Characteristics of an aqueous two-phase system for α-amylase production

The characteristics of an aqueous two-phase system for the overproduction of extracellular enzyme through α-amylase fermentation by Bacillus amyloliquefaciens were investigated. With higher molecular weight of polyethylene glycol (PEG) or lower molecular weight of dextran, the partition coefficient of α-amylase was increased. α-Amylase biosynthesis was increased when PEG 6000 was included in the medium compared to the medium without PEG. Phosphate addition to the PEG-dextran system improved the partition coefficient of α-amylase, but deactivated α-amylase severely. By using sodium sulfate instead of phosphate, α-amylase deactivation was negligible, and high partitioning of the enzyme in the top phase was obtained.     

Rapid process for purification of an extracellular β-xylosidase by aqueous two-phase extraction

A rapid process for purification of an extracellular β-xylosidase with high purity was developed. The manipulation involved the precipitation of protein from culture medium and the extraction of enzyme from the resuspended crude protein solution by an aqueous-two phase separation. A linear random copolymer, PE62, with 20% ethylene oxide and 80% propylene oxide was employed in both stages of the purification. The enzyme was precipitated effectively by using 10% (w/v) PE62 and 5% (w/v) Na₂HPO₄. The aqueous two-phase extraction was performed with PE62 (10%)–NaH₂PO₄ (15%) as phase-forming reagent. SDS–PAGE analysis revealed that the purified enzyme is near homogeneity. The yield is about 100% with a purification factor of 8.8-fold. The whole process can be completed within an hour without any column chromatography.     

Synthesis of octyl-β-d-glucopyranoside catalyzed by Thai rosewood β-glucosidase-displaying Pichia pastoris in an aqueous/organic two-phase system

We explored the ability of a Thai rosewood β-glucosidase-displaying P. pastoris whole-cell biocatalyst (Pp-DCBGL) system to synthesize alkyl β-d-glucosides. The primary investigation centered on the synthesis of octyl-β-d-glucopyranoside (octyl-glu, OG). OG could be synthesized through reverse hydrolysis reaction with very low efficiency. Then, OG was synthesized between BG and octanol by a transglycosylation reaction. In a 2-ml reaction system, OG was synthesized with a conversion rate of 51.1% in 3 h when 5 mg/ml BG was utilized as the glucosyl donor under optimized conditions. And, even after being reused four times, the Pp-DCBGL was relatively stable. Additionally, a 500-ml-scale reaction system was conducted in a 2-L stirred reactor with a conversion rate of 47.5% in 1.5 h. Moreover, the conversion rate did not decrease after the whole-cell catalyst was reused two times. In conclusion, Pp-DCBGL has high reaction efficiency and operational stability, which is a powerful biocatalyst available for industrial synthesis.     

Increased yield of biotransformation of exemestane with β-cyclodextrin complexation technique

In this study, 6-methylenandrosta-4-ene-3,17-dione and Hydroxypropyl-β-cyclodextrin (HP-β-CD) were used to form a complex, which could be then biotransformed by Arthrobacter simplex ATCC6946 to obtain the antitumor drug exemestane. The complex was analyzed by UV, DSC and TG techniques, while the products were analyzed by HPLC, NMR and MS. These results confirmed that the β-cyclodextrin not only improved the water-solubility of 6-methylenandrosta-4-ene-3,17-dione, but also greatly enhanced the biocompatibility during the biotransformation process. This result may be applied to other precursors which have poor aqueous solubility in the biotransformation processes.     

Production of β-glucosidase withAspergillus phoenicis QM329 in aqueous two-phase systems

Summary The production of -glucosidase withAspergillus phoenicis QM 329 was studied in two different aqueous two-phase systems: polyethylene glycol (PEG) 1550 7.5%/Dextran T2000 9.5% and PEG 8000 4%/polyvinyl alcohol (PVA) 14000 8%. The enzyme concentrations in the top phase of the phase systems were 3.4 IU/ml and 3.2 IU/ml, respectively, compared with 2.0 IU/ml obtained in a regular medium. The total amount of -glucosidase obtained in the phase systems was 265 IU and 176 IU, respectively, compared with 200 IU in a regular medium.     

Separation of recombinant β-glucuronidase from transgenic tobacco by aqueous two-phase extraction

Transgenic plants hold many promises as viable production hosts for therapeutic recombinant proteins. Many efforts have been devoted to increase the expression level of the proteins, but the efforts for developing economic processes to purify those proteins are lacking. In this report, aqueous two-phase extraction (ATPE) was investigated as an alternative for the separation of an acidic recombinant protein, β-glucuronidase (rGUS), from transgenic tobacco. Screening experiments by fractional factorial designs showed that PEG concentration and ionic strength of the system significantly affected the partitioning of native tobacco proteins and GUS. Response surface methodology was used to determine an optimized aqueous two-phase system for the purification of rGUS from transgenic tobacco. In a 13.4% (w/w) PEG 3400/18% (w/w) potassium phosphate system, 74% of the rGUS was recovered in the top PEG-rich phase while more than 90% of the native tobacco proteins were removed in the interphase and the bottom phase. A purification factor of about 20 was achieved in this process. The most important impurity from tobacco, Rubisco, was largely removed from the rGUS in the recovered phase.     

