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.     

Improvement of fractional precipitation process for pre-purification of paclitaxel

Fractional precipitation is a simple, efficient method for pre-purifying paclitaxel extracted from plant cell cultures. However, the fractional precipitation process has been inherently problematic due to the lengthy precipitation time (～3 days) that is required. An improved fractional precipitation process could significantly reduce the precipitation time by increasing the purity of crude extract and the surface area available for precipitation. Glass beads (7 mm) were used to increase the surface area, and the optimal surface area per working volume (i.e. volume of reaction solution) (S/V) for achieving the highest purity and yield of paclitaxel possible was found to be 0.428 mm^?1. The content of paclitaxel dissolved in methanol that can be processed during fractional precipitation was evaluated, and it was established that up to 0.9% (w/v) pure paclitaxel content could be processed. This improved pre-purification process serves to minimize solvent usage and the size and complexity of the high performance liquid chromatography operation required for paclitaxel purification.     

Fractional precipitation for paclitaxel pre-purification from plant cell cultures of Taxus chinensis

Fractional precipitation is a simple and efficient procedure for pre-purification of paclitaxel. The optimal methanol composition in water, paclitaxel content in crude extract, storage temperature, and time were 61.5% (v/v), 0.5% (w/v), 0°C, and 3 days, respectively. As purity of the paclitaxel in the crude extract increases, the purity and yield of paclitaxel from fractional precipitation increases. This pre-purification process serves to minimize the solvent usage, size and complexity of the HPLC operations for paclitaxel purification. This process is readily scalable to a pilot plant and eventually to a production environment where multikilogram quantities of material are expected to be produced.     

Optimization of micellar extraction for the pre-purification of paclitaxel from<Emphasis Type="Italic">Taxus chinensis</Emphasis>

Currently, there are many reports in the literature regarding technological methods for paclitaxel purification. However, there have been few reports on the purification of paclitaxel using a micellar system. This method is based on the transfer of paclitaxel within the crude extract to an aqueous surfactant solution as a micelle, allowing the use of organic solvents to be used for the removal of lipids and non-polar impurities. In this study, we optimized the important process parameters of micellar extraction to obtain a high purity and yield of paclitaxel in a pre-purification step. The optimal surfactant (N-cetylpyridinium chloride, CPC) concentration, initial crude paclitaxel concentration, organic solvents (methylt-butyl ether/hexane) ratio, extraction temperature, and extraction time were 7.5% (w/v), 16.4 mg/mL, 1.5/1 (v/v), 25°C, and 30 min, respectively. The crude extracts from the liquid-liquid extracts were efficiently pre-purified by micellar extraction, increasing in purity from 6% to over 21%, with a yield of 92%. Overall, the use of micellar extraction in the pre-purification process allowed for rapid and efficient separation of paclitaxel from interfering compounds, and dramatically increased the yield and purity of the crucle paclitael for subsequent purification steps.     

Development of a micelle-fractional precipitation hybrid process for the pre-purification of paclitaxel from plant cell cultures

A micelle-fractional precipitation hybrid process was developed for the effective pre-purification of the anticancer agent paclitaxel extracted from plant cell cultures. First, it was found that the efficiency of such a developed process could be remarkably enhanced by removing waxy substances originating from plant cells using the adsorbent sylopute. Paclitaxel yield was improved and the fractional precipitation time was shortened by increasing the surface area per working volume (S/V) of the reacting solution through the addition of a cation exchange resin (Amberlite IR120 or Amberlite 200), an anion exchange resin (Amberlite IRA400 or Amberlite IRA96), or glass beads. Most of the paclitaxel (>98%) could be obtained after about 12 h of fractional precipitation using Amberlite 200. Purity increased with increasing fractional precipitation time up to 9 h to about 85%, after which it showed little change. On the other hand, no paclitaxel precipitate was formed using either of the nonionic exchange resins because paclitaxel, which is hydrophobic, was strongly adsorbed on the hydrophobic resin surface. Since high-purity paclitaxel can be obtained in high yield and the precipitation time can be reduced by combining micelle formation with fractional precipitation, this hybrid method is expected to significantly enhance the final purification process.     

Evaluation of the effect of crude extract purity and pure paclitaxel content on the increased surface area fractional precipitation process for the purification of paclitaxel

This study evaluated the effect of crude extract purity and pure paclitaxel content on the behavior in terms of purity, yield, fractional precipitation time, and precipitate shape and size of fractional precipitation in the increased surface area fractional precipitation process for the purification of paclitaxel. With increased pure paclitaxel content and crude extract purity, the purity and yield of paclitaxel were improved and the fractional precipitation time was reduced. Regardless of changes in crude extract purity and pure paclitaxel content, it was possible to obtain a small paclitaxel precipitate size by hindering the growth of precipitate particles using an ion exchange resin to increase the surface area. In addition, according to the type of surface-area increasing substance used, precipitate size and shape differed because of a differing affinity for the paclitaxel particles. The lower the crude extract purity and pure paclitaxel content, the higher the yield and the improvement in purity in the process of increased surface area fractional precipitation, with a greater effect on the decrease in paclitaxel particle size.     

