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.     

Microbial production of (S)-1-phenyl-1,3-propanediol by stereospecific reduction of 3-hydroxy-1-phenylpropane-1-one

A novel microbial method of synthesizing (S)-1-phenyl-1,3-propanediol [(S)-PPD] was developed in this study. Our laboratory stock cultures were screened for microorganisms that stereospecifically produced (S)-PPD from 3-hydroxy-1-phenylpropane-1-one (HPPO) using an intact cell system. Of the 828 strains examined (321 bacteria, 233 yeasts and 274 molds), certain strains of Williopsis saturnus var. mrakii and Cryptococcus albidus were found to produce (S)-PPD with over 99% enantiomeric excess (e.e.). Screening identified W. saturnus var. mrakii AJ-5620 as the most productive strain, and this strain was used for further experiments. The (S)-PPD-producing reaction using intact W. saturnus var. mrakii AJ-5620 cells was carried out by successive feeding of HPPO. A total (S)-PPD yield of 9.9 g/l was produced in 20 h. The molar yield was 81% and the optical purity of the (S)-PPD produced was over 99% e.e.     

Applying slow-release biocatalysis to the asymmetric reduction of ethyl 4-chloroacetoacetate

Amberlite XAD 2 resin enhanced the asymmetric reduction of ethyl 4-chloroacetoacetate (ECA) to S-4-chloro-3-hydroxybutyric acid ethyl ester as catalyzed by Saccharomyces cerevisiae. The absorbed ECA was released slowly to the solution during the reaction so that the substrate inhibition and the spontaneous chemical hydrolysis of ECA were considerably lessened. With 75 g resin l^–1 and ECA at 74 mM, the reaction yield and the product's optical purity increased from 75% to 84% and from 88% to 93%, respectively.     

Enantioselective synthesis of ethyl-(S)-3-hydroxy-3-phenylpropanoate (S-HPPE) from ethyl-3-oxo-3-phenylpropanoate using recombinant fatty acid synthase (FAS2) from Kluyveromyces lactis KCTC 7133 in Pichia pastoris GS115

Various yeast strains were examined for the microbial reduction of ethyl-3-oxo-3-phenylpropanoate (OPPE) to ethyl-(S)-3-hydroxy-3-phenylpropanoate (S-HPPE), which is the chiral intermediate for the synthesis of a serotonin uptake inhibitor, Fluoxetine. Kluyveromyces lactis KCTC 7133 was found as the most efficient strain in terms of high yield (83% at 50 mM) and high optical purity ee > 99% of S-HPPE. Based on the protein purification, activity analysis and the genomic analysis, a fatty acid synthase (FAS) was identified as the responsible β-ketoreductase. To increase the productivity, a recombinant Pichia pastoris GS115 over-expressing FAS2 (α-subunit of FAS) of K. lactis KCTC7133 was constructed. In the optimized media condition, the recombinant P. pastoris functionally over-expressed the FAS2. Recombinant P. pastoris showed 2.3-fold higher reductase activity compared with wild type P. pastoris. With the recombinant P. pastoris, the 91% yield of S-HPPE was achieved at 50 mM OPPE maintaining the high optical purity of the product (ee > 99%).     

Integration of ion exchange resin materials for a downstream-processing approach of an imine reductase-catalyzed reaction

In this study, an ion exchange resin-based downstream-processing concept for imine reductase (IRED)-catalyzed reactions was investigated. As a model reaction, 2-methylpyrroline was converted to its corresponding product (S)-2-methylpyrrolidine with >99% of conversion by the (S)-selective IRED from Paenibacillus elgii B69. Under optimized reaction conditions full conversion was achieved using a substrate concentration of 150 and 500 mmol/L of d -glucose. Seven commercially available cation- and anion-exchange resins were studied with respect to their ability to recover the product from the reaction solution. Without any pretreatment, cation-exchange resins Amberlite IR-120(H), IRN-150, Dowex Monosphere 650C, and Dowex Marathon MSC showed high recovery capacities (up to >90%). A 150-ml preparative scale reaction was performed yielding ~1 g hydrochloride salt product with >99% purity. Any further purification steps, for example, by column chromatography or recrystallization, were not required.     

Production and purification of recombinant Blomia tropicalis group 5 allergen from Pichia pastoris culture

The gene of Blomia tropicalis group 5 allergen (Blo t 5) was cloned and expressed in Pichia pastoris KM71. Selected KM71 clones were cultivated in a fed-batch bioreactor feeding first glycerol then followed by methanol. Recombinant Blo t 5 constituted about 30% of the total broth protein after 60 h cultivation. The harvested broth was purified to >95% purity by a two-step anion exchange chromatography. The overall yield was 37 mg Blo t 5 per litre broth.     

