Ginsenoside Rd production from the major ginsenoside Rb<Subscript>1</Subscript> by <Emphasis Type="Italic">β</Emphasis>-glucosidase from <Emphasis Type="Italic">Thermus caldophilus</Emphasis>

Under optimum conditions (pH 5, 75°C, and 0.2 U purified enzyme ml⁻¹), 4 mg ginsenoside Rd was produced from 5 mg reagent-grade ginsenoside Rb₁ in 5 ml after 30 min by β-glucosidase from Thermus caldophilus GK24. Using a ginseng root extract containing 1 mg ginsenoside Rb₁ ml⁻¹ and 3.2 mg additional ginsenosides ml⁻¹, 1.23 mg ginsenoside Rd ml⁻¹ was produced after 18 h; the concentrations of ginsenosides Rb₁, Rb₂, and Rc used for ginsenoside Rd production were 0.77, 0.17, and 0.19 mg ml⁻¹, respectively.     

Hydrolysis of soy isoflavone glycosides by recombinant β-glucosidase from hyperthermophile <Emphasis Type="Italic">Thermotoga maritima</Emphasis>

A recombinant Thermotoga maritima β-glucosidase A (BglA) was purified to homogeneity for performing enzymatic hydrolysis of isoflavone glycosides from soy flour. The kinetic properties K _m, k _cat, and k _cat/K _m of BglA towards isoflavone glycosides, determined using high-performance liquid chromatography, confirmed the higher efficiency of BglA in hydrolyzing malonylglycosides than non-conjugated glycosides (daidzin and genistin). During hydrolysis of soy flour by BglA at 80°C, the isoflavone glycosides (soluble form) were extracted from soy flour (solid state) into the solution (liquid state) in thermal condition and converted to their aglycones (insoluble form), which mostly existed in the pellet to be separated from BglA in the reaction solution. The enzymatic hydrolysis in one-step and two-step approaches yielded 0.38 and 0.35 mg genistein and daidzein per gram of soy flour, respectively. The optimum conditions for conversion of isoflavone aglycones were 100 U per gram of soy flour, substrate concentration 25% (w/v), and incubation time 3 h for 80°C.     

Isolation and functional characterization of <Emphasis Type="Italic">Lycopene β-cyclase</Emphasis> (<Emphasis Type="Italic">CYC-B</Emphasis>) promoter from <Emphasis Type="Italic">Solanum habrochaites</Emphasis>

Background  

Carotenoids are a group of C40 isoprenoid molecules that play diverse biological and ecological roles in plants. Tomato is an important vegetable in human diet and provides the vitamin A precursor β-carotene. Genes encoding enzymes involved in carotenoid biosynthetic pathway have been cloned. However, regulation of genes involved in carotenoid biosynthetic pathway and accumulation of specific carotenoid in chromoplasts are not well understood. One of the approaches to understand regulation of carotenoid metabolism is to characterize the promoters of genes encoding proteins involved in carotenoid metabolism. Lycopene β-cyclase is one of the crucial enzymes in carotenoid biosynthesis pathway in plants. Its activity is required for synthesis of both α-and β-carotenes that are further converted into other carotenoids such as lutein, zeaxanthin, etc. This study describes the isolation and characterization of chromoplast-specific Lycopene β-cyclase (CYC-B) promoter from a green fruited S. habrochaites genotype EC520061.     

Regeneration of transformed verbena (<Emphasis Type="Italic">Verbena </Emphasis>× <Emphasis Type="Italic">hybrida</Emphasis>) by <Emphasis Type="Italic">Agrobacterium tumefaciens</Emphasis>

Verbena (Verbena x hybrida), an important floricultural species, was successfully regenerated from stem segments on Murashige and Skoog's basal medium supplemented with thidiazuron and indole-3-acetic acid. A transformation system was developed using cvs. Temari Scarlet, Temari Sakura, Tapien Rose and TP-P2. Agrobacterium tumefaciens strain Agl0 harboring the sGFP gene was infected into stem segments. Transformation efficiency was improved by evaluating and manipulating the age of the plant material, the concentration of kanamycin in the medium during selection, and the length of the culture period in the dark. After 2-3 months of culture on the selection medium, GFP-positive shoots were obtained in all four of the cultivars tested. These shoots were successfully acclimated and set flowers within 2-3 months in a greenhouse. GFP was expressed in all of the organs including the floral parts. Stable genomic transformation was confirmed by Southern blot analysis. No morphological differences were observed between the transformed plants and their host plants.     

Asymmetric reduction of (<Emphasis Type="Italic">S</Emphasis>)-3-chloro-1-phenylpropanol from 3-chloropropiophenone by preheated immobilized <Emphasis Type="Italic">Candida</Emphasis> <Emphasis Type="Italic">utilis</Emphasis>

An efficient method for asymmetric reduction of (S)-3-chloro-1-phenylpropanol from 3-chloropropiophenone was developed using preheated Candida utilis cells immobilized in calcium alginate gel beads. Heating the immobilized cells (bead diameter 1.5 mm) at 45°C for 50 min allowed the reaction to proceed with 99.5% enantiomeric excess (ee) and an 85% yield with 1 g substrate l⁻¹ (batch addition in three aliquots) in 48 h. The immobilized cells retained approximately 50% of their original catalytic activity after being reused three times.     