Evaluation of a high surface area fractional precipitation process for the purification of paclitaxel from Taxus chinensis

In this study, we evaluated a high surface area fractional precipitation process to achieve the effective purification of paclitaxel, an anticancer agent, from plant cell cultures. Fractional precipitation experiments were performed by increasing the surface area per working volume (S/V) to 0.428/mm using a variety of ion exchange resins. When the cation exchange resin Amberlite IR 120 H was used, the highest purity (>85%) and yield (>80%) of paclitaxel could be obtained in the shortest fractional precipitation time (within 6 h). Use of an ion exchange resin resulted in the production of smaller paclitaxel precipitates since it inhibited the growth of particles. When Amberlite IR 120 H in particular was used, paclitaxel particles were 2 ?? 3 times smaller (less than 30 ??m radius) than those obtained in the absence of ion exchange resin. Paclitaxel particle size was inversely correlated with the zeta potential of the fractional precipitation solution after the addition of ion exchange resin.     

Improved fractional precipitation method for purification of paclitaxel

This study investigated changing the methanol/water ratio during fractional precipitation of paclitaxel, and adding all the distilled water at room temperature, followed mixing for an additional 10 min. When the methanol/water ratio was 50:50, 40:60, and 30:70 (v/v), the paclitaxel yield was 42.0%, 84.3%, and 92.0%, respectively. When using a methanol/water ratio of 50:50 (v/v), a similar high purity and yield of paclitaxel to the case of storing at a low temperature was achieved when adding all the distilled water at room temperature, followed by additional mixing for 10 min and further mixing at room temperature during fractional precipitation. Thus, additional mixing after adding all the distilled water is confirmed as important during fractional precipitation. Furthermore, the present results show that a high yield of high-purity paclitaxel is possible with additional mixing at room temperature after adding all the distilled water, which is significantly more economical than the existing method of storing at a low temperature for a long time after adding all the distilled water during fractional precipitation.     

Evaluation of feeding and mixing conditions for fractional precipitation of paclitaxel from plant cell cultures

Fractional precipitation based on the difference in solubility of crude paclitaxel dissolved in methanol, to which distilled water must be added, is the most effective method for the pre-purification of paclitaxel. In this study, the effect of the distilled water feeding and mixing method on the efficiency of fractional precipitation and the formation of paclitaxel precipitate were evaluated. When the distilled water was added all at once, the highest purity (∼57.0%) and yield (∼81.0%) were obtained, and a spherical precipitate was formed by the clustering of crystal branches. On the other hand, when the distilled water was added intermittently in several aliquots, the purity and yield tended to decrease with increasing number of additions, and the precipitate took the form of a cross or pentagon with less clustering of branches. Not mixing after the addition of distilled water resulted in high purity (∼57.0%) and the formation of a spherical precipitate that showed increased branching around the nucleus over time. In contrast, when the sample was mixed intermittently after adding distilled water, paclitaxel was obtained in high yield (∼99.7%). Continuously mixing the sample after adding distilled water, however, caused the precipitate crystals to be broken into smaller pieces.     

中试规模纯化海洋芽孢杆菌源脂肽类化合物

本次研究旨在建立经济可行的海洋芽孢杆菌源脂肽类化合物的中试规模纯化工艺。对包括酸化沉淀、甲醇浸提、溶剂沉淀、盐析、萃取、硅胶柱层析和HZ806大孔树脂吸附工艺在内的可放大的成熟单元工艺进行反复试验,考察脂肽类化合物表面活性对单元工艺的影响。严格遵循以高收率为前提循序渐进逐步减少杂质的原则,组合上述单元工艺对目标产物进行提取和纯化,并最终获得高纯度脂肽样品。新工艺可从1 t海洋芽孢杆菌Bacillus marinus B-9987的发酵液中,以百克量级的规模制备87.51%–100%纯度的脂肽类化合物样品,收率81.73%。本研究首次实现了高纯度的海洋芽孢杆菌源脂肽类化合物的百克量级制备;允许发酵生产阶段使用天然培养基,缓解了脂肽中游发酵生产和下游大规模纯化之间的矛盾;且各单元工艺规避了脂肽类化合物水溶液的乳化起泡和不经济的大体积水溶液蒸发浓缩。新工艺实用可行,经济合理。     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

Development and optimization of fractional precipitation for the pre-purification of (+)-dihydromyricetin

