Optimization of culture conditions and scale-up to pilot and plant scales for coenzyme Q<Subscript>10</Subscript> production by <Emphasis Type="Italic">Agrobacterium tumefaciens</Emphasis>

This report describes the optimization of culture conditions for coenzyme Q₁₀ (CoQ₁₀) production by Agrobacterium tumefaciens KCCM 10413, an identified high-CoQ₁₀-producing strain (Kim et al., Korean patent. 10-0458818, 2002b). Among the conditions tested, the pH and the dissolved oxygen (DO) levels were the key factors affecting CoQ₁₀ production. When the pH and DO levels were controlled at 7.0 and 0–10%, respectively, a dry cell weight (DCW) of 48.4 g l⁻¹ and a CoQ₁₀ production of 320 mg l⁻¹ were obtained after 96 h of batch culture, corresponding to a specific CoQ₁₀ content of 6.61 mg g-DCW⁻¹. In a fed-batch culture of sucrose, the DCW, specific CoQ₁₀ content, and CoQ₁₀ production increased to 53.6 g l⁻¹, 8.54 mg g-DCW⁻¹, and 458 mg l⁻¹, respectively. CoQ₁₀ production was scaled up from a laboratory scale (5-l fermentor) to a pilot scale (300 l) and a plant scale (5,000 l) using the impeller tip velocity (V _tip) as a scale-up parameter. CoQ₁₀ production at the laboratory scale was similar to those at the pilot and plant scales. This is the first report of pilot- and plant-scale productions of CoQ₁₀ in A. tumefaciens.     

Scale-up fermentation of recombinant <Emphasis Type="Italic">Candida rugosa</Emphasis> lipase expressed in <Emphasis Type="Italic">Pichia pastoris</Emphasis> using the GAP promoter

The high-cell-density fermentation of Candida rugosa lipase in the constitutive Pichia pastoris expression system was scaled up from 5 to 800 l in series by optimizing the fermentation conditions at both lab scale and pilot scale. The exponential feeding combined with pH-stat strategy succeeded in small scale studies, while a two-stage fermentation strategy, which shifted at 48 h by fine tuning the culture temperature and pH, was assessed effective in pilot-scale fermentation. The two-stage strategy made an excellent balance between the expression of heterogeneous protein and the growth of host cells, controlling the fermentation at a relatively low cell growth rate for the constitutive yeast expression system to accumulate high-level product. A stable lipase activity of approximately 14,000 IU ml⁻¹ and a cell wet weight of ca. 500 g l⁻¹ at the 800-l scale were obtained. The efficient and convenient techniques suggested in this study might facilitate further scale-up for industrial lipase production.     

Improvement in Production and Quality of Gellan Gum by Sphingomonas paucimobilis Under High Dissolved Oxygen Tension Levels

The effect of agitation rate and dissolved oxygen tension (DOT) on growth and gellan production by Sphingomonas paucimobilis was studied. Higher cell growth of 5.4 g l⁻¹ was␣obtained at 700 rpm but maximum gellan (15 g l⁻¹) was produced at 500 rpm. DOT levels above 20% had no effect on cell growth but gellan yield was increased to 23 g l⁻¹ with increase in DOT level to 100%. Higher DOT levels improved the viscosity and molecular weight of the polymer with change in acetate and glycerate content of the polymer.     

Optimization of culture conditions and scale-up to plant scales for teicoplanin production by <Emphasis Type="Italic">Actinoplanes teichomyceticus</Emphasis>

This report describes the optimization of culture conditions for teicoplanin production by Actinoplanes teichomyceticus KCCM-10601, an identified high-teicoplanin-producing strain (US 2006/0134757 A1). Among the conditions tested, temperature, pH, and the dissolved oxygen tension (DOT) were key factors affecting teicoplanin production. When the temperature, pH, and DOT were controlled at 34 degrees C, 7.0 and 20-30%, respectively, a dry-cell weight of 42.8 g l(-1) and a teicoplanin production of 2.9 g l(-1) were obtained after 120 h of batch culture, corresponding to a specific teicoplanin content of 67.8 mg g-DCW(-1). Teicoplanin production was scaled-up from a laboratory scale (7-l fermenter) to a pilot scale (300 l) and a plant scale (5,000 l) using the impeller tip velocity (V tip) as a scale-up parameter. Teicoplanin production at the laboratory scale was similar to those at the pilot and plant scales. This is the highest report of pilot- and plant-scale production of teicoplanin.     

