of different sample materials are listed. Furthermore, commercially available manual magnetic separators and automated systems for magnetic particle handling and liquid handling are mentioned.     

Separation used for purification of recombinant proteins

The purification of molecules from recombinant cells may be strongly influenced by the molecular biology of gene isolation and expression. At the beginning of the process there may be a demand for information on the minute amounts of proteins and thus for ever increasingly sensitive techniques. Purification of recombinant proteins can differ from conventional purifications in several ways, depending on the solubility of the protein, occurrence in inclusion bodies, creation of fusion proteins with tags that enable simpler purification. Sometimes a (re)naturation step is required to get a bioactive protein. On the other hand, the techniques used in separation are essentially the same as for purification from the natural source and environment.     

Designing new monoclonal antibody purification processes using mixed-mode chromatography sorbents

Current platforms for purification of monoclonal antibodies, mostly relying on Protein A as a first capture step, are robust and efficient but significantly increase downstream purification costs, mainly due to Protein A resins. To decrease manufacturing costs, industry is increasingly considering the use of purification schemes without affinity Protein A resins. Mixed-mode chromatography can be used as a powerful alternative to standard purification platforms as it offers new selectivity and separation mechanisms exploiting a combination of both ionic and hydrophobic characteristics of antibodies and contaminating proteins. By using a design of experiments (DoE) approach and high throughput screening in 96-well plates, we developed four different two-steps MAb purification processes, based on the use of mixed-mode sorbents. Finally, three of the tested processes resulted in final purified Mab fractions containing less than 100 ppm of residual CHO proteins (CHOP), with overall process yields above 70%. These data show that mixed-mode chromatography sorbents, used at capture or intermediate purification steps, really expand the options of MAb purification process development with or without Protein A affinity chromatography.     

抗生素分离纯化技术研究进展

抗生素分离纯化是抗生素产业中的技术难点和关键环节,对抗生素常用的分离纯化技术及其研究进展进行了概述,以期为抗生素分离领域提供理论指导。最后对新型分离纯化技术进行了总结和展望。     

从桑白皮中提取药物成分桑根酮D

开发了从中药桑白皮中提取和精制桑根酮D的工艺路线.用紫外光谱、红外光谱、质谱以及核磁共振谱(13C NMR、1H NMR与重水交换)进行结构鉴定,证实其为桑根酮D(sanggenon D).     

A continuous multicolumn countercurrent solvent gradient purification (MCSGP) process

Biomolecules are often purified via solvent gradient batch chromatography. Typically suitable smooth linear solvent gradients are applied to obtain the separation between the desired component and hundreds of impurities. The desired product is usually intermediate between weakly and strongly adsorbing impurities, and therefore a central cut is required to get the desired pure product. The stationary phases used for preparative and industrial separations have a low efficiency due to strong axial dispersion and strong mass transfer resistances. Therefore a satisfactory purification often cannot be achieved in a single chromatographic step. For large scale productions and for very valuable molecules, countercurrent operation such as the well known SMB process, is needed in order to increase separation efficiency, yield and productivity. In this work a novel multicolumn solvent gradient purification process (MCSGP-process) is introduced, which combines two chromatographic separation techniques, which are solvent gradient batch and continuous countercurrent SMB. The process consists of several chromatographic columns, which are switched in position opposite to the flow direction. Most of the columns are equipped with a gradient pump to adjust the modifier concentration at the column inlet. Some columns are interconnected, so that non pure product streams are internally, countercurrently recycled. Other columns are short circuited and operate in batch mode. As a working example the purification of an industrial stream containing 46% of the hormone Calcitonin is considered. It is found that for the required purity the MCSGP unit achieves a yield close to 100% compared to a maximum value of a single column batch chromatography of 66%.     

Separation of alpha-lactalbumin and beta-lactoglobulin using membrane ultrafiltration

There is considerable commercial interest in the preparation of individual whey proteins as high-value food additives, nutraceuticals, and therapeutics. This study examined the use of membrane filtration for the separation of alpha-lactalbumin and beta-lactoglobulin. Stirred cell filtration experiments were performed using both cellulosic and polyethersulfone membranes to determine the optimal pH, ionic strength, and filtration conditions. Selectivities of greater than 55 could be achieved at pH 5.5 and 50 mM ionic strength using a 30-kD cellulose membrane. A diafiltration process was then designed for the protein separation. A 16-diavolume filtration yielded beta-lactoglobulin as the retentate product with a purification factor of 100 and recovery of 90%. The alpha-lactalbumin was recovered in the filtrate with a purification factor of more than 10 and nearly 99% yield. Model calculations were in good agreement with the experimental data.     

