Astragaloside IV and polysaccharide production by hairy roots of Astragalus membranaceus in bioreactors

Hairy roots of Astragalus membranaceus were grown in bioreactors up to 30 l for 20 d. Cultures from a 30 l airlift bioreactor gave 11.5 g l dry wt with 1.4 mg g^–1 astragaloside IV, similar to cultures from 250 ml and 1 l flasks, but greater than yields from a 10 l bioreactor (dry wt 9.4 g l^–1, astragaloside IV 0.9 mg g^–1). Polysaccharide yields were similar amongst the different bioreactors (range 25–32 mg g^–1). The active constituent content of the cells approached that of plant extracts, indicating that large scale hairy root cultures of A. membranaceus has the potential to provide an alternative to plant crops without compromising yield or pharmacological potential.     

Production of eleutherosides in in vitro regenerated embryos and plantlets of <Emphasis Type="BoldItalic">Eleutherococcus chiisanensis</Emphasis>

High frequency somatic embryogenesis of Eleutheorcoccus chiisanensis was achieved through suspension culture of embryogenic cells in hormone-free Murashige and Skoog liquid medium supplemented with 30 g sucrose l⁻¹. Cotyledonary somatic embryos were germinated and converted into plantlets using 20 μM gibberellic acid which were then grown in a 10 l airlift bioreactor. HPLC analysis revealed the accumulation of eleutheroside B, E and E1 in the embryos and plantlets. Thus mass production of embryos and plantlets of E. chiisanensis can be achieved in liquid cultures and the biomass produced may become an alternative source of eleutherosides.     

Regulatory mechanisms of biosynthesis of betacyanin and anthocyanin in relation to cell division activity in suspension cultures

Regulatory mechanisms of betacyanin biosynthesis in suspension cultures of Phytolacca americana and anthocyanin in Vitis sp. were investigated in relation to cell division activity.Betacyanin biosynthesis in Phytolacca cells clearly shows a positive correlation with cell division, as the peak of betacyanin accumulation was observed at the log phase of batch cultures. Incorporation of radioactivity from labelled tyrosine into betacyanin also showed a peak at early log phase. Aphidicolin, an inhibitor of DNA synthesis, and propyzamide, an antimicrotubule drug, reduced betacyanin accumulation and inhibited the incorporation of radioactivity from labelled tyrosine into betacyanin at concentrations which were inhibitory to cell division. Both inhibitors reduced the incorporation of radioactivity from labelled tyrosine to 3,4-dihydroxyphenylalanine (DOPA), but the incorporation of labelled DOPA into betacyanin was not affected. These results suggest that the conversion of tyrosine to DOPA is coupled with cell division activity.In contrast, the anthocyanin accumulation in Vitis cells showed a negative correlation with cell division. Accumulation occurred at the stationary phase in batch cultures when cell division ceased. Aphidicolin or reduced phosphate concentration induced a substantial increase in anthocyanin accumulation as well as the inhibition of cell division. Chalcone synthase (CHS) activity increased at the time of anthocyanin accumulation. Northern blotting analysis indicated that changes in CHS mRNA levels corresponded to similar changes in enzymatic activity. The pool size of endogenous phenylalanine was low during active cell division, but increased before anthocyanin began to accumulate and concomitantly with increasing levels of CHS mRNA. Exogenous supply of phenylalanine at the time of low endogenous levels induced the elevation of CHS mRNA and anthocyanin accumulation. These results indicate that the elevation of endogenous phenylalanine levels, when cell division ceases, may cause the increase in CHS mRNA levels, resulting in increased CHS activity and subsequently in anthocyanin accumulation in Vitis suspension cultures.Abbreviations CHS chalcone synthase - CHFI chalcone flavanone isomerase - DOPA 3,4-dihydroxyphenylalanine - PAL phenylalanine ammonia lyase     

Accumulation of peonidin 3-glucoside enhanced by osmotic stress in grape (Vitis vinifera L.) cell suspension

Cell cultures of grapes, Vitis vinifera L. cv Gamay Fréaux were grown under different conditions of external osmotic potential induced by an increase of sucrose concentration or by the addition of mannitol to the culture medium. Addition of 82 mM mannitol or increasing sucrose concentration to 132 mM had similar effects on repressing growth. Cyanidin 3-glucoside, peonidin 3-glucoside and peonidin 3-p-coumaroylglucoside are three main anthocyanins of Vitis cells. Increasing osmotic potential from –0.43 MPa to –0.8 MPa in the medium resulted in a significant intracellular accumulation of anthocyanin especially peonidin 3-glucoside in the pigmented cells. High osmotic potential appears to stimulate the methylation of anthocyanins. Osmotic potential is an important culture factor and may be useful in the controlling of anthocyanin production and composition.     