Controlling the sucrose concentration increases Coenzyme Q10 production in fed-batch culture of <Emphasis Type="Italic">Agrobacterium tumefaciens</Emphasis>

The production yield of Coenzyme Q₁₀ (CoQ₁₀) from the sucrose consumed by Agrobacterium tumefaciens KCCM 10413 decreased, and high levels of exopolysaccharide (EPS) accumulated after switching from batch culture to fed-batch culture. Therefore, we examined the effect of sucrose concentration on the fermentation profile by A. tumefaciens. In the continuous fed-batch culture with the sucrose concentration maintained constantly at 10, 20, 30, and 40 g l⁻¹, the dry cell weight (DCW), specific CoQ₁₀ content, CoQ₁₀ production, and the production yield of CoQ₁₀ from the sucrose consumed increased, whereas EPS production decreased as maintained sucrose concentration decreased. The pH-stat fed-batch culture system was adapted for CoQ₁₀ production to minimize the concentration of the carbon source and osmotic stress from sucrose. Using the pH-stat fed-batch culture system, the DCW, specific CoQ₁₀ content, CoQ₁₀ production, and the product yield of CoQ₁₀ from the sucrose consumed increased by 22.6, 13.7, 39.3, and 39.3%, respectively, whereas EPS production decreased by 30.7% compared to those of fed-batch culture in the previous report (Ha SJ, Kim SY, Seo JH, Oh DK, Lee JK, Appl Microbiol Biotechnol, 74:974–980, 2007). The pH-stat fed-batch culture system was scaled up to a pilot scale (300 l), and the CoQ₁₀ production results obtained (626.5 mg l⁻¹ of CoQ₁₀ and 9.25 mg g DCW⁻¹ of specific CoQ₁₀ content) were similar to those obtained at the laboratory scale. Thus, an efficient and highly competitive process for microbial CoQ₁₀ production is available.     

Production of Alkaline Protease with <Emphasis Type="Italic">Teredinobacter turnirae</Emphasis> in Controlled Fed-batch Fermentation

By using our previously optimized media and a fed-batch operation controlled by LabVIEW Software, the key parameter for a high production of alkaline protease using the marine bacterium, Teredinobacter turnirae, was to maintain a low concentration of C and N-sources ( < 2 g sucrose l⁻¹ and < 0.2 g NH₄C l l⁻¹) using an appropriate fed-batch culture system. A maximum protease activity of 8250 U ml⁻¹ was thus achieved.     

The effect of several factors on somatic embryogenesis and plant regeneration in protoplast cultures of <Emphasis Type="Italic">Gentiana kurroo</Emphasis> (Royle)

Protoplasts were isolated from cell suspensions derived from cotyledon and hypocotyl Gentiana kurroo (Royle). Cell walls were digested with an enzyme cocktail containing cellulase, macerozyme, driselase, hemicellulase and pectolyase in CPW solution. Protoplast viability ranged from 88 to 96%. Three techniques of culture and six media were evaluated in terms of their efficiency in producing viable cultures and regenerating whole plants. With liquid culture, cell division occurred in only a low number of the protoplasts isolated, and no plant regeneration was successful. Cell division occurred within 2 or 3 days in case of agarose solidified media. After 10 days of culture, the number of dividing cells was the highest with modified MS medium in which NH₄NO₃ was replaced with 3.0 g l⁻¹ glutamine. The best results were obtained with agarose bead cultures: plating efficiency was 68.7% and 58.1% for protoplasts isolated from cotyledon and hypocotyl derived suspensions, respectively. The results were achieved with using medium containing 0.5 mg l⁻¹ 2,4-D + 1.0 mg l⁻¹ kinetin or 2.0 mg l⁻¹ BAP + 1.0 mg l⁻¹ dicamba + 0.1 mg l⁻¹ NAA + 80 mg l⁻¹ adenine sulfate. Protocalluses transferred on the following composition of plant growth regulators: 0.5 mg l⁻¹ 2,4-D + 1.0 mg l⁻¹ kinetin or 1.0 mg l⁻¹ kinetin + 0.5 mg l⁻¹ GA₃ + 80.0 mg l⁻¹ adenine sulfate developed in embryogenic cultures. However, the best embryo production occurred with the first one. Later embryos were transferred to half-strength MS mineral salts to promote plants formation. Flow cytometry studies revealed increased amounts of DNA in about one third of the regenerants.     

