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.     

Integrated enzyme purification and immobilization processes with immobilized metal affinity adsorbents

Silica-based immobilized metal affinity chromatography adsorbents with various ligand densities were prepared for the purification and immobilization of poly(His)-tagged d-hydantoinase (DHTase). An adsorbent with a ligand density of 13.0 μmol Cu²⁺/g gel exhibiting the optimal selectivity and a capacity of 1.4 mg/g gel toward the poly(His)-tagged enzyme was identified. The adsorbent was used for the one-step purification of His-tagged enzymes from crude cell lysate with a purity above 90%. The silica-based affinity adsorbents are particularly well suited for industrial scale operations due to their robustness. A packed-bed bioreactor with the DHTase-loaded adsorbents was used for the continuous conversion of d,l-p-hydroxyphenylhydantoin (d,l-HPH) to N-carbamoyl-d-hydroxyphenylglycine, an intermediate for the production of d-hydroxylphenylglycine. Under optimal conditions, 60 °C and pH 8.0, a conversion of 60% was obtained at a residence time of 30 min. Upon extended operation, the catalytic activity of the biocatalysts declined significantly due to enzyme leakage and enzyme denaturation. The extent of enzyme leakage can be attenuated by crosslinking with glutaraldehyde. In this study, we successfully demonstrate that a packed-bed bioreactor containing silica-based IMAC adsorbents can be used for the direct purification and immobilization of poly(His)-tagged enzymes for biotransformation.     

Ethyl isovalerate synthesis using Candida rugosa lipase immobilized on silica nanoparticles prepared in nonionic reverse micelles

Uniform and monodispersed silica nanoparticles were synthesized with a mean diameter of 100 ± 20 nm as analyzed by Transmission Electron Microscopy (TEM). Glutaraldehyde was used as a coupling agent for efficient binding of the lipase onto the silica nanoparticles. For the hydrolysis of pNPP at pH 7.2, the activation energy within 25–40 °C for free and immobilized lipase was 7.8 and 1.25 KJ/mol, respectively. The V_max and K_m of immobilized lipase at 25 °C for pNPP hydrolysis were found to be 212 μmol/min/mg and 0.3 mM, whereas those for free lipase were 26.17 μmol/min and 1.427 mM, respectively. The lower activation energy of immobilized lipase in comparison to free lipase suggests a change in conformation of the enzyme leading to a requirement for lower energy on the surface of the nanoparticles. A better yield (7 fold higher) of ethyl isovalerate was observed using lipase immobilized onto silica nanoparticles in comparison to free lipase.     

Immobilization of glucose oxidase enzyme (GOD) in large pore ordered mesoporous cage-like FDU-1 silica

Large pore ordered mesoporous silica FDU-1 with three-dimensional (3D) face-centered cubic, Fm3m arrangement of mesopores, was synthesized under strong acid media using B-50-6600 poly(ethylene oxide)–poly(butylene oxide)–poly(ethylene oxide) triblock copolymer (EO₃₉BO₄₇EO₃₉), tetraethyl orthosilicate (TEOS) and trimethyl-benzene (TMB). Large pore FDU-1 silica was obtained by using the following gel composition 1TEOS:0.00735B50-6600:0.00735TMB:6HCl:155H₂O. The pristine material exhibited a BET specific surface area of 684 m² g⁻¹, total pore volume of 0.89 cm³ g⁻¹, external surface area of 49 m² g⁻¹ and microporous volume of 0.09 cm³ g⁻¹. The enzyme activity was determined by the Flow Injection Analysis-Chemiluminescence (FIA-CL) method. For GOD immobilized on the FDU-1 silica, GOD supernatant and GOD solution, the FIA-CL results were 9.0, 18.6 and 34.0 U, respectively. The value obtained for the activity of the GOD solution with FIA-CL method is in agreement with the 35 U, obtained by spectrophotometry.     