A novel carbonyl reductase from Pichia stipitis for the production of ethyl (S)-4-chloro-3-hydroxybutanoate

An NADPH-dependent carbonyl reductase (PsCR) gene from Pichia stipitis was cloned. It contains an open reading frame of 849 bp encoding 283 amino acids whose sequence had less than 60% identity to known reductases that produce ethyl (S)-4-chloro-3-hydroxybutanoates (S-CHBE). When expressed in Escherichia coli, the recombinant PsCR exhibited an activity of 27 U/mg using ethyl 4-chloro-3-oxobutanoate (COBE) as a substrate. Reduction of COBE to (S)-CHBE by transformants in an aqueous mono-phase system for 18 h, gave a molar yield of 94% and an optical purity of the (S)-isomer of more than 99% enantiomeric excess.     

Transformation of cholesterol to testosterone byMycobacterium sp.

Summary The production of testosterone from cholesterol via a single-step microbial transformation process was investigated. A supplement of44% glucose and 1% peptone into a synthetic medium, pH control at 6.0 and continuous feeding of cholesterol were the most important parameters. Under optimal conditions, the maximum molar conversion rate of testosterone from cholesterol was up to 42.68% in 2.5-L surface-aerated fermentor after 100 h cultivation. The reduction of androst-4-ene-3.17-dione, an intermediate product, to testosterone was catalyzed by 17-hydroxysteroid dehydrogenase inMycobacterium sp. Testosterone was isolated from the fermentation broth by the addition of Amberlite XAD-7 resin and was further purified by flash chromatography on a silica gel column. After crystallization in acetone, testosterone could be obtained as needle crystals.     

Purification and properties of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis><Emphasis Type="Italic">S</Emphasis>-adenosylmethionine synthetase expressed in recombinant <Emphasis Type="Italic">Pichia pastoris</Emphasis>

An intracellular S-adenosylmethionine synthetase (SAM-s) was purified from the fermentation broth of Pichia pastoris GS115 by a sequence chromatography column. It was purified to apparent homogeneity by (NH₄)₂SO₄ fractionation (30–60%), anion exchange, hydrophobic interaction, anion exchange and gel filtration chromatography. HPLC showed the purity of purified SAM-s was 91.2%. The enzyme was purified up to 49.5-fold with a final yield of 20.3%. The molecular weight of the homogeneous enzyme was 43.6 KDa, as determined by electro-spray ionization mass spectrometry (ESI-MS). Its isoelectric point was approximately 4.7, indicating an acidic character. The optimum pH and temperature for the enzyme reaction were 8.5 and 35 °C, respectively. The enzyme was stable at pH 7.0–9.0 and was easy to inactivate in acid solution (pH ≤ 5.0). The temperature stability was up to 45 °C. Metal ions, such as, Mn²⁺ and K⁺ at the concentration of 5 mM had a slight activation effect on the enzyme activity and the Mg²⁺ activated the enzyme significantly. The enzyme activity was strongly inhibited by heavy metal ions (Cu²⁺ and Ag²⁺) and EDTA. The purified enzyme from the transformed Pichia pastoris synthesized S-adenosylmethionine (SAM) from ATP and l-methionine in vitro with a K _m of 120 and 330 μM and V _max of 8.1 and 23.2 μmol/mg/min for l-methionine and ATP, respectively.     

Comparison of engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> and engineered <Emphasis Type="Italic">Escherichia coli</Emphasis> for the production of an optically pure keto alcohol

In this study, the production of enantiomerically pure (1R,4S,6S)-6-hydroxy-bicyclo[2.2.2]octane-2-one ((−)-2) through stereoselective bioreduction was used as a model reaction for the comparison of engineered Saccharomyces cerevisiae and engineered Escherichia coli as biocatalysts. For both microorganisms, over-expression of the gene encoding the NADPH-dependent aldo-keto reductase YPR1 resulted in high purity of the keto alcohol (−)-2 (>99% ee, 97–98% de). E. coli had three times higher initial reduction rate but S. cerevisiae continued the reduction reaction for a longer time period, thus reaching a higher conversion of the substrate (95%). S. cerevisiae was also more robust than E. coli, as demonstrated by higher viability during bioreduction. It was also investigated whether the NADPH regeneration rate was sufficient to supply the over-expressed reductase with NADPH. Five strains of each microorganism with varied carbon flux through the NADPH regenerating pentose phosphate pathway were genetically constructed and compared. S. cerevisiae required an increased NADPH regeneration rate to supply YPR1 with co-enzyme while the native NADPH regeneration rate was sufficient for E. coli. Nádia Skorupa Parachin and Magnus Carlquist have contributed equally to the paper.     