Integrated immobilized cell reactor-adsorption system for β-cyclodextrin production: a model study using PVA-cryogel entrapped Bacillus agaradhaerens cells

Production of cyclodextrins (CDs) by immobilized cells of the alkaliphilic Bacillus agaradhaerens LS-3C with integrated product recovery was studied. The microorganism was entrapped in polyvinyl alcohol-cryogel beads and used as a convenient source of immobilized cyclodextrin glycosyltransferase (CGTase). On activation by incubation in the cultivation medium containing 1% (w/v) starch, the entrapped cells multiplied and secreted CGTase with an activity of 2–3 mg -cyclodextrin h^–1 g^–1 beads. The immobilized biocatalyst exhibited maximum activity at pH 9 and 50 °C, and formed cyclodextrins comprising 92–94% -CD and remaining -CD. The cyclodextrin product from the immobilized cell bioreactor was continuously recovered by adsorption to Amberlite XAD-4 in a recycle batch mode. The product adsorption was facilitated at low temperature while hot water was used for elution.     

α-Amylase production in aqueous two-phase systems with Bacillus amyloliquefaciens

-Amylase production was studied in Bacillus amyloliquefaciens in aqueous two-phase systems composed of polyethyleneglycol (PEG)/dextran T500. Cells and enzyme were obtained in different phases when phase systems were applied to the growth media. Effects of different molecular weights and concentrations of polymers on differences of enzyme separation were established. The effect of PEG used in the system to the release of enzyme was investigated.     

α-amylase production in aqueous two-phase systems with Bacillus subtilis

The production of α-amylase (1,4-α-d-glucan glucanohydrolase, EC 3.2.1.1) by Bacillus subtilis has been studied in repeated batch fermentations in aqueous two-phase systems. In a phase system composed of PEG 600, 8% (w/w), PEG 3350, 5% (w/w)/Dextran T 500, 2% (w/w), 82% of the enzyme partitioned to the top phase. The enzyme concentration in the top phase reached 0.85–1.35 U ml^?1 during the fermentations compared with 0.58 U ml^?1 in the reference fermentation. In the phase system composed of PEG 3350, 9% (w/w)/Dextran T 500, 2% (w/w), 73% of the enzyme partitioned to the top phase. However, the enzyme concentration in this phase system reached only 0.35 U ml^?1 in the top phase. The bacterial cells were microscopically observed to partition totally to the bottom phase in the aqueous two-phase system used. The results are discussed in relation to recirculation of cells by immobilizing to a solid matrix. Extraction of the product to the top phase and the effect of the phase polymers, especially PEG, on the production are also discussed.     

Increased production of cloned β-galactosidase in two-stage culture of Bacillus amyloliquefaciens

Bacillus amyloliquefaciens harboring recombinant plasmid pHG5, which encodes B. stearothermophilus β-galactosidase, was cultured in a jar fermentor. By feeding lactose a considerable concentration of the enzyme was produced, but the cells stopped growing at an OD₆₆₀ of about 30. On the other hand, the microorganism grew to a very high cell concentration with an OD₆₆₀ of around 110 with glucose as a carbon source, but the enzyme specific activity was a half of the maximum value with lactose. Based on these facts, B. amyloliquefaciens was first grown using glucose, and the carbon source was then switched to lactose to induce β-galactosidase production. By this two-step culture method, both good cell growth and high enzyme productivity were obtained.     

Lactose hydrolysis in aqueous two-phase system by whole-cellβ-galactosidase of Kluyveromyces marxianus

Semicontinuous and continuous hydrolysis of lactose in aqueous two-phase systems (polyethylene glycol 20000/dextran 40) with whole-cell-galactosidase ofK. marxianus were studied. Both phase polymers had no effect on-galactosidase activity confined in cells. Good operational stability of the biocatalyst during 55 cycles of semicontinuous process was observed without appreciable decrease in product concentration. Continuous hydrolysis of lactose was performed in the stirred bioreactor, connected with the phase separator. The satisfactory degree of hydrolysis (between 82–88%) and volumetric productivity (21.6 g/l/h) were reached during 72 hours of continuous hydrolysis of 5% (w/w) lactose.     

