Formation of phenylethanoid glycosides by Cistanche deserticola callus grown on solid media

The optimal growth of Cistanche deserticola callus and formation of phenylethanoid glycosides (PeG) was at 25°C with light irradiation intensity of 24 mol m^–2 s^–1 on solidified B5 media supplemented with 0.5 mg 6-benzylaminopurine l^–1, 10 mg gibberellin l^–1, 800 mg casein hydrolysate l^–1 and 20 g sucrose l^–1. After 30 d culture, the biomass reached 15.5 g dry wt callus l^–1 medium and its PEG content was 10.7% (w/w). The PeG content was 42%–127% higher than those in explants.     

Peptone,a low-cost growth-promoting nutrient for intensive animal cell culture

The effect of addition of peptone to serum-free and serum supplemented media for the growth of hybridoma cells in various systems was studied. Supplementation of defined medium with either proteose peptone or meat peptone resulted in significant increases in cell number and specific monoclonal antibody production in batch culture system. Other peptones were either inactive or less effective. In continuous culture, using medium supplemented with new born calf serum, the addition of peptone resulted in 125% and 150% increases in cell and antibody concentrations respectively. Similar increase in cell number (128%) was also obtained in spin-filter perfusion culture when medium was supplemented with peptone. By comparison, the substitution of a defined 1xMEM amino acids mixture resulted in only a 50% increase. At higher perfusion rates the cell number maintained in steady state using peptone supplement could be increased to 1.3×10⁷ cells ml^–1 while the serum concentration was reduced from 5% to 1% at a perfusion rate of 2.5 volumes per day.     

Effects of tissue culture conditions and explant characteristics on direct somatic embryogenesis in Oncidium `Gower Ramsey'

The effects of tissue culture conditions and explant characteristics on direct somatic embryogenesis were studied on Oncidium `Gower Ramsey'. Embryo formation was significantly affected by explant position. Leaf tip segments had a significantly higher embryogenic response than other segments of leaves. Adaxial-side-up orientation significantly promoted embryogenesis in comparison with abaxial-side-up orientation. There was no significant effect of sucrose in a range of concentrations (10–60 g l^–1). Modified 1/2-MS medium (containing 85 mg l^–1 KH₂PO₄) supplemented with 170 mg l^–1 NaH₂PO₄ significantly promoted direct somatic embryogenesis. Peptone at 0.5 mg l^–1 gave significantly higher emrbyogenic response (80%) on leaf tips than control treatment (50%). The best response on direct embryo formation was obtained on the modified 1/2-MS medium supplemented with 10–20 g l^–1 sucrose, 170 mg l^–1 NaH₂PO₄ and 0.5 g l^–1 peptone.     

Biotransformation of 10-deoxoartemisinin to its 7β-hydroxy derivative by Mucor ramannianus

10-Deoxoartemisinin at 0.2 mg ml^–1 medium was transformed to 7-hydroxy deoxoartemisinin by Mucor ramannianus growing on sucrose, 20 g l^–1, and peptone, 10 g l^–1, at pH 4 and 26 °C. The yield of product was increased from 16% to 45% by selecting optimal culture conditions using a 2^5–2 factorial design.     

Synthesis of recombinant human interleukin-2 via controlled feed of lactose-complex media in fed-batch cultures of Escherichia coli BL21(DE3)[pT7-G3IL2]

Using lactose as an inducer, recombinant human interleukin-2 (rhIL-2) was synthesized with an N-terminus fusion partner, G3 (three tandem-arranged glucagon peptides) in fed-batch cultures at high cell concentration (60–90 g l^–1) of Escherichia coli BL21(DE3) [pT7-G3IL2]. With batch additions of lactose (4 × 13.5 g), the fusion rhIL-2 was synthesized up to 9.3 g l^–1. However, if all the lactose (54 g) was added at once to the culture, synthesized fusion rhIL-2 decreased to 5.4 g l^–1 with a decreased cell growth rate. A statistical optimization of the production medium containing glucose, yeast extract, and lactose led to fusion rhIL-2 being produced at > 9 g l^–1.     