Immobilization of cyclodextrin glucanotransferase on amberlite IRA-900 for biosynthesis of transglycosylated xylitol

Cyclodextrin glucanotransferase (CGTase) fromThermoanaerobacter sp. was adsorbed on the ion exchange resin Amberlite IRA-900. The optimum conditions for the immobilization of the CGTase were pH 6.0 and 600 U CGTase/g resin, and the maximum yield of immobilization was around 63% on the basis of the amount ratio of the adsorbed enzyme to the initial amount in the solution. Immobilization of CGTase shifted the optimum temperature for the enzyme to produce transglycosylated xylitol from 70°C to 90°C and improved the thermal stability of immobilized CGTase, especially after the addition of soluble starch and calcium ions. Transglycosylated xylitol was continuously produced using immobilized CGTase in the column type packed bed reactor, and the operating conditions for maximum yield were 10% (w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10% (w/v) xylitol as the glycosyl acceptor, 20 mL/h of medium flow rate, and 60°C. The maximum yield of transglycosylated xylitol and productivity were 25% and 7.82 g·L⁻¹·h⁻¹, respectively. The half-life of the immobilized CGTase in a column type packed bed reactor was longer than 30 days.     

A Simple and Green Procedure for the Microbial Effective Synthesis of 1-phenylethyl Alcohol in Both Enantiomeric Forms

Both R- and S-phenylethyl alcohol of high enantiomeric purity (98%) and with a satisfactory yield (40–80%) were obtained by bioreduction of acetophenone, catalyzed by whole cells of baker’s yeast. Revisions requested 29 November 2005; Revisions received 9 January 2006     

Routine manufacture of recombinant proteins using expanded bed adsorption chromatography

Two different recombinant human proteins were purified directly from Pichia pastoris whole cell fermentation broth, containing 30–44% biomass (wet weight percent), by strong cation exchange expanded bed adsorption chromatography. Expanded bed adsorption chromatography provided clarification, product purification and product concentration in a single unit operation at large scale (2000-l nominal fermentation volume). The efficiency of expanded bed adsorption chromatography resulted in a short process time, high process yield, and limited proteolytic degradation of the target proteins. The separations were operated using a 60-cm (d) column run at 14 l/min. For one protein, expanded bed adsorption chromatography resulted in an average product recovery of 113% (relative to fermentation supernatant) and a purity of 89% (n=10). For the other protein, the average product recovery was 99% (relative to fermentation supernatant) and the purity was 62.1 (n=10). Laboratory experiments showed that biomass reduced product dynamic binding capacity for protein 2.     

Production of (<Emphasis Type="Italic">R</Emphasis>)-ethyl-3,4-epoxybutyrate by newly isolated <Emphasis Type="Italic">Acinetobacter baumannii</Emphasis> containing epoxide hydrolase

Several new microorganisms have been isolated from soil samples with high epoxide hydrolase activity toward ethyl 3,4-epoxybutyrate. Screening was performed by enrichment culture on alkenes as sole carbon source, followed by chiral gas chromatography. Eight strains were discovered with enantioselectivity from moderate to high level and identified as bacterial and yeast species. Cells were cultivated under aerobic condition at 30°C using glucose as carbon source and resting cells were used as biocatalysts for kinetic resolution of ethyl 3,4-epoxybutyrate. Among isolated microorganisms, Acinetobacter baumannii showed highest enantioselectivity for (S)-enantiomer, resulting in (R)-ethyl-3,4-epoxybutyrates (>99%ee, 46% yield). It is the first report on the fact that epoxide hydrolases originating from bacterial species of A. baumannii was applied to kinetic resolution of ethyl 3,4-epoxybutyrate in order to obtain enantiopure high-value-added (R)-ethyl-3,4-epoxybutyrate.     