Improved guggulsterone production from sugars, precursors, and morphactin in cell cultures of Commiphora wightii grown in shake flasks and a bioreactor

Cell cultures of Commiphora wightii (Arnott.) Bhandari were grown in shake flasks and a bioreactor and an increase in guggulsterone accumulation up to 18 μg l⁻¹ was recorded in cells grown in the production medium containing a combination of sucrose:glucose (4% total), precursors (phenylalanine, pyruvic acid, xylose, and sodium acetate), morphactin, and 2iP. A yield of 10 g l⁻¹ biomass and ∼200 μg l⁻¹ guggulsterone was recorded in a 3-l flask and in a 2-l stirred tank bioreactor compared with 6.6 g biomass and 67 μg l⁻¹ guggulsterone in 250-ml flasks. Increased vessel size was correlated with increased biomass and guggulsterone accumulation. 2iP alone was not effective for biomass and guggulsterone accumulation in cell cultures of C. wightii.     

The formation of flavonoids in cell suspension cultures ofPrunus x yedoensis matsum

Two lines of the red and pale yellow cell suspension cultures, prepared fromPrunus x yedoensis Matsum. callus induced by Murashige and Skoog's (1962) basal medium supplemented with 2, 4-dichlorophenoxyacetic acid (2, 4-D, 1.0 mg/l), kinetin (0.1 mg/l) and sucrose (30 g/l), were maintained on Schenk and Hildebrandt medium as modified by Mitchell and Gildow (1975). The red cell suspension culture produced cyanidin 3-monoglucoside, 5, 4′-dihydroxy-7-methoxyisoflavone 4′-glucoside (prunetrin), isoquercitrin, catechin, epicatechin, and procyanidin B-1, B-2, B-3 and B-4, while the pale yellow cells produced only a small amount of catechin and epicatechin as main flavonoids. These flavonoid compounds found in the red cell culture were present also in maturePrunus leaves. Maximum growth and maximum amount of total phenol and proanthocyanidin (procyanidins) were obtained with 0.3 mg/l of both 2,4-D and kinetin. Maximum concentration of anthocyanin was also obtained with 0.3 mg/l 2, 4-D regardless of kinetin concentration. Accumulation of proanthocyanidin was markedly stimulated by low concentrations of phosphate, which reduced growth by about half, and also by high concentrations of inorganic nitrogen. Production of both anthocyanin and proanthocyanidin was reduced by lowered nitrogen levels. Cell growth and production of all phenolics were inhibited when ammonium ion replaced nitrate in the medium.     

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant <Emphasis Type="Italic">Escherichia coli arcA</Emphasis> mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the 'one-factor-at-a-time' technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett-Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box-Wilson design. Under such optimized conditions (22.02 g l(-1) glycerol, 1.78 g l(-1) CAS, and 1.83 g l(-1) inoculum) microaerobic batch cultures gave rise to 8.37 g l(-1) CDW and 3.52 g l(-1) PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l(-1). After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l(-1), respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures.     

Effects of cadmium accumulation on growth and respiration of a cadmium-sensitive strain of Bacillus subtilis and a selected cadmium resistant mutant

The effects of cadmium on the growth and respiration of two strains of Bacillus subtilis are compared to the accumulation of Cd by viable and cyanide-killed cells, protoplasts and cell fractions of the strains. Growth and respiration of strain 1A1 were significantly inhibited at 10g Cd²⁺/ml while the growth and respiration of strain 1A1R, a selected mutant of 1A1, were only slightly affected. Similarly, 1A1R protoplasts were more resistant to Cd than were 1A1 protoplasts. The differential resistance of the strains correlates with the accumulation of Cd by the two strains, with 1A1 accumulating approximately 10 times the level of Cd after a 4 h exposure to 1 g Cd²⁺/ml. The distributions of Cd throughout the cells, however, were similar between strains. Based on the accumulation of Cd by cyanide-killed protoplasts, uptake of Cd by 1A1 appears to be an active process, while for 1A1R, Cd accumulation is independent of protoplast viability.Non-standard abbreviations SMM Subtilis Minimal Medium - AAS Atomic Absorption Spectrophotometry - TSA Trypticase Soy Agar - PCA Plate Count Agar - INT 2-p-iodophenyl-3-p-nitrophenyl-5-phenyl-2H tetrazolium chloride - dd H₂O double distilled demineralized water - OD Optical Density     