Enhanced production of extracellular α-amylase and glucoamylase by amylolytic yeasts using β-cyclodextrin as carbon source

Summary Several amylolytic yeasts from the genera Candida, Cryptococcus, Filobasidium, Lipomyces, Saccharomycopsis, Schwanniomyces, and Trichosporon can utilize -cyclodextrin as a sole carbon source. For most species significantly higher yields of both -amylase and glucoamylase are obtained as compared to with starch. This novel inducer of yeast amylases should therefore be useful in the characterization of these amylolytic enzymes and their regulation.     

New mode of Dunaliella biotechnology: two-phase growth for β-carotene production

Attempts to adapt the laboratory experience of bi-phasic growth and carotenogenesis in Dunaliella to large-scale conditions were highly successful. Algae were initially cultivated in stage one for optimizing biomass production of cells containing a low β-carotene to chlorophyll ratio. The culture was then transferred to stage two, diluted to about one third and induced for carotenogenesis. The bi-phase cultivation increased β- carotene productivity to 450 mg m^-2 d^-1 in stage one and to 300 mg m^-2 d^-1 in stage two, compared to the relatively low productivity of below 200 mg β- carotene m^-2 d^-1, in the conventional one phase type of cultivation. The results indicate that a selected algal product can be promoted specifically by growth manipulation of the alga and its environment.     

Liquid–liquid extraction of an extracellular alkaline protease from fermentation broth using aqueous two-phase and reversed micelles systems

Summary The study of recovery of an extracellular alkaline protease from fermentation broth produced by Norcadiopsis sp, was carried out with liquid–liquid extraction through sodium di-(2-ethylhexyl) sulphosuccinate/isooctane reversed micelles systems and aqueous two-phase systems (polyethylene glycol/potassium phosphate). The best conditions for extraction and back-extraction with the reversed micelles system was obtained at pH 9.0 and pH 5.0, respectively, showing a yield of protein of 6.16%, a specific activity of 4.10 U/ml and a purification factor of 1.80. The studies using aqueous two-phase systems of polyethylene glycol/potassium phosphate at pH 10.0 showed purification factors of 2 and 5, and protein yield of 11 and 4%, respectively, for polyethylene glycol 550/potassium phosphate and polyethylene glycol 8000/potassium phosphate. The results indicate that the aqueous two-phase systems are more attractive as a first step in the isolation and purification processes.     

Molecular recognition and enhancement of aqueous solubility and bioactivity of CD437 by β-cyclodextrin

CD437 (6-[3-(1-adamantyl)-4-hydroxyphenyl]-2-naphthalene carboxylic acid) is a novel synthetic retinoic acid derivative that has been shown to selectively induce apoptosis in human lung cancer cells. This compound, however, is limited in its application due to its low solubility in aqueous solutions. One technique for increasing the solubility and bioavailability of a cytotoxic agent is the formation of inclusion complexes with cyclodextrins. Herein, we report the formation and characterization of a 2:1 complex between β-cyclodextrin (β-CD) and CD437. It is shown that CD437 is a tight binder of β-CD with an overall association constant of 2.6 ± 0.6 × 10⁷ M⁻². In addition, we demonstrate (a) that β-CD-derived complexation enhances the aqueous solubility of CD437, and (b) that a significant increase in the toxicity of CD437 against a human lung adenocarcinoma cell line can be achieved by co-treatment with β-CD.     

Partitioning of α-lactalbumin and β-lactoglobulin in aqueous two-phase systems of polyvinylpyrrolidone and potassium phosphate

In the present study, the partitioning of α-lactalbumin, β-lactoglobulin, and cheese whey proteins in aqueous two-phase system of polyvinylpyrrolidone-potassium phosphate is investigated. The partitioning of proteins in this system depends on the polymer and salt weight percents in feed, temperature, and pH. The orthogonal central composite design is used to study the effects of different parameters on partitioning of α-lactalbumin and β-lactoglobulin. A second order model is proposed to determine the impact of these parameters. The results of the model show that the weight percent of the salt in feed has a large effect on the protein partitioning. The weight percent of polyvinylpyrrolidone in the feed increases the partitioning coefficients. By increasing the temperature, the viscosity of polyvinylpyrrolidone is reduced and the protein can easily be transferred from one phase to the other phase. The pH of the aqueous two phase system can alter the protein partitioning coefficient through the variation of the protein net charge.     

Theoretical study of an anti-Markovnikov addition reaction catalyzed by β-cyclodextrin

Journal of Molecular Modeling - Human sodium-dependent glucose co-transporter 2 (hSGLT2) is a crucial therapeutic target in the treatment of type 2 diabetes. In this study, both comparative...     

Hyper production of β-glucosidase by an Aspergillus sp.

Summary An Aspergillus sp. was isolated which secreted high levels of -glucosidase in growth medium. The maximum activity(10 IU/ml of -glucosidase and 22.6 IU/ml of cellobiase) was obtained in cellulose medium supplemented with wheat bran. The pH and temperature optima for this enzyme were 4.5 and 65°C respectively.NCL Communication No. 3616