Stimulation of menthol production in <Emphasis Type="Italic">Mentha piperita</Emphasis> cell culture

Plant cell culture provides an alternative means for producing secondary metabolites. In this study, experiments were carried out to study the impact of several parameters, independently and in combination, on the stimulation of menthol production in the cell suspension culture of Mentha piperita. Callus was obtained from leaf segments of in vitro grown plantlets on Murashige and Skoog (MS) medium supplemented with 0.2 mg l⁻¹of 2,4-dichlorophenoxy acetic acid to initiate cell suspension culture. This culture was maintained in half-strength MS medium supplemented with 0.2 mg l⁻¹of 2,4-dichlorophenoxy acetic acid at 15 d interval and used for further studies. Precursor feeding alone, i.e., menthone, at 35 μM concentration showed slightly improved productivity. γ-Cyclodextrin alone at 60 μM concentration and in combination with menthone feeding at 35 μM increased menthol yield up to 92 and 110 mg l⁻¹ in comparison to 77 mg l⁻¹ of control culture. Synergistic potentiation effect of menthone feeding at 35 μM and γ-cyclodextrin at 60 μM treatment followed by in situ adsorption with RP-8 also showed potential stimulation of menthol production in M. piperita cell culture. Fungal elicitor treatment showed enhanced production level up to 140.8 mg l⁻¹ in comparison to that of control. Further studies were carried out with the establishment of Agrobacterium tumefaciens (Ach5) gall-mediated calli, and consequently, cell suspension culture and results showed the significant enhancement of menthol yield up to 278 mg l⁻¹. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Effect of growth rate on the production of<Emphasis Type="SmallCaps">l</Emphasis>-proline in the fed-batch culture of<Emphasis Type="Italic">Corynebacterium acetoacidophilum</Emphasis>

Corynebacterium acetoacidophilum RYU3161 was cultivated in al-histidine-limited fed-batch culture. To investigate the effect of cell growth on thel-proline production, 5l fed-batch culture was performed using an exponential feeding rate to obtain the specific growth rates (μ) of 0.04, 0.06, 0.08, and 0.1 h⁻¹. The results show that the highest production ofl-proline was obtained at μ=0.04 h⁻¹. The specificl-proline production rate (Q_p) increased proportionally as a function of the specific growth rate, but decreased after it revealed the maximum value at μ=0.08 h⁻¹. Thus, the highest productivity ofl-proline was 1.66 g L⁻¹ h⁻¹ at μ=0.08 h⁻¹. The results show that the production of L-proline inC. acetoacidophilum RYU3161 has mixed growth-associated characteristics.     

Production and characterization of esterase and lipase from <Emphasis Type="Italic">Haloarcula marismortui</Emphasis>

The present study was conducted to investigate the capability of Haloarcula marismortui to synthesize esterases and lipases, and the effect of physicochemical conditions on the growth and the production of esterases and lipases. Finally, the effect of NaCl concentration and temperature on esterase and lipase activities was studied using intracellular crude extracts. In order to confirm the genomic prediction about the esterase and lipase synthesis, H. marismortui was cultured on a rich medium and the crude extracts (intra- or extracellular) obtained were assayed for both activities using p-nitrophenyl esters and triacylglycerides as substrates. Studies on the kinetics of growth and production of esterase and lipase of H. marismortui were performed, reaching a maximum growth rate of 0.053 h⁻¹ and maximal productions of intracellular esterase and lipase of 2.094 and 0.722 U l⁻¹ using p-nitrophenyl valerate and p-nitrophenyl laurate, respectively. Both enzymes were produced as growth-associated metabolites. The effects of temperature, pH, and NaCl concentration on the growth rate and production of enzymes were studied by using a Box–Behnken response surface design. The three response variables were significantly influenced by the physicochemical factors and an interaction effect between temperature and NaCl concentration was also evidenced. The surface response method estimated the following maximal values for growth rate and productions of esterase and lipase: 0.086 h⁻¹ (at 42.5°C, pH 7.4, and 3.6 mol l⁻¹ NaCl), 2.3 U l⁻¹ (at 50°C, pH 7.5, and 4.3 mol l⁻¹ NaCl), and 0.58 U l⁻¹ (at 50°C, pH 7.6, and 4.5 mol l⁻¹ NaCl), respectively. Esterases were active at different salt concentrations, showing two optimal activities (at 0.5 and 5 mol l⁻¹ NaCl), which suggested the presence of two different esterases. Interestingly, in the absence of salt, esterase retained 50% residual activity. Esterases and lipase activities were maximal at 45°C and inactive at 75°C. This study represents the first report evidencing the synthesis of esterase and lipase by H. marismortui.     