Production of crocin using Crocus sativus callus by two-stage culture system

Saffron callus was grown in a two-stage culture on B5 medium supplemented with casein hydrolysate (300 mg l^–1) at 22 °C in dark with naphthalene acetic acid (2 mg l^–1) and 6-benzyladenine (1 mg l^–1) to give maximum biomass (16 g dry wt l^–1), and with indole 3-acetic acid (2 mg l^–1) and 6-benzyladenine (0.5 mg l^–1) for crocin formation. The maximum crocin production (0.43 g l^–1) was achieved by this two-stage culture method, which was three times that by a one-stage method.     

In Vitro Propagation and Reintroduction of the Endangered Renanthera imschootiana Rolfe

Renanthera imschootiana Rolfe is an endangered tropical epiphytic orchid that is threatened with extinction due to over-collection and the loss of suitable habitats. In vitro propagation is a useful way to mass produce plants for re-establishment in the wild and for commercial propagation. Seeds collected 150 days after pollination (DAP) were the optimum stage for in vitro culture. Seed germination reached 93.1% on quarter-strength MS (i.e., MS containing a quarter of macro- and micronutrients) medium containing 0.5 mg l⁻¹ α-naphthaleneacetic acid (NAA), 20% coconut water (CW), 1.0 g l⁻¹ peptone, 10 g l⁻¹ sucrose and 1.0 g l⁻¹ activated charcoal (AC). Quarter-strength MS medium supplemented with 1.0 mg l⁻¹ BA, 0.5 mg l⁻¹ NAA, 1.0 g l⁻¹ peptone, 10 g l⁻¹ sucrose and 20% CW was suitable for the sub-culture of protocorm-like bodies (PLBs) in which the PLB proliferation ratio was 2.88. Quarter-strength MS medium containing 1.0 mg l⁻¹ NAA, 1.0 g l⁻¹ peptone, 100 g l⁻¹ banana homogenate (BH), and 1.0 g l⁻¹ AC was suitable for plantlet formation and 95.67% of plantlets developed from PLBs within 60 days of culture. Hyponex N016 medium supplemented with 0.5 mg l⁻¹ NAA, 1.0 g l⁻¹ peptone, 20 g l⁻¹ sucrose, 150 g l⁻¹ BH, and 1.0 g l⁻¹ AC was suitable for the in vitro growth of plantlets about 2-cm in height. Plantlets 3-cm in height or taller were transplanted to Chilean sphagnum moss, and 95% of plantlets survived after 60 days in a greenhouse. Three hundred transplanted of seedlings 360-days old were reintroduced into three natural habitats. Highest percentage survival (79.67%) was observed in Yuanjiang Nature Reserve two years after reintroduction, followed by Huolu Mountain forest park (71.33%). This protocol is an efficient means for the large-scale propagation and in vitro and in vivo germplasm conservation of R. imschootiana.     

Poly(3-hydroxybutyrate) synthesis in fed-batch culture of Ralstonia eutropha with phosphate limitation under different glucose concentrations

Poly(3-hydroxybutyrate) (PHB) was produced by fed-batch cultures of Ralstonia eutropha with phosphate limitation under different glucose concentrations. When glucose was kept at 2.5 g l^–1, cell growth and PHB synthesis were limited due to the shortage of carbon source but a higher PHB content occurred in the cell-growth stage. This shows that a low glucose concentration is favorable for PHB accumulation in R. eutropha. PHB obtained with glucose at 9 g l^–1 is 1.6 times that obtained with 40 g l^–1. When glucose was in the range of 9 to 40 g l^–1, PHB concentration and productivity decreased significantly with the increase of glucose concentration. The highest PHB productivity was obtained with glucose at 9 g l^–1.     