Rheology and Shear Stress of Centaurea calcitrapa Cell Suspension Cultures Grown in Bioreactor

Centaurea calcitrapa suspension cultures were grown either in Erlenmeyer flasks or in a mechanically stirred bioreactor. Its rheological behaviour, when fitted to the Oswald–de Waele model (power law), showed pseudoplastic characteristics in both cases. The flow behaviour index (n) decreased over the course of a growth cycle and the consistency index (K) increased, reached a value of 1.81 N sⁿ m⁻² run on 2 l bioreactor. Bioreactor cultivation of C. calcitrapa cells at different agitation rates (30, 60, 100 and 250 rpm), highlighted the influence of shear forces on cell viability loss (90–34%) and phenol accumulation (74–140 μg l⁻¹), due to increased stirring speeds. Analysis of these results suggests that this cell line is shear-sensitive. An empirical exponential correlation was defined between apparent viscosity and biomass concentration, under the studied conditions, giving the possibility to estimate the prevailing broth regime and to optimize bioreactor design. Revisions requested 10 October 2005; Revisions received 19 December 2005     

Comparative analysis of mixing distribution in aerobic stirred bioreactor for simulated yeasts and fungus broths

The study on mixing distribution for an aerobic stirred bioreactor and simulated (solutions of carboxymethylcellulose sodium salt), yeasts (S. cerevisiae) and fungus (P. chrysogenum pellets and free mycelia) broths indicated the significant variation of mixing time on the bioreactor height. The experiments suggested the possibility to reach a uniform mixing in whole bulk of the real broths for a certain value of rotation speed or biomass concentration domain. For S. cerevisiae broths the optimum rotation speed increased to 500 rpm with the biomass accumulation from 40 to 150 g/l d.w. Irrespective of their morphology, for fungus cultures the existence of optimum rotation speed (500 rpm) has been recorded only for biomass concentration below 24 g/l d.w. The influence of aeration rate depends on the apparent viscosity/biomass concentration and on the impellers and sparger positions. By increasing the apparent viscosity for simulated broths, or biomass amount for real broths, the shape of the curves describing the mixing time variation is significantly changed for all the considered positions. The intensification of the aeration induced the increase of mixing time, which reached a maximum value, decreasing then, due to the flooding phenomena. This variation became more pronounced at higher viscosities for simulated broths, at higher yeasts concentration, and at lower pellets or filamentous fungus concentration, respectively. By means of the experimental data and using MATLAB software, some mathematical correlations for mixing time have been proposed for each broth and considered position inside the bioreactor. These equations offer a good agreement with the experiment, the maximum deviation being ±7.3% for S. cerevisiae broths.     

Ribonuclease production by free and immobilizedAspergillus clavatus cells

Several fungal strains ofAspergillus andPenicillium were immobilized by cryopolymerization in polyvinyl alcohol cryogel beads.Aspergillus clavatus was the best producer of extracellular ribonuclease. Enzyme productivity and growth of free and immobilized cells in shake flasks and agitated bioreactor were studied. Ribonuclease production and growth behaviour depended on concentrations of glucose, peptone and soybean in the culture medium. Enzyme production was influenced by agitation and aeration intensity. In repeated batch, shake-flask cultures, the immobilized cells showed 2 to 3.5 times higher enzyme activity than free cells. The optimal conditions in a bioreactor were at 150 rev/min agitation speed and 0.5 vol/vol.min aeration. Enzyme productivity of immobilized cells (237 units/g dry mycelium.h) was 2.1 times higher than the productivity of free cells in a bioreactor, and 2.3 times higher than that of a shake-flask culture.R.J. Manolov is with the Institute of Microbiology, Department of Enzymes, Bulgarian Academy of Sciences, Georgy Bonchev Street 26, 1113 Sofia, Bulgaria.     

The role of calcium channels in anthocyanin production in callus cultures of Daucus carota

The involvement of Ca²⁺ ATPases in anthocyanin accumulation in callus cultures of Daucus carota was investigated under the influence of calcium and calcium channel modulators. Ionophore (I) treatment enhanced callus growth and anthocyanin accumulation. Increasing the amount of calcium applied to cultures enhanced the anthocyanin level. Ionophore treatment influenced the enhancement of Ca²⁺ATPase and endogenous titres of PAs. Addition of the calcium channel blocker verapamil or the calmodulin antagonist chlorpromazine to the A23187 (ionophore) treated cells caused a reduction in anthocyanin levels. Channel blockers reduced Ca²⁺ATPase activity, which was restored by ionophore treatment, showing the importance of calcium in anthocyanin production. Higher ethylene levels were also found in treatment with ionophore or 2X calcium. Thus the influence of ionophore in anthocyanin production and its inhibition by calcium channel modulators suggests that calcium plays an important role in the production of anthocyanin by carrot callus cultures.     