Effect of ethrel,chlormequat chloride and paclobutrazol on growth and pyrethrins accumulation in <Emphasis Type="Italic">Chrysanthemum cinerariaefolium</Emphasis> Vis.

Pyrethrins and flower yield of pyrethrum (Chrysanthemum cinerariaefolium Viz.) plants were determined after application of ethrel, chlormequat chloride and paclobutrazol. Ethrel at 50, 100, 250 and 500 mg l^−l produced a significant positive effect on pyrethrins level, decreased plant height, while 50 and 100 mg l^−l significantly increased fresh and dry flower yield. Chlormequat chloride at 1000 and 2000 mg l^−l and paclobutrazol (80 and 160 mg l^−l) increased pyrethrins level, single flower weight and decreased plant height and flower yield. ¹⁴C-acetate incorporation studies further substantiated positive effect of growth retardants on pyrethrins biosynthesis. The effect of growth retardants on pyrethrins seems to be mediated through its effect on biosynthesis.     

In vitro germination and development of western hemlock dwarf mistletoe

A procedure for in vitro culture of the parasitic flowering plant western hemlock dwarf mistletoe, Arceuthobium tsugense (Rosend.) G.N. Jones subsp. tsugense, is described. A factorial experiment evaluated the effects of media (Harvey's medium (HM) and modified White's medium (WM)), temperatures (15 °C and 20 °C), presence or absence of light, and plant growth regulators (the auxin 2,4-dichlorophenoxyacetic acid (2,4-D) and the cytokinin 6-benzylaminopurine (BAP) at varying concentrations (0.001 mg l⁻¹ to 1 mg l⁻¹)). Seed explants germinated in less than one week in culture and produced radicles. Optimal conditions for radicle elongation were WM at 20 °C in the presence of light and without plant growth regulators. Some of the radicles split at the tip to yield callus while others swelled to become spherical holdfasts. Holdfasts were also produced at the tips of radicles, and callus arose from split holdfasts. Factors that promoted holdfast production were Harvey's medium, light, and 2,4-D at 1 mg l⁻¹. Callus development from split radicles and split holdfasts was optimal on WM with 0.5 mg l⁻¹ 2,4-D and 1 mg l⁻¹ BAP at 20 °C in the dark. This revised version was published online in June 2006 with corrections to the Cover Date.     

Production of nisin Z using <Emphasis Type="Italic">Lactococcus lactis</Emphasis> IO-1 from hydrolyzed sago starch

A membrane bioreactor for production of nisin Z was constructed using Lactococcus lactis IO-1 in continuous culture using hydrolyzed sago starch as carbon source. A strategy used to enhance the productivity of nisin Z was to maintain the cells in a continuous growth at high cell concentration. This resulted in a volumetric productivity of nisin Z, as 50,000 IU l⁻¹ h⁻¹ using a cell concentration of 15 g l⁻¹, 30^°C, pH 5.5 and a dilution rate of 1.24 h⁻¹. Adding 10 g l⁻¹ YE and 2 g l⁻¹ polypeptone, other inducers were unnecessary to maintain production of nisin. The operating conditions of the reactor removed nisin and lactate, thus minimizing their effects which allowed the maintenance of cells in continuous exponential growth phase mode with high metabolic activity.     