Stimulation of murine granulocyte macrophage-colony stimulating factor production by Pluronic F-68 and polyethylene glycol in transgenic Nicotiana tabacum cell culture

Pluronic F-68, PEG 8000, or PEG 20 000 added to cell suspension cultures of transgenic Nicotiana tabacum promoted cell growth and the production of the recombinant murine granulocyte macrophage-colony stimulating factor (mGM-CSF) in a 5-l stirred tank bioreactor. The specific growth rates were enhanced from 0.27 d^–1 to 0.47 d^–1, 0.37 d^–1 and 0.4 d^–1 when Pluronic F-68, PEG 8000, or PEG 20 000 was added, respectively. The maximum cell density was also increased most to 13.6 g l^–1 when Pluronic F-68 was added (11.3 g l^–1 in the control culture). In terms of mGM-CSF production, PEG 8000 gave the greatest stimulation and with 2 g PEG 8000 l^–1, mGM-CSF increased from 1.6 to 6.6 ng ml^–1.     

Glucose repression of xylitol production in Candida tropicalis mixed-sugar fermentations

Glucose repressed xylose utilization inCandida tropicalis pre-grown on xylose until glucose reached approximately 0–5 g l^–1. In fermentations consisting of xylose (93 g l^–1) and glucose (47 g l^–1), xylitol was produced with a yield of 0.65 g g^–1 and a specific rate of 0.09 g g^–1 h^–1, and high concentrations of ethanol were also produced (25 g l^–1). If the initial glucose was decreased to 8 g l^–1, the xylitol yield (0.79 g g^–1) and specific rate (0.24 g g^–1 h^–1) increased with little ethanol formation (<5 g l^–1). To minimize glucose repression, batch fermentations were performed using an aerobic, glucose growth phase followed by xylitol production. Xylitol was produced under O₂ limited and anaerobic conditions, but the specific production rate was higher under O₂ limited conditions (0.1–0.4 vs. 0.03 g g^–1 h^–1). On-line analysis of the respiratory quotient defined the time of xylose reductase induction.     

Isolation and study of two strains ofLeptospirillum-like bacteria from a natural mixed population cultured on a cobaltiferous pyrite substrate

Two strains ofLeptospirillum-like bacteria, L6 and L8, have been isolated from a mixed inoculum, also containingThiobacillus ferrooxidans andT. thiooxidans, cultured for one year with a colbaltiferous pyrite as energy substrate in a 100 I continuous bioleaching laboratory unit. Several physiological properties of the strains are described. The vibrio-shaped microorganisms grew at pH values lower than 1.3. Their growth rate was maximum between 2.5 and 8.0 g l¹ ferrous iron. The optimal growth temperature was 37.5° C. Ferric iron had a stimulative effect on bacterial development up to 8 g l^–1, and growth was as rapid at 14 g l^–1 ferric iron as at 8 g l^–1. The negative influence of cobalt on the final cell concentration was observed at 0.5 g l^–1, but the growth rate was not affected up to 2 g l^–1. The G + C content of strains L8 is 55.6 mol%.     

Establishment of Orthosiphon stamineus Cell Suspension Culture for Cell Growth

Callus of Orthosiphon stamineus could be induced successfully from petiole, leaf and stem tissues but not roots when cultured on MS medium containing different concentration of NAA (0–4.0 mg l^–1) and 2,4-D (0–2.0 mg l^–1). Highest fresh weight callus production was obtained from leaf explants and those with best friability were obtained on MS medium plus 1.0 mg l^–1 2,4-D plus 1.0 mg l^–1 NAA. Cell suspension cultures were established from these cultures. The appropriate cell inoculum size for the best cell growth was 0.75 g of cells in 20 ml culture medium. Cell suspension culture using MS medium supplemented with 1.0 mg l^–1 2,4-D promoted the best cell growth with maximum biomass of 8.609 g fresh weight and 0.309 g dry weight 24 days after inoculation. Cells that grew in MS medium supplemented with 1.0 mg l^–1 2,4-D reached the stationary growth phase in 15 days as compared to the cells that grew in MS medium supplemented with 1.0 mg l^–1 2,4-D + 1.0 mg l^–1 NAA reached the stationary phase in 24 days. MS medium supplemented with 1.0 mg l^–1 2,4-D was considered as the maintenance medium for maintaining the optimum cell growth of O. stamineus in the cell suspension cultures with 2-week interval subculture.     