Development of a novel disposable filter bag for separation of biomolecules with functionalized magnetic particles

The integration of disposable magnetic filters in combination with functionalized magnetic particles represents a fast and cost‐effective alternative for enzyme purification in comparison to solid/liquid separation by means of centrifugation followed by chromatographic purification. The main advantage of the particle‐based process is the solid/solid/liquid separation in one step combined with disposable equipment. Furthermore this combination provides the possibility to also process biocatalytic reactions in cell‐containing media into disposable equipment with preimmobilized enzymes onto the magnetic particles. The focus of the presented study is on the design and performance of a disposable filtration unit consisting of a plastic bag with an inlet and outlet and a stainless steel filter matrix. During magnetic separation, the magnetic particles selectively retard at the filter matrix due to the magnetic force, which counteracts the drag force. It was found that the length of a lengthwise aligned filter matrix should be longer than the magnetic pole surfaces in fluid flow direction. Hereby, a filtration capacity of 5.6 g magnetic particles was measured with a loss of below 0.5%. Introducing a two‐phase flow optimizes the cleaning of the bag after a magnetic filtration. The procedure offered a high cleaning efficiency. Herewith, the cleaned filter unit could be discarded with minimum losses of product and magnet particles.     

Isolation and culture of rat microvascular endothelial cells

The purpose of this study is to identify the separation techniques that result in pure cultures of rat microvascular endothelial cells (MECs). A multistep process is used to optimize the separation of the cells from rat epididymal fat pads, obtaining as pure a culture as possible within a relatively short processing time. The process initially employs the digestion, filtration, and density gradient separation steps. We further describe the use of an attachment phase that allows the differential adherence of contaminating cell types. Immunomagnetic purification is the final step in the process and is performed using anti-PECAM-1 (CD31) monoclonal antibody-labeled DynaBeads.     

Recovery of lysozyme from hen egg white by selective magnetic cake filtration

A new concept for the improvement of the downstream processing and purification is the so‐called magnetic separation. By using surface functionalized magnetic substrate particles, which selectively adsorb the target product, it can be directly separated out of a crude bioprocess stream. These methods are already used for analytical purposes, where only small amounts of functionalized particles are necessary. To apply the same concept at a larger scale, effective and economical procedures have to be provided. First, suitable process equipment has to be developed. Second, the magnetic particles have to be manufactured with a stable surface functionalization and long‐term stability for their reuse. Up to now mainly high‐gradient magnetic separation filter devices are applied for selective magnetic separation. They consist of a magnetic matrix in which the magnetic particles are trapped. In this work, a new magnetic filter is introduced that overcomes the capacity limitations of the current high‐gradient magnetic separation technology. The principle is demonstrated by selective recovery of lysozyme from hen egg white. Prior to the separation experiments magnetic beads with a strong acid cation‐exchange surface functionalization are synthesized. The separation procedure is implemented in only one unit operation. With the implementation of the displacement elution sequence lysozyme can be separated out of a hen egg white solution with a purification factor of PF=36 and a purity P=0.83.     

Dye-affinity techniques for bioprocessing: Recent developments

Textile or triazine dyes play an important role as affinity ligands in protein purification. Each step of the protein purification protocol can be divided into three stages, partitioning between two phases, separation of these phases and recovery of the target protein from the enriched phase. Now developments in dye-affinity techniques are discussed emphasizing the innovations in all three stages of the protein purification process. Dye-affinity chromatography has become a routine step in protein purification. New dyes have been developed and used successfully in both traditional chromatographic mode and new modes like affinity precipitation, polymer aqueous two-phase partitioning or expanded bed chromatography. The specificity of dye techniques has been increased by both purposeful designing of new dyes and decreasing non-specific protein–dye interactions with polymer shielding. One can envisage further development and ramification of dye-affinity techniuqes in protein purification.     

Evaluation of solid phase extraction for downstream separation of propane-1,3-diol and butan-1-ol from fermentation broth

Today, glycerol is mainly a by-product of fat splitting and biodiesel production. This study examined the use of chemically modified silica gels for downstream separation of propane-1,3-diol and butan-1-ol from fermentation broths obtained through the glycerol fermentation process. The developed method was found to be simple and efficient for the isolation and purification of butan-1-ol from the other components in the fermentation mixture. However, in the case of the separation of propane-1,3-diol from fermentation broth, the silica gel sorbents were ineffective.     