Rapid and extensive vacuolation of the budding yeastsSaccharomyces cerevisiae andCandida albicans by amphotericin B

The effect of amphotericin B (AMPH) on vacuolation in the budding yeastsSaccharomyces cerevisiae andCandida albicans was studied. The minimum inhibitory concentration of AMPH for growth ofS. cerevisiae andC. albicans was 1 µg/ml. In untreated control cultures, mature cells had large central vacuoles in the exponential phase, which hampered the detection of vacuolation effect. Small buds in untreated exponential phase cells, however, only rarely showed vacuoles under the light microscope. Treatment with 0.2 µg/ml of AMPH for 20–30 min induced extensive vacuolation not only in mothers but also buds ofS. cerevisiae. Extensive vacuolation lasted 4 h or more, and growth rate of the cells was much reduced for 8 h or more. Vacuolation itself was not fatal: on removal of the drug most cells gradually recovered from vacuolation and eventually multiplied. A similar effect of AMPH was also observed inC. albicans but at a higher concentration (0.5 µg/ml).     

High cell density cultivation of <Emphasis Type="Italic">Escherichia coli</Emphasis> with surface anchored transglucosidase for use as whole-cell biocatalyst for α-arbutin synthesis

A fed-batch culture strategy for the production of recombinant Escherichia coli cells anchoring surface-displayed transglucosidase for use as a whole-cell biocatalyst for α-arbutin synthesis was developed. Lactose was used as an inducer of the recombinant protein. In fed-batch cultures, dissolved oxygen was used as the feed indicator for glucose, thus accumulation of glucose and acetate that affected the cell growth and recombinant protein production was avoided. Fed-batch fermentation with lactose induction yielded a biomass of 18 g/L, and the cells possessed very high transglucosylation activity. In the synthesis of α-arbutin by hydroquinone glucosylation, the whole-cell biocatalysts showed a specific activity of 501 nkat/g cell and produced 21 g/L of arbutin, which corresponded to 76% molar conversion. A sixfold increased productivity of whole cell biocatalysts was obtained in the fed-batch culture with lactose induction, as compared to batch culture induced by IPTG.     

Optimization of Bifidobacterium longum growth by use of calcium carbonate-alginate beads

High concentrations of ammonium and sodium ions inhibited Bifidobacterium longum growth more than a high calcium ion concentration. The optimal pH for B. longum growth was determined to be 5.0 due to the lower accumulation of ammonium ion. To reduce the accumulation of ammonium ion and obtain an enhanced growth of B. longum, the pH of the culture containing immobilized calcium carbonate beads was controlled to 5.0 with ammonia water. The concentrations of ammonium, sodium, and calcium ions in the culture were maintained at the desired level. The maximum cell mass increased to 16.8 g/l, 1.23 times higher than cultures without calcium carbonate beads. The number of viable cells in the culture increased to 5.0 × 10¹⁰, 1.67 times more than cultures without calcium carbonate beads.     

Production of steroidal alkaloids by hairy roots of Solanum aviculare and the effect of gibberellic acid

Cultures of Solanum aviculare hairy roots were established after transformation with Agrobacterium rhizogenes A4. High levels of steroidal alkaloids measured as solasodine equivalents were produced in shake-flasks and bioreactor, even though relatively low concentrations are found in roots in vivo. In shake flasks the maximum alkaloid yield was 32 mg g^-1 dry weight; in a 3-1 air-driven bioreactor the yield was 29 mg g^-1. These yields represent a 5-fold increase over previous reports for in vitro production, and are comparable with levels found in the aerial parts of intact S. aviculare plants. Production of steroidal alkaloids was growth-associated. High sugar levels at stationary phase and insensitivity to increased levels of medium components suggest that root cultures were limited by oxygen mass-transfer. In Petri-dish culture with and without exogenous gibberellic acid, root length and number of root tips increased exponentially; growth proceeded with a constant length per root tip of about 35 mm. Addition of gibberellic acid enhanced growth but reduced the specific steroidal-alkaloid level. Taking into account both growth and alkaloid yield, accumulation of steroidal alkaloids was improved by about 40% at gibberellic-acid concentrations of 10 and 100 g l^-1.     