L-Sorbose production in a continuous fermenter with and without cell recycle

The kinetics of continuous l-sorbose fermentation using Acetobacter suboxydans with and without cell recycle (100%) were investigated at dilution rates (D) of 0.05, 0.10, 0.15 and 0.3 h^–1. The biomass and sorbose concentrations for continuous fermentation without recycle increased as the dilution rate was increased from 0.05 to 0.10 h^–1. A maximum biomass concentration of 8.44 g l^–1 and sorbose concentration of 176.90 g l^–1 were obtained at D=0.10 h^–1. The specific rate of sorbose production and volumetric sorbose productivity at this dilution rate were 2.09 g g^–1 h^–1 and 17.69 g l^–1 h^–1. However, on further increasing the dilution rate to 0.3 h^–1, both biomass and sorbose concentrations decreased to 2.93 and 73.20 g l^–1 respectively, mainly due to washout of the reactor contents. However, the specific rate of sorbose formation and volumetric sorbose productivity at this dilution rate increased to 7.49 g g^–1 h^–1 and 21.96 g l^–1 h^–1 respectively. Continuous fermentation with 100% cell recycle served to further enhance the concentration of biomass and sorbose to 28.27 and 184.32 g l^–1 respectively (in the reactor at a dilution rate of 0.05 h^–1). Even though, there was a decline in the biomass and sorbose concentrations to 6.8 and 83.40 g l^–1 at a dilution rate of 0.3 h^–1, the specific rates of sorbose formation and volumetric sorbose productivity increased to 3.67 g g^–1h^–1 and 25.02 g l^–1 h^–1.     

Improved isolated microspore culture efficiency in medium with maltose and optimized growth regulator combination in japonica rice (Oryza sativa)

The influence of maltose and growth regulators on microspore culture response was investigated in japonica rice. High frequency of callus induction of isolated microspores was obtained with liquid medium containing MS salts, 100 mg l^–1 myo-inositol, 1 mg l^–1 thiamine-HCl, 500 mg l^–1 glutamine, 60 g l^–1 maltose, and several growth regulators. The effect of maltose on promoting callus formation was associated with keeping a high proportion of swollen microspores after 5 day preculture and increasing the microspore division rate on the 3rd day after culture initiation. No significant effect of maltose in place of sucrose on plantlet regeneration was seen in regeneration medium. Among the growth regulators tested, the combination of auxin 2,4-dichlorophenoxyacetic acid (1 mg l^–1), naphthaleneacetic acid (1 mg l^–1), and cytokinin (6-benzyl-aminopurine 1 mg l^–1) in the medium proved to be much better for callus formation than in the other media, and the percentage of callusing microspores of that medium reached 0.86%. Indole-3-acetic acid (0.5 mg l^–1) and kinetin (2 mg l^–1) in regeneration medium were beneficial for green plantlet differentiation. The results also showed that the frequencies of microspores initial division, callus formation and green plant regeneration varied among genotypes no matter what kind of growth regulator and sugar were used. Xiushui 117 was the best variety for callusing followed by 02428 & Taipei 309. Taipei 309 showed a good ability for green plantlet regeneration.Abbreviations 2,4-d 2,4-dichlorophenoxyacetic acid - NAA naphthaleneacetic acid - 6-BA 6-benzylaminopurine - KT kinetin - IAA indole-3 acetic acid     

Evaluation of succinic acid continuous and repeat-batch biofilm fermentation by <Emphasis Type="Italic">Actinobacillus succinogenes</Emphasis> using plastic composite support bioreactors