A novel fractional precipitation process, both simple and efficient, was developed for producing (+)-dihydromyricetin in high purity and high yield from crude extracts. The optimal acetone composition in water, initial (+)-dihydromyricetin concentration in crude extract, storage temperature, storage time, and pH were 1/5 (v/v), 0.1 g/mL, 4°C, 32 h, and 9.0, respectively. Crude extracts were efficiently pre-purified using fractional precipitation of (+)-dihydromyricetin by differences of solubility in an acetone solution, increasing purity from 55.0 to over 84.9% with an overall yield of 97.5%. The use of fractional precipitation for pre-purification allowed for rapid and efficient separation of (+)-dihydromyricetin from interfering compounds and dramatically increased the purity of crude (+)-dihydromyricetin for subsequent purification steps.     

精制破伤风类毒素产毒及精制工艺的改进

用超滤、硫酸铵二段盐析法取代等电点沉淀法后,精制破伤风类毒素（精破类）的纯度由８０７Ｌｆ／ｍｇＰＮ提高到１８８３Ｌｆ／ｍｇＰＮ,纯度提高一倍以上。使用双胨培养基取代酪素培养基后,产毒水平由４７Ｌｆ／ｍｌ提高到８８Ｌｆ／ｍｌ（ｔ＝６．４６,ｐ＜０．００１）;用新法精制后,精破类纯度分别为１９４９Ｌｆ／ｍｇＰＮ及１７８５Ｌｆ／ｍｇＰＮ（ｔ＝０．３３４,ｐ＞０．０５）,引用双胨培养基后可提高产毒水平,但不影响精破类的纯度。     

The extractive purification of peroxidase from plant raw materials in aqueous two-phase systems

The extractive purification of peroxidase from Armoracia rusticana roots and Glycine max seed coats in temperature-induced and affinity microsphere-containing aqueous two-phase systems was stuied. The extractive purification of peroxidase from Glycine max seed coats was carried out in a temperature-induced aqueous two-phase system formed by Triton X-45, Triton X-100 and sodium acetate at pH 5.5 A 99% yield with a 6-fold purification factor was obtained. When the clear top phase was subjected to concanavalin-A affinity chromatography, the purification factor rose to 41 and the yield dropped to 28%. A two-step purification process for peroxidase from Armoracia rusticana roots was developed by adding concanavalin-A affinity microspheres to a PEG/phosphate aqueous two-phase system. The method allows a 60% recovery of high purity peroxidase (1,860 guaiacol units per mg). A lower recovery rate and degree of purification of this enzyme was achieved after temperature-induced aqueous two-phase partition or acetone precipitation and concanavalin-A affinity column chromatography.     

Selective precipitation and purification of monovalent proteins using oligovalent ligands and ammonium sulfate

This paper describes a method for the selective precipitation and purification of a monovalent protein (carbonic anhydrase is used as a demonstration) from cellular lysate using ammonium sulfate and oligovalent ligands. The oligovalent ligands induce the formation of protein-ligand aggregates, and at an appropriate concentration of dissolved ammonium sulfate, these complexes precipitate. The purification involves three steps: (i) the removal of high-molecular-weight impurities through the addition of ammonium sulfate to the crude cell lysate; (ii) the introduction of an oligovalent ligand and the selective precipitation of the target protein-ligand aggregates from solution; and (iii) the removal of the oligovalent ligand from the precipitate by dialysis to release the target protein. The increase of mass and volume of the proteins upon aggregate formation reduces their solubility, and results in the selective precipitation of these aggregates. We recovered human carbonic anhydrase, from crude cellular lysate, in 82% yield and 95% purity with a trivalent benzene sulfonamide ligand. This method provides a chromatography-free strategy of purifying monovalent proteins--for which appropriate oligovalent ligands can be synthesized--and combines the selectivity of affinity-based purification with the convenience of salt-induced precipitation.     

Development of aqueous two‐phase systems comprising poly ethylene glycol and dextran for purification of pullulan: Phase diagrams and fiscal analysis

Pullulan is a commercially important Exopolysaccharide (EPS) with wide‐spread applications which is produced by Aureobasidium pullulans. The alternative α (1 4) & α (1 6) configuration in pullulan provides it the specific structural and conformational properties. Pullulan is currently being exploited in food, health care, pharmacy, lithography, cosmetics. The fermented broth is processed by organic solvent precipitation for isolation and purification of pullulan. In this study, we have tried to analyze the potential of aqueous two phase system as an alternate technique to extract pullulan from fermented broth. Including this viability of ATPS was also compared with conventional organic solvent precipitation system in terms of cost and time. It was found that ATPS process produced a higher yield of pullulan (80.56%) than organic solvent precipitation method (71.6%). ATPS was also found more economical and less time consuming method.     