Phytotoxic activity of selected water-soluble metabolites of Fusarium against Lemna minor L. (Duckweed)

Phytotoxicity and inhibitory effects of the fusarial toxins fumonisin B₁ (FB₁) [m.p. 103–105 °C], fusaric acid [m.p. 106–107 °C], butenolide (4-acetamido-4-hydroxy-2-butenoic acid lactone) [116–117 °C], 9, 10-dihydroxyfusaric acid [m.p. 150–155 ° C], and moniliformin on chlorophyll synthesis in the aquatic macrophyte Lemna minor (duckweed) were examined. FB₁ proved to be most active, reducing the growth of L. minor fronds and their ability to synthesize chlorophyll by 53% and 59%, respectively, at 0.7 g/ml. The growth rate of L. minor was reduced 59% by 6.7 g/ml fusaric acid, 62% by 66.7 g/ml butenolide, and 22% by 66.7 g/ml 9,10-dihydroxyfusaric acid. Moniliformin was the least phytotoxic to L. minor, with only a 16% suppression of growth rate and a 54% reduction in chlorophyll at 66.7 g/ml.The mention of firm names or trade products does not imply that they are endorsed or recommended by the US Department of Agriculture over other firms or similar products not mentioned.     

High solids fermentation of hydrolysates of wheat starch B in a continuous dynamic immobilized biocatalyst bioreactor

Summary A simple and efficient method of conversion of wheat starch B to ethanol was investigated. Employing a two-stage enzymatic saccharification process, 95% of the wheat starch was converted to fermentable sugars in 40 h. From 140 g/l total sugars in the feed solution, 63.6 g/l ethanol was produced continuously with a residence time of 3.3 h in a continuous dynamic immobilized biocatalyst bioreactor by immobilized cells ofSaccharomyces cerevisiae. The advantages and the application of this bioreactor to continuous alcoholic fermentation of industrial substrates are presented.     

Role of oxygen in the utilization of phenol by Pseudomonas CF600 in continuous culture

The dissolved oxygen (DO) level is the key factor which decides the rate of degradation of the organic load in aerobic growth conditions. In this study the role of DO levels on the utilization of phenols has been reported using the continuous culture system. A phenol-utilizing strain, Pseudomonas CF600 has been used as a model. Its phenol-degrading capacity was studied using continuous cultivation for a period of 60 days. The bioreactor was kept at a dilution rate of 0.006 h^–1 with DO levels maintained at 2, 3, and 4 ppm keeping all the other cultivation conditions constant. Physiological variations under the cultivation conditions were studied by monitoring off-line phenol utilization and respirometric analysis of harvested culture against different substrates. It was observed that the accumulation of 2-hydroxymuconate semialdehyde (HMS), an intermediate in the phenol degradation pathway, depends on the DO level. The maximum level of HMS in the medium observed was 3.92 M when DO was maintained at 2 ppm whereas with 3 ppm of DO, HMS level was below 0.4 M. Oxygen uptake data of the cells harvested from cultures grown at different DO levels showed that the uptake was highest at 3 ppm DO for all the substrates tried. When phenol was used as substrate, the oxygen uptake rate was 42.66, 66.36 and 35.55 nM/min/mg dry weight of cells at 4, 3 and 2 ppm DO respectively. Results show that DO levels influence the rate of phenol utilization in Pseudomonas CF600.     

Taxane Production in Suspension Culture of <Emphasis Type="Italic">Taxus</Emphasis> × <Emphasis Type="Italic">Media</Emphasis> var. <Emphasis Type="Italic">Hicksii</Emphasis> Carried Out in Flasks and Bioreactor

Paclitaxel and 10-deacetylbaccatin III (10-DAB III) were produced in suspension cultures of Taxus × media var. Hicksii grown in shake-flasks and in a 7-l bioreactor reaching, in the bioreactor, 4.4 mg l⁻¹ (on day 14) and 37.5 mg l⁻¹ (on day 11). In shake-flasks the highest total content of paclitaxel and 10-DAB III was 7.3 mg l⁻¹ (on day 4) and 8.8 mg l⁻¹ (on day 18). Phenylalanine, at 0.05 mM, increased paclitaxel accumulation in cells cultivated in bioreactor and flasks 30-fold and 9-fold (from 0.02 mg l⁻¹ to 0.6 mg l⁻¹ and to 0.2 mg l⁻¹, respectively). The 10-DAB III content in cells from flasks was increased from 0.4 mg l⁻¹ to 1.6 mg l⁻¹.