Glucose oxidase enzyme immobilized porous silica for improved performance of a glucose biosensor

High activity of glucose oxidase (GOD) enzyme (immobilized in porous silica particles) is desirable for a better glucose biosensor. In this work, effect of pore diameter of two porous hosts on enzyme immobilization, activity and glucose sensing was compared. The hosts were amine functionalized: (i) microporous silica (NH₂-MS) and (ii) mesoporous silica (NH₂-SBA-15). Based on whether the dimension of GOD is either larger or smaller than the pore diameter, GOD was immobilized on either external or internal surface of NH₂-MS and NH₂-SBA-15, with loadings of 512.5 and 634 mg/g, respectively. However, GOD in NH₂-SBA-15 gave a higher normalized absolute activity (NAA), which led to an amperometric sensor with a larger linear range of 0.4–13.0 mM glucose. In comparison, GOD in NH₂-MS had a lower NAA and a smaller linear range of 0.4–3.1 mM. In fact, the present GOD-NH₂-SBA-15 electrode based sensor was better than other MS and SBA-15 based electrodes reported in literature. Thus, achieving only a high GOD loading (as in NH₂-MS) does not necessarily give a good sensor performance. Instead, a host with a relatively larger pore than enzyme, together with optimized electrode composition ensures the sensor to be functional in both hyper- and hypoglycemic range.     

Immobilization of glucose oxidase onto cobalt based on silica core/shell nanoparticles as carrier

Co–B/SiO₂/NH₂ magnetic nanoparticles (NPs) were prepared from a silica shell-coated Co–B core using the Stöber method and amine-modification on the surface. Glucose oxidase (GOD) was covalently immobilized on the surface of Co–B/SiO₂/NH₂ NPs using N-(3-dimethylaminopropyl)-N′-ethylcarbodiimide (EDC) as an activating agent. The magnetic NPs characteristics, such as the synthesis of Co–B/SiO₂/NH₂ NPs, effect of pH, temperature, and concentration of buffer for enzyme immobilization, were investigated. The optimal reaction conditions for immobilization were determined to be 0.1 M of phosphate buffer solution, pH 7.0, and 5 °C. In the case of immobilized GOD without d-glucose and with 0.1 M of d-glucose for blocking, 22.98 U/g and 24.83 U/g of their original activity were retained after 7 reuses, respectively.     

Enhancing oxidation activity and stability of iso-1-cytochrome c and chloroperoxidase by immobilization in nanostructured supports

The immobilization of enzymes in inorganic materials has been widely used because it can produce an enhancement of the catalytic stability and enzymatic activity. In this article, the effect of the immobilization of iso-1-cytochrome c (CYC-Sc) from Saccharomyces cerevisiae and chloroperoxidase (CPO) from Caldariomyces fumago on the enzyme stability and catalytic oxidation of styrene was studied. The immobilization was carried out in three silica nanostructured supports with different pore size MCM-41 (3.3 nm), SBA-15 (6.4 nm) and MCF (12.1 nm). The adsorption parameters and leaching degree of immobilized enzymes were determined. Catalytic parameters of immobilized and free enzymes were determined at different temperatures (20–60 °C) and in different acetonitrile/water mixtures (15–85% of acetonitrile). The results show that there is low leaching of the enzymes in the three supports assayed and the adsorption capacity (q_max) was higher as the pore size of the support increased. The pore size also produces the enhancement of peroxidase activities on the styrene oxidation. Thus, CPO adsorption into SBA-15 and MCF showed remarkable thermal and solvent stabilities at 40 °C showing a total turnover numbers of 48,000 and 54,000 times higher than free CPO, respectively. The enhancement of activity and stability doubtless is interesting for the potential industrial use of peroxidases.     

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.     

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.     

Comparing the performance of granular coral limestone and Leca in adsorbing Acid Cyanine 5R from aqueous solution

The effect of granular coral limestone and Leca as adsorbents for removing Acid Cyanine 5R (AC5R) from aqueous solution was studied. The optimum pH and adsorbent particles size in both adsorbents were determined to be 3 and 297 μm, respectively. The optimum dosages of coral limestone and granular Leca were 0.150 and 0.145 g/mg of dye, respectively. Also, results have shown that the adsorption efficiency by both coral limestone and Leca increased with the decreasing adsorbent particles size. Moreover, under similar conditions, the maximum removal efficiency by granular coral limestone and Leca was 94% and 88%, respectively. The results revealed that the performance of granular coral limestone was better in AC5R removal than that of Leca granulated under such condition. In total, granular coral limestone and Leca act as suitable adsorbents for removing dye pollutants from an aqueous solution.     