High‐throughput process development of purification alternatives for the protein avidin

With an increased number of applications in the field of the avidin‐biotin technology, the resulting demand for highly‐purified protein avidin has drawn our attention to the purification process of avidin that naturally occurs in chicken egg white. The high‐throughput process development (HTPD) methodology was exploited, in order to evaluate purification process alternatives to commonly used ion‐exchange chromatography. In a high‐throughput format, process parameters for aqueous two‐phase extraction, selective precipitation with salts and polyethylene glycol, and hydrophobic interaction and mixed‐mode column chromatography experiments were performed. The HTPD strategy was complemented by a high‐throughput tandem high‐performance liquid chromatography assay for protein quantification. Suitable conditions for the separation of avidin from the major impurities ovalbumin, ovomucoid, ovotransferrin, and lysozyme were identified in the screening experiments. By combination of polyethylene glycol precipitation with subsequent resolubilization and separation in a polyethylene glycol/sulfate/sodium chloride two‐phase system an avidin purity of 77% was obtained with a yield >90% while at the same time achieving a significant reduction of the process volume. The two‐phase extraction and precipitation results were largely confirmed in larger scale with scale‐up factors of 230 and 133, respectively. Seamless processing of the avidin enriched bottom phase was found feasible by using mixed‐mode chromatography. By gradient elution a final avidin purity of at least 97% and yield >90% was obtained in the elution pool. The presented identification of a new and beneficial alternative for the purification of the high value protein thus represents a successful implementation of HTPD for an industrially relevant purification task. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:957–973, 2015     

Purification of trypsin by affinity precipitation and combining with aqueous two-phase extraction

Summary Soybean trypsin inhibitor was bound to a pH-sensitive reversibly soluble-insoluble polymer (AS-L) for affinity precipitation of trypsin. Trypsin was purified from a crude extract 5.4-fold and with 61% yield, however, the reusability of the ligand was poor. This can be overcome by combining aqueous two-phase extraction with affinity precipitation, which improved trypsin yield and purity factor after repeated ligand usage.     

Efficient recovery of recombinant human erythropoietin from milk of transgenic pigs by two-step pretreatment

The selective removal of impurity proteins and colloidal particles from milk prior to chromatographic purification processes presents a crucial issue in the production of therapeutic proteins from transgenic animals with high recovery yield and purity. We have developed an efficient two-step precipitation method for the recovery of the recombinant human erythropoietin (rhEPO) of interest from transgenic sow milk. Here, rhEPO was partially purified from transgenic sow milk via a two-step precipitation method consisting of ammonium sulfate and divalent metal precipitations, with a yield of approximately 82.1% and a purification fold of 10.4 at a copper concentration of 30 mM. Copper proved to be the strongest flocculating agent among the divalent ions tested for the aggregation of milk proteins under 35%, with ammonium sulfate, zinc, nickel, and calcium demonstrating increasing flocculating capability in the given order. Copper and zinc proved to be appropriate divalent metals for the recovery of rhEPO at high yield and purity, and the optimal concentration ranges of copper and zinc were 20~40 and 40~80 mM, respectively.     

Ammonium chloride: a novel effective and inexpensive salt solution for phycocyanin extraction from <Emphasis Type="BoldItalic">Arthrospira</Emphasis> (<Emphasis Type="BoldItalic">Spirulina</Emphasis>) <Emphasis Type="BoldItalic">platensis</Emphasis>

Phycocyanin, a blue pigment, is a type of phycobiliproteins. Because of its various potential properties, phycocyanin is applied to various fields, such as nutraceutical, pharmaceutical, medicine, cosmetics, and biotechnological research. The cost and application of phycocyanin are highly dependent on its purity index. In this study, ammonium chloride is presented as a novel, effective, and inexpensive salt for phycocyanin extraction. Compared with sodium phosphate, which is commonly used during phycocyanin extraction process, ammonium chloride solution efficiently extracted phycocyanin with high purity from Arthrospira platensis FACHB-314. In addition, ammonium phosphate solution is also presented as an alternative precipitation agent in phycocyanin purification that may replace the widely used ammonium sulfate. Statistical analysis shows that there is no significant difference in phycocyanin concentration between crude extracts (overall mean of 0.208 and 0.215 for extraction using sodium phosphate and ammonium chloride, respectively). However, the difference in phycocyanin purity ratio (A₆₂₀/A₂₈₀) between these two extractions is significant (overall mean of 0.742 and 1.428 for extraction using sodium phosphate and ammonium chloride, respectively). With ammonium chloride, the purity indexes of phycocyanin are 1.5 and 2.81 after the optimum extraction step, and precipitation used as the primary purification step, respectively. The present study describes a novel purification method to achieve phycocyanin with analytical grade without multiple purification steps.