Optical Resolution and Optimization of (R,S)‐Propranolol Using Dehydroabietic Acid Via Diastereomeric Crystallization

The optical resolution of (R,S)‐propranolol by the diastereomeric crystallization method was successfully performed using dehydroabietic acid (DHAA) as the resolving agent in methanol. The three important parameters: DHAA amount, solvent (methanol) amount, and crystallization temperature of diastereomeric salts were optimized employing the response surface methodology (RSM). When maintaining a lower limit of 95% for the purity of (S)‐propranolol, the optimal resolution conditions were a DHAA/(R,S)‐propranolol molar ratio of 1.1, solvent/(R,S)‐propranolol ratio of 16.2 mL.g^‐1, and crystallization temperature of –5 °C. The desired (S)‐propranolol was prepared with 94.8% optical purity and 72.2% yield under the optimal conditions. Chirality 27:131–136, 2015. © 2014 Wiley Periodicals, Inc.     

Conversion of paper sludge to ethanol. I: Impact of feeding frequency and mixing energy characterization

In this paper, conversion of paper sludge to ethanol was investigated with the objective of optimization of the overall operation costs. Experimental work was undertaken to optimize cellulase loading, and to determine mixing energy requirements. It was found that decreasing feeding frequency (feed additions per residence time) allows the cellulase loading to be decreased at least two fold with no decrease in cellulose conversion but also entails mixing a slurry of higher solids content and lower conversion at the beginning of the operating cycle. The viscosity of paper sludge slurries was found to increase exponentially with decreasing conversion and increasing solid content. In particular, the viscosity (V) was described well by equation V = e^(kX−X ₀^)(S−S ₀^)+C (V viscosity (cp), X conversion, S solid content (g/L), k, X ₀, S ₀, C are empirical parameters). Added costs associated with operating at low feeding frequencies (including higher mixing energy and higher capital costs for the motor and for sludge hold tasks) were found to be small compared to the economic benefits resulting from reduced cellulase loading.     

In situ separation of lactic acid from fermentation broth using ion exchange resins

Lactic acid fermentation is an end product inhibited reaction. In situ separation of lactic acid from fermentation broth using ion exchange resins was investigated and compared with conventional fermentation system. Amberlite resin (IRA-400, Cl⁻) was used to separate lactic acid from fermentation broth and pH was controlled online with an automatic pH controller. The effect of process variables on lactic acid production by Lactobacillus casei in whey permeate was studied. The maximum productivity was obtained at pH = 6.1, T = 37 °C and impeller speed = 200 rpm. The maximum concentration of lactic acid at optimum condition was found to be 37.4 g/L after 38 h of fermentation using in situ separation system. The productivity of in situ separation system was five times increased in comparison with conventional system.     

Stereoselective reduction of 2-substituted cyclohexanones by Saccharomyces cerevisiae

A comparative study of two modifications of enzymic reduction of ethyl N-{2-{4-[(2-oxo-cyclohexyl)methyl]phe- noxy}ethyl} carbamate (1), an insect juvenile hormone bioanalog, was performed using Saccharomyces cerevisiae in two bioreactors of different size, 250-ml shake-flask and 1-l fermenter. The two major products of this reduction were obtained in 45–49% (w/w) yields but with > 99% enantiomeric purity. Their absolute configurations were assigned as ethyl (1S,2S)-N-{2-{4-[(2-hydroxycyclohexyl)methyl]phenoxy}ethyl}carbamate (2a) and ethyl (1R,2S)-N-{2-{4-[(2-hydroxycyclohexyl)methyl]phenoxy}ethyl}carbamate (3a).     

Isolation and characterization of Acinetobacter sp. ES-1 excreting a lipase with high enantioselectivity for (S)-ketoprofen ethyl ester

A new Acinetobacter sp. ES-1, grown on triolein, tryptone and Triton X-100, excreted a lipase that hydrolyzed 10m M (R,S)-ketoprofen ethyl ester into (S)-ketoprofen. The crude lipase had an activity of 10Uml^-1 and, at 30°C and pH7 over 48h, gave a conversion yield of 35% with an enantiomeric excess for the product 96%.     

Recovery of Nuclease Produced by Lactococcus Lactis Using Expanded Bed Ion Exchange Chromatography

Expanded bed-ionic exchange chromatography (EB-IEC) was used for the recovery and purification of recombinant staphylococcal nuclease secreted by Lactococcus lactis. At the end of the fermentation process, the nuclease activity reached 39 U ml⁻¹. The EB-IEC performances were firstly evaluated with clarified culture broth. The isocratic elution with 0.5 M NaCl led to approximately 80% of nuclease recovery. Proceeding with 3-fold bed expansion resulted in a reduction of the resin capacity by a factor of 32% compared to the process in a packed bed configuration. Simplification of the early purification steps was reached by loading immediately the unclarified culture broth previously diluted to reduce conductivity. Presence of Cells did not affect the chromatography performances resulting in 55-fold purification with the same yield.