Microwave assisted synthesis of naphthopyrans catalysed by silica supported fluoroboric acid as a new class of non purine xanthine oxidase inhibitors

A series of naphthopyrans was synthesized employing silica supported fluoroboric acid under solvent free conditions in a microwave reactor. The catalytic influence of HBF₄–SiO₂ was investigated in detail to optimize the reaction conditions. The synthesised compounds were evaluated for in vitro xanthine oxidase inhibitory activity for the first time. Structure–activity relationship analyses have also been presented. Among the synthesised compounds, NP-17, NP-19, NP-20, NP-23, NP-24, NP-25 and NP-26 were the active inhibitors with an IC₅₀ ranging from 4 to 17 μM. Compound NP-19 with a thiophenyl ring at position 1 emerged as the most potent xanthine oxidase inhibitor (IC₅₀ = 4 μM) in comparison to allopurinol (IC₅₀ = 11.10 μM) and febuxostat (IC₅₀ = 0.025 μM). The basis of significant inhibition of xanthine oxidase by NP-19 was rationalized by its molecular docking at MTE binding site of xanthine oxidase.     

Interaction of SiO2 nanoparticles with neuronal cells: Ionic mechanisms involved in the perturbation of calcium homeostasis

SiO₂ nanoparticles (NPs), in addition to their widespread utilization in consumer goods, are also being engineered for clinical use. They are considered to exert low toxicity both in vivo and in vitro, but the mechanisms involved in the cellular responses activated by these nanoobjects, even at non-toxic doses, have not been characterized in detail. This is of particular relevance for their interaction with the nervous system: silica NPs are good candidates for nanoneuromedicine applications. Here, by using two neuronal cell lines (GT1–7 and GN11 cells), derived from gonadotropin hormone releasing hormone (GnRH) neurons, we describe the mechanisms involved in the perturbation of calcium signaling, a key controller of neuronal function. At the non-toxic dose of 20 μg mL⁻¹, 50 nm SiO₂ NPs induce long lasting but reversible calcium signals, that in most cases show a complex oscillatory behavior. Using fluorescent NPs, we show that these signals do not depend on NPs internalization, are totally ascribable to calcium influx and are dependent in a complex way from size and surface charge. We provide evidence of the involvement of voltage-dependent and transient receptor potential-vanilloid 4 (TRPV4) channels.     

Lipase-catalyzed biodiesel production from soybean oil deodorizer distillate with absorbent present in tert-butanol system

Lipase-catalyzed alcoholysis of soybean oil deodorizer distillate (SODD) for biodiesel production was studied. During this system both free fatty acids and glycerides could be converted to biodiesel simultaneously. tert-Butanol has been adopted as the reaction medium, in which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated completely. There was no obvious loss in lipase activity even after being repeatedly used for 120 cycles. Fine-pored silica gel and 3 Å molecular were found to be effective to control by-product water concentration and much higher biodiesel yield could be achieved with those adsorbents present in the reaction system. The highest biodiesel yield of 97% could be achieved with 3 Å molecular sieve as the adsorbent.     

Enhanced anthraquinones production from adsorbent-treated Morinda elliptica cell suspension cultures in production medium strategy

Continuous removal of anthraquinones (AQ) by Amberlite polymeric adsorbents (XAD-4, XAD-7 and XAD-16) through in situ adsorption in Morinda elliptica cell suspension cultures is studied for product recovery and improvement of the overall titre. Ethanol was the best eluting solvent for effective recovery of AQ from all adsorbents. Pre-treatment of XAD-4 with sodium acetate not only enhanced intracellular AQ, but also AQ release and subsequent recovery from the adsorbent. The addition of sodium acetate pretreated XAD-4 on day 18 for 6-day contact period, achieved comparable cell growth to control (41 g/L), but with 1.3-fold higher intracellular AQ (124 mg/g DW) and two-fold increase in extracellular AQ (14.3 mg/L). High amount of adsorbent and longer contact period for the cultures entering stationary growth phase, stimulated AQ release and recovery but at the expense of cell growth. With 5–8.3 g XAD-4 adsorbent per litre M. elliptica culture in production (P) medium, between 60 and 90% AQ was recovered from extracellular AQ after 24–26 days of culture period.     