Recovery of endo-polygalacturonase using polyethylene glycol-salt aqueous two-phase extraction with polymer recycling

The partitioning behaviour of endo-polygalacturonase (endo-PG) and total protein from a clarified Kluyveromyces marxianus fermentation broth in polyethylene glycol (PEG)-ammonium sulfate and PEG-potassium phosphate (pH=7) aqueous two-phase systems was experimentally investigated. Both the enzyme and total protein partitioned in the bottom phase for these two kinds of systems. The enzyme partitioning coefficient can be lower than 0.01 in PEG8000-(NH₄)₂SO₄ ATPS with a large phase volume ratio and a moderate tie-line length, which implies the possibility of concentration operation using aqueous two phase partitioning. An ion-exchange separation of high purification efficiency was applied to analyze the clarified and dialyzed fermentation broth. A total purification factor of only 2.3 was obtained, which indicated the high enzyme protein content in the total protein of the fermentation broth. Consequently, the main purpose for separating endo-PG is concentration rather than purification. A separation scheme using an aqueous two-phase extraction process with polymer recycling and a dialysis was proposed to recover endo-PG from the fermentation supernatant of K. marxianus for commercial purpose. A high enzyme recovery up to 95% and a concentration factor of 5 to 8 with a purification factor of about 1.25 were obtained using the single aqueous two-phase extraction process. More than 95% polymer recycled will not affect the enzyme recovery and purification factor. Dialysis was used mainly to remove salts in the bottom phase. The dialysis step has no enzyme loss and can further remove small bulk proteins. The total purification factor for the scheme is about 1.7.     

Extraction of protease from Aspergillus tamarii URM 4634 in aqueous two-phase system under continuous and discontinuous process

Abstract

Aqueous two-phase systems have been studied for almost a century to separate biomolecules in harmless conditions. Proteases produced by Aspergillus tamarii URM 4634 were extracted in polyethylene glycol (PEG)/phosphate aqueous two-phase system under discontinuous and continuous (perforated rotative discs column) process. On the discontinuous process, it was evaluated the effect of operational conditions (PEG molar mass and its concentration, phosphate concentration and pH) over the partition coefficient, activity yield and purification factor. Protease partitioned to PEG-phase with partition coefficients up to 55.73. The best process parameters were 17.5% of PEG, with molar mass 8000?g·mol^?1, 15% of phosphate salt at pH 6, with 113.15% of activity yield and purification factor of 2.62. Under continuous extraction, hold up data showed that 57.1% of the discontinuous phase was available for protein extraction. Further, separation achieved 90.0% of efficiency. The yields surpassed 100% in almost all runs, and the best purification factor was 1.84, with both flows of 2?mL·min^?1. Thus, the best operational conditions reached an activity yield of 95.3% and 90.0% of separation efficiency. Hence, aqueous two-phase system PEG/phosphate extraction is an efficient process for separation of proteases produced by Aspergillus tamarii URM 4634, under continuous extraction likewise under discontinuous process.     

Isolation and purification of protease from human placenta by foam fractionation

The effect of operating parameters like pH, protein concentration, column geometry, and gas flow rate on the separation efficiency of proteolytic enzymes from crude human placental homogenate has been studied in a batch foam column. Purification has been found to be optimum at pH 8.0, close to the isoelectric pH, at which the surface adsorption of the protein on the foam bubbles is maximum. Both purification and recovery varied significantly with total protein concentration. Stable bubble formation was hindered at lower protein concentrations, while extraneous proteins rather than the protease were preferentially adsorbed at higher protein concentrations, decreasing the purification efficiency. Column diameter and column height should be optimized for any specific feed protein concentration and gas flow rate. However, the enrichment ratio was found to decrease with the increase in flow rate. The results indicate that foam fractionation is an effective separation process for recovering valuable biochemicals from biological materials.     

Application of semi-industrial monolithic columns for downstream processing of clotting factor IX

It has been shown in a previous study that monolithic columns can be used for downstream processing of different concentrates of clotting factor IX [K. Branovi? et al., J. Chromatogr. A 903 (2000) 21]. This paper demonstrates that such supports are useful tools also at an early stage of the purification process of factor IX from human plasma. Starting with the eluate after solid-phase extraction with DEAE-Sephadex, the use of monolithic columns has allowed much better purification than that achieved with conventional anion-exchange supports. The period of time required for separation is also much reduced. In up-scaling experiments, separations are carried out with 8, 80 and 500 ml columns. A volume of 1830 ml of DEAE-Sephadex eluate, containing a total of 27.6 g of protein and 48500 IU of factor IX is applied to the 500 ml monolithic column. This corresponds to a separation on a pilot scale. The results of this separation after up-scaling are comparable to those obtained with the 8 ml column on a laboratory scale.     

Magnetic techniques for the isolation and purification of proteins and peptides

Isolation and separation of specific molecules is used in almost all areas of biosciences and biotechnology. Diverse procedures can be used to achieve this goal. Recently, increased attention has been paid to the development and application of magnetic separation techniques, which employ small magnetic particles. The purpose of this review paper is to summarize various methodologies, strategies and materials which can be used for the isolation and purification of target proteins and peptides with the help of magnetic field. An extensive list of realised purification procedures documents the efficiency of magnetic separation techniques.