Morphactin influences guggulsterone production in callus cultures of <Emphasis Type="Italic">Commiphora wightii</Emphasis>

Guggulsterone, a hypolipidemic natural agent, is produced in resin canals of the plant Commiphora wightii. In this study, the efficacy of different plant growth regulators was evaluated for optimizing its production. Morphactin was found to be effective in enhancing the accumulation of guggulsterones in callus cultures. Maximum callus growth was recorded on medium containing morphactin (0.1 mg l⁻¹) and 2iP (2.5 mg l⁻¹), whereas maximum guggulsterone production occurred when the calluses were cultured on medium containing 0.1 mg l⁻¹ morphactin and 1.0 mg l⁻¹ 2iP. Morphactin and 2iP interacted significantly to enhance the callus growth and guggulsterone production by about 8-folds in one-year-old cultures. However, the effect of morphactin on callus growth and guggulsterone production was not uniform over the levels of 2iP tested. Such an effect of morphactin has never been reported on the production of secondary metabolites.     

Long-term production of soluble human Fas ligand through immobilization of <Emphasis Type="Italic">Dictyostelium discoideum</Emphasis> in a fibrous bed bioreactor

The production of recombinant glycoproteins in Dictyostelium discoideum by conventional cell culture methods was limited by low cell density as well as low growth rate. In this work, cotton towel with a good adsorption capability for D. discoideum cells was used as the immobilization matrix in an external fibrous bed bioreactor (FBB) system. With batch cultures in the FBB, the concentration of immobilized cells in the cotton fiber carrier increased to 1.37 × 10⁸ cells per milliliter after 110-h cultivation, which was about tenfold higher than the maximal cell density in the conventional free-cell culture. Correspondingly, a high concentration of soluble human Fas ligand (hFasL; 173.7 μg l⁻¹) was achieved with a high productivity (23 μg l⁻¹ h⁻¹). The FBB system also maintained a high density of viable cells for hFasL production during repeated-batch cultures, achieving a productivity of 9∼10 μg l⁻¹ h⁻¹ in all three batches studied during 15 days. The repeated-batch culture using immobilized cells of D. discoideum in the FBB system thus provides a good method for long-term and high-level production of hFasL.     

Prospects of using marine actinobacteria as probiotics in aquaculture

In the present study, optimum culture conditions for the production of extracellular polysaccharides (EPS) in submerged culture of an edible mushroom, Laetiporus sulphureus var. miniatus and their stimulatory effects on insulinoma cell (RINm5F) proliferation and insulin secretion were investigated. The maximum mycelial growth (4.1 g l⁻¹) and EPS production (0.6 g l⁻¹) in submerged flask culture were achieved in a medium containing 30 g l⁻¹ maltose, 2 g l⁻¹ soy peptone, and 2 mM MnSO₄·5H₂O at an initial pH 2.0 and temperature 25°C. In the stirred-tank fermenter under optimized medium, the concentrations of mycelial biomass and EPS reached a maximum level of 8.1 and 3.9 g l⁻¹, respectively. Interestingly, supplementation of deep sea water (DSW) into the culture medium significantly increased both mycelial biomass and EPS production by 4- and 6.7-fold at 70% (v/v) DSW medium, respectively. The EPS were proved to be glucose-rich polysaccharides and were able to increase proliferation and insulin secretary function of rat insulinoma RINm5F cells, in a dose-dependent manner. In addition, EPS also strikingly reduced the streptozotocin-induced apoptosis in RINm5F cells indicating the mode of the cytoprotective role of EPS on RINm5F cells.     

Optimization of nutrient components for enhanced phenazine-1-carboxylic acid production by <Emphasis Type="Italic">gacA</Emphasis>-inactivated <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. M18G using response surface method

The nutritional requirements for phenazine-1-carboxylic acid (PCA) production using Pseudomonas sp. M18G, a gacA chromosomal-inactivated mutant of the strain M18, with a high PCA yield, were optimized statistically in shake flask experiments. Based on a single-factor experiment design, we implemented the two-level Plackett–Burman (PB) design with 11 variables to screen medium components that significantly influence PCA production. Soybean meal, glucose, soy peptone, and ethanol were identified as the most important significant factors (P < 0.05). Response surface methodology based on the Center Composite Design (CCD) was applied to determine these factors’ optimal levels and their mutual interactions between components for PCA production. The predicted results showed that 1.89 g l⁻¹ of PCA production was obtained after a 60-h fermentation period, with optimal concentrations of soybean meal powder (33.4 g l⁻¹), glucose (12.7 g l⁻¹), soy peptone (10.9 g l⁻¹), and ethanol (13.8 ml l⁻¹) in the flask fermentations. The validity of the model developed was verified, and the optimum medium led to a maximum PCA concentration of 2.0 g l⁻¹, a nearly threefold increase compared to that in the basal medium. Furthermore, the experiment was scaled up in the 10 l fermentor and 2 g l⁻¹ PCA productions were achieved in 48 h based on optimization mediums which further verified the practicability of this optimum strategy.     