Sono-chemical preparation of cellulose nanocrystals from lignocellulose derived materials

This study examined the production of cellulose nanocrystals from microcrystalline wood cellulose, Avicel and recycled pulp of wood pulp using sono-chemical-assisted hydrolysis. Two hydrolysis systems: deionized water and maleic acid were evaluated. In deionized water, Avicel produced cellulose nanocrystals with average diameter of 21 ± 5 nm (minimum 15 nm and maximum 32 nm). Cellulose nanocrystals from recycled pulp were not distinctively spherical and had an average diameter of 23 ± 4 nm (minimum 14 nm and maximum 32 nm). Maleic acid (50 mM) sono-chemical assisted hydrolysis of Avicel at 15 °C and 90% power output for 9 min produced cellulose nanocrystals which were cylindrical in shape and were of dimensions, length 65 ± 19 nm and width 15 nm.     

Amperometric biosensor based on enzymes immobilized in hybrid mesoporous membranes for the determination of acetylcholine

Acetylcholine sensor is successfully prepared by using immobilized enzymes, i.e., acetylcholinesterase and choline oxidase within separate hybrid mesoporous silica membranes with 12 nm pore diameter (F127M). The measurement was based on the detection of hydrogen peroxide produced by two sequential enzyme reactions. The determination range and the response time are 6.0–800 μM and within approximately 3 min, respectively. The sensor is very stable compared to free enzymes and 80% of the initial response was maintained even after storage for 80 days. These results show that two enzymes are successfully immobilized and well stabilized, and at the same time, two sequential enzyme reactions efficiently proceed within the separate hybrid mesoporous membranes. Further, we studied the possible detection of organophosphorus pesticides in terms of the inhibition of acetylcholinesterase activity, i.e., the decrease of current response, and demonstrated that the nanomolar concentrations of pesticide (DZN-oxon) can be detected with our sensor.     

Synthesis and characterization of pHLIP® coated gold nanoparticles

Novel approaches in synthesis of spherical and multispiked gold nanoparticles coated with polyethylene glycol (PEG) and pH Low Insertion Peptide (pHLIP^®) were introduced. The presence of a tumor-targeting pHLIP^® peptide in the nanoparticle coating enhances the stability of particles in solution and promotes a pH-dependent cellular uptake. The spherical particles were prepared with sodium citrate as a gold reducing agent to form particles of 7.0±2.5 nm in mean metallic core diameter and ～43 nm in mean hydrodynamic diameter. The particles that were injected into tumors in mice (21 µg of gold) were homogeneously distributed within a tumor mass with no staining of the muscle tissue adjacent to the tumor. Up to 30% of the injected gold dose remained within the tumor one hour post-injection. The multispiked gold nanoparticles with a mean metallic core diameter of 146.0±50.4 nm and a mean hydrodynamic size of ~161 nm were prepared using ascorbic acid as a reducing agent and disk-like bicelles as a template. Only the presence of a soft template, like bicelles, ensured the appearance of spiked nanoparticles with resonance in the near infrared region. The irradiation of spiked gold nanoparticles by an 805 nm laser led to the time- and concentration-dependent increase of temperature. Both pHLIP^® and PEG coated gold spherical and multispiked nanoparticles might find application in radiation and thermal therapies of tumors.     