Characteristics of β-lactamases and their genes (<Emphasis Type="Italic">blaA</Emphasis> and <Emphasis Type="Italic">blaB</Emphasis>) in <Emphasis Type="Italic">Yersinia intermedia</Emphasis> and <Emphasis Type="Italic">Y. frederiksenii</Emphasis>

Background  

The presence of β-lactamases in Y. enterocolitica has been reported to vary with serovars, biovars and geographical origin of the isolates. An understanding of the β-lactamases in other related species is important for an overall perception of antibiotic resistance in yersiniae. The objective of this work was to study the characteristics of β-lactamases and their genes in strains of Y. intermedia and Y. frederiksenii, isolated from clinical and non-clinical sources in India.     

Syntheses of <Emphasis Type="Italic">N</Emphasis>-vanillyl-nonanamide glycosides using amyloglucosidase from <Emphasis Type="Italic">Rhizopus</Emphasis> and β-glucosidase from sweet almond

Enzymatic syntheses of N-vanillyl-nonanamide, 1, glycosides with D-glucose, 2, D-galactose, 3, D-mannose, 4, D-ribose, 5, maltose, 6, and lactose, 7, were carried out using amyloglucosidase from Rhizopus and beta-glucosidase from sweet almond. The latter catalysed the syntheses of N-vanillyl-nonanamide glycosides (8-13) and exclusively yielded beta-glycosides with carbohydrates 2, 3, 4, 6 and 7, while amyloglucosidase yielded C1-alpha- and beta-glycosides and 6-O-aryl derivatives (8, 9, 11 and 12).     

Production of enantiomerically pure (<Emphasis Type="Italic">S</Emphasis>)-β-phenylalanine and (<Emphasis Type="Italic">R</Emphasis>)-β-phenylalanine by penicillin G acylase from <Emphasis Type="Italic">Escherichia coli</Emphasis> in aqueous medium

A new approach has been developed for the production of enantiomerically pure (S)-β-phenylalanine (S-BPA) and (R)-β-phenylalanine in aqueous medium based on enantioselective acylation and hydrolysis properties of penicillin G acylase from Escherichia coli. The acylation reaction was highly preferential for the acylation of (R)-BPA to form N-phenylacetyl-(R)-BPA using phenylacetamide as an acyl donor, which was separated and then hydrolyzed to (R)-BPA by the same enzyme at pH 7.5. The optimal acylation reaction was at pH 10, 25°C with a 2:1 molar ratio of phenylacetamide to BPA, 8 IU ml⁻¹ enzyme and 150 mM BPA. These resulted in a conversion of about 50% BPA; enantiomeric excess of (S)-BPA and (R)-BPA separated were 98 and 99%, respectively.     

Rapid induction of <Emphasis Type="Italic">Agrobacterium</Emphasis> <Emphasis Type="Italic">tumefaciens</Emphasis>-mediated transgenic roots directly from adventitious roots in <Emphasis Type="Italic">Panax</Emphasis> <Emphasis Type="Italic">ginseng</Emphasis>

Root segments from seedlings of Panax ginseng produced adventitious roots directly when cultured on 1/2 MS solid medium lacking NH₄NO₃ and containing 3.0 mg l⁻¹ IBA. Using this adventitious root formation, we developed rapid and efficient transgenic root formation directly from adventitious root segments in P. ginseng. Root segments were co-cultivated with Agrobacterium tumefaciens (GV3101) caring β-glucuronidase (GUS) gene. Putative transgenic adventitious roots were formed directly from root segments on medium with 400 mg l⁻¹ cefotaxime and 50 mg l⁻¹ kanamycin. Kanamycin resistant adventitious roots were selected and proliferated as individual lines by subculturing on medium with 300 mg l⁻¹ cefotaxime and 50 mg l⁻¹ kanamycin at two weeks subculture interval. Frequency of transient and stable expression of GUS gene was enhanced by acetosyringon (50 mg l⁻¹) treatment. Integration of transgene into the plants was confirmed by the X-gluc reaction, PCR and Southern analysis. Production of transgenic plants was achieved via somatic embryogenesis from the embryogenic callus derived from independent lines of adventitious roots. The protocol for rapid induction of transgenic adventitious roots directly from adventitious roots can be applied for a new Agrobacterium tumefaciens-mediated genetic transformation protocol in P. ginseng.     

Galacto-oligosaccharide production by a thermostable recombinant β-galactosidase from <Emphasis Type="Italic">Thermotoga maritima</Emphasis>

Summary A β-galactosidase from Thermotoga maritima produced galacto-oligosaccharides (GOS) from lactose by transgalactosylation when expressed in Escherichia coli. The enzyme activity for GOS production was maximal at pH 6.0 and 90 °C. In thermal stability experiments, the enzyme followed first-order kinetics of pH and thermal inactivation, and half-lives at pH 5.0, pH 8.0, 80 °C, and 95 °C were 27 h, 82 h, 41 h, and 14 min, respectively, suggesting that the enzyme was stable below 80 °C and in the pH range of 5.0–8.0. Mn²⁺ was the most effective divalent cation for GOS production. Cu²⁺ and EDTA inhibited more than 84% of enzyme activity. GOS production increased with increasing lactose concentrations and peaked at 500 g lactose/l. Among tested enzyme concentrations, the highest production of GOS was obtained at 1.5 units enzyme/ml. Under the optimal conditions of pH 6.0, 80 °C, 500 g lactose/l, and 1.5 units enzyme/ml, GOS production was 91 g/l for 300 min, with a GOS productivity of 18.2 g/l · h and a conversion yield of GOS to lactose of 18%.