Biological acidification during grape must fermentation using mixed cultures of <Emphasis Type="Italic">Kluyveromyces thermotolerans</Emphasis> and <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Four mixed culture fermentations of grape must were carried out with Kluyveromyces thermotolerans strain TH941 and Saccharomyces cerevisiae strain SCM952. In the first culture, both yeasts were added together, whereas in the remaining three cultures S. cerevisiae was added 1, 2, and 3 days after the inoculation of K. thermotolerans. The growth and survival of the K. thermotolerans strain and the amount of the produced l-lactic acid depend on the time of inoculation of the S. cerevisiae strain and provided an effective acidification during alcoholic fermentation. The four cultures contained, respectively, at the end of fermentation 0.18, 1.80, 4.28, and 5.13 g l-lactic acid l⁻¹. The grape must with an initial pH of 3.50 was effectively acidified (70% increase in titratable acidity, 0.30 pH unit decrease) by the production of 5.13 g l-lactic acid l⁻¹.     

Synergistic effect of morphactin on cytokinin-induced production of isoflavonoids in cell cultures of Pueraria tuberosa (Roxb. ex. Willd.) DC

Isoflavonoids, the functional molecules of Fabaceae, are under clinical trials against cancer, osteoporosis and cardiovascular diseases. In this study, the efficacy of different plant growth regulators was evaluated for optimizing the production of isoflavonoids in Pueraria tuberosa. The cultures were maintained in Murashige and Skoog’s medium containing 0.1 mg l⁻¹ 2,4,5-trichlorophenoxyacetic acid (2,4,5-T) and 0.1 mg l⁻¹ kinetin. The addition of 5.0 mg l⁻¹ N⁶-(2-Isopentenyl) adenine (2iP) resulted in about ∼32-folds increase in production of isoflavonoids, while about ∼23-folds increase was recorded in the absence of kinetin in the maintenance medium. A maximum yield of isoflavonoids (∼80 mg l⁻¹; 82-folds increase) was obtained in cultures grown at 0.1 mg l⁻¹ morphactin and 5.0 mg l⁻¹ of 2iP. However, 2,4,5-T in combination with 2iP was ineffective for their production. Among different plant growth regulators tested, maximum yields of puerarin, genistin, daidzein and genistein were 17.4, 15.9, 69.0 and 0.04 mg l⁻¹, respectively. The study suggested that the presence of two cytokinins or 2iP with morphactin in the culture medium markedly enhanced the production of isoflavonoids in P. tuberosa.     

Optimized culture conditions for the production of furanocoumarins by micropropagated shoots of Ruta graveolens

Ruta graveolens in vitro cultures are a potential source of secondary metabolites (furanocoumarins) of significant medical interest. Experiments led in our laboratory showed that micropropagated shoots were richer in furanocoumarins than any other plant material. In order to optimize the molecule production by such cultivation systems, several factors related to the culture medium were studied. Effects of medium composition on biomass growth and furanocoumarin content were analysed and optimal conditions were determined for phosphate (300 mg l⁻¹ of NaH₂PO₄), nitrate (2527 mg l⁻¹ of KNO₃), carbon source (10 g l⁻¹ of sucrose) and phytohormones (2,4-dichlorophenoxyacetic acid (2,4-D) 50 μM and benzylaminopurine (BAP) 50 μM). Ruta shoot growth and furanocoumarin production were compared for optimized and standard culture conditions. Specific medium gave better results in terms of growth (t_D equal to 6.9 days against 8.6 for standard conditions) but no significant differences appeared concerning metabolite concentrations. However, the present study opens the way to scale-up studies with bioreactor cultivation systems. This revised version was published online in June 2006 with corrections to the Cover Date.