Facile purification of mono-PEGylated interleukin-1 receptor antagonist and its characterization with multi-angle laser light scattering

Recombinant human interleukin-1 receptor antagonist (rhIL-1ra) was chemically conjugated with succinimidyl carbonate monomethoxyl polyethylene glycols of 5 kDa (SC-PEG_5k) and 10 kDa (SC-PEG_10k) molecular weight. A facile purification of the conjugates was achieved by one-step cationic exchange chromatography. The purity of mono-PEGylated protein was greater than 95%. The purified conjugate was characterized by multi-angle laser light scattering (MALLS) for determining the apparent gyration radius (r_g) and hydrodynamic radius (r_h). MALLS results showed that the conjugation of PEG markedly enhanced r_g and r_h of parent protein (r_g: from 15.7 to 48.2 nm for the PEG_5k and 81.9 nm for the PEG_10k; r_h: from 4.2 to 58.4 nm for the PEG_5k and 102.3 nm for the PEG_10k). The PEGylated rhIL-1ra retained 44.6% of binding activities to the cell receptor for PEG_5k and 40.2% for PEG_10k, compared to the original protein.     

Effects of pore characters of mesoporous resorcinol–formaldehyde carbon gels on enzyme immobilization

This paper demonstrates, for the first time, the use of resorcinol–formaldehyde carbon gels (RFCs) as enzyme carriers. The immobilization behavior of Bacillus licheniformis serine protease in RFCs of different pore characters was investigated. RFCs derived with (RF1) and without (RF2) cationic surfactant (trimethylstearylammonium chloride; C18) resulted in predominantly microporous, and mesoporous characters, respectively. It was found that support pore size and volume were key parameters in determining immobilized enzyme loading, specific activity, and stability. RF2, with higher mesopore volume (V_mes: RF1 = 0.21 cm³/g; RF2 = 0.81 cm³/g) and mesopore size radius (RF1 = 1.7–3.8 nm; RF2 = 7.01 nm), accommodated approximately fourfold more enzyme than RF1. Serine protease loading in RF2 could reach as high as 21.05 unit/g support. In addition, RF2 was found to be a better support in terms of serine protease operation and storage stability. Suitable mesopore size likely helped preventing immobilized enzyme from structural denaturation due to external forces and heat. However, immobilized enzyme in RF1 gave 12.8-fold higher specific activity than in RF2, and 2.1-fold higher than soluble enzyme. Enzyme leaching was found to be problematic in both supports, nonetheless, higher desorption was observed in RF2. Enhancement of interaction between serine protease and RFCs as well as pore size adjustment will be necessary for repeated use of the enzyme and further process development.     

Characterization and evaluation of hydrophobically modified chitosan scaffolds: Towards design of enzyme immobilized flow-through electrodes

Chitosan scaffolds were fabricated by application of thermally induced phase separation from aqueous solutions of unmodified chitosan and hydrophobically modified chitosan polymer. The final pore structure, in terms of diameter and geometry, were correlated to freezing temperature and freezing time for both the unmodified and hydrophobically modified chitosan polymer. Results showed that the resulting pore structure is strongly dependent upon the freezing temperature and less dependant upon the freezing time. For scaffolds produced from unmodified chitosan, the pore size decreased as expected with decreasing freezing temperature from ?5 °C to ?10 °C. However, an inconsistency in this trend was observed as the freezing temperature was decreased to ?20 °C. Combined analysis of pore size distribution and average pore diameter suggested that the freezing process was mainly mass transfer dominated at ?5 °C and ?10 °C, but principally heat transfer dominated at ?20 °C. In comparison, the scaffolds produced from hydrophobically modified chitosan (butyl-chitosan) followed the expected trend of decreasing mean pore diameter with decreased freezing temperatures throughout the entire temperature range. The scaffolds produced from the unmodified chitosan were more stable and rigid, and possessed average pore diameters that were generally smaller than those fabricated from the hydrophobically modified chitosan. The generally larger pores in the butyl-modified chitosan scaffolds might be explained by increased phase separation rates due to the introduced hydrophobicity of the chitosan polymer. Among the scaffolds fabricated from the butyl-modified chitosan, those produced at ?20 °C yielded the most uniform pore structure, the smallest average pore diameters, and the least temporal broadening of pore size distribution.