Continuous and repeat-batch biofilm fermentations using Actinobacillus succinogenes were performed with immobilized and suspended-cell systems. For the immobilized continuous system, plastic composite supports (PCS) containing 50% (w/w) polypropylene (PP), 35% (w/w) ground soybean hulls, 5% (w/w) dried bovine albumin, 2.5% (w/w) soybean flour, 2.5% (w/w) yeast extract, 2.5% (w/w) dried red blood cells, and 2.5% (w/w) peptone, or PP tubes (8.5 cm in length) were arranged around the agitator shaft in a grid formation. Agitation was controlled at 125 rpm and 150 rpm. Samples were taken at dilution rates of 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 h^–1 and analyzed for succinic acid production and glucose consumption (g l^–1). For PCS bioreactors, the highest final succinic acid concentrations (10.1 g ^–1, 10.4 g l^–1) and percentage yields (62.6%, 71.6%) occurred at the dilution rate of 0.2 h^–1. PCS disks were evaluated in a repeat-batch biofilm reactor. Suspended-cell batch fermentations were performed in flasks and a repeat-batch bioreactor. The maximum concentration of succinic acid produced was 40 g l^–1. Peak succinic acid percentage yields in continuous and repeat-batch fermentations of A. succinogenes were observed in suspended-cell continuous fermentations at a dilution rate of 1.0 h^–1 (76.2%) and in PCS repeat-batch fermentations with an initial glucose concentration of 40 g l^–1 (86.7%).     

Phytase production by high cell density culture of recombinant Bacillus subtilis

Bacillus subtilis BD170, harboring a plasmid pGT44[phyC] carrying the phytase gene (phyC) and a phosphate-depletion inducible pst-promoter, was grown in a 2 l bioreactor. Using a controlled feeding of glucose, high cell densities of 32 and 56 g dry cell weight l^–1 were achieved with peptone and yeast extract, respectively, as the complex nitrogen sources in a semi-defined growth medium. The fed-batch protocol was applied to production of recombinant phytase and a high extracellular phytase activity (48 U ml^–1) was reached with peptone. Although the yeast extract feeding resulted in a higher cell density, it was unsuitable as a medium component for phytase expression due to its relatively high phosphate content.     

Anaerobic fermentation of Salmonella typhimurium with and without pyruvate carboxylase

A plasmid that expressed pyruvate carboxylase (PYC) from Rhizobium etli was introduced into Salmonella typhimurium LT2. Anaerobic fermentations of S. typhimurium with and without PYC were compared with glucose as a carbon source. The presence of PYC increased the succinate yield from glucose from 0.044 g g^–1 to 0.22 g g^–1, while the lactate yield decreased from 0.31 g g^–1 to 0.16 g g^–1. Metabolic flux calculations during the early growth phase indicate that under these growth conditions in the presence of PYC more carbon flows to oxaloacetate via pyruvate carboxylase than via phosphoenolpyruvate carboxylase. Also, under these growth and induction conditions, the presence of PYC diminished the cell growth rate from 0.34 h^–1 to 0.28 h^–1, the specific rate of ATP formation from 45 mmol l^–1 h^–1 to 27 mmol l^–1 h^–1, and the specific rate of glucose consumption from 17 mmol l^–1 h^–1 to 10 mmol l^–1 h^–1.     

Characteristics of mixotrophic growth of Synechocystis sp. in an enclosed photobioreactor

Synechocystis sp. PCC 6803 was grown in a 2.5 l enclosed photobioreactor on medium with or without glucose. The incident light intensities ranged from 1.5 klux to 7 klux. The highest average specific growth rates of mixotrophic culture and photoautotrophic culture were, respectively, 1.3 h^–1 at a light intensity of 7 klux on 3.2 g l^–1 glucose and 0.3 h^–1 at both light intensities of 5 klux and 7 klux. The highest cell density 2.5 g l ^–1 was obtained at both of light intensities 5 klux and 7 klux on 3.2 g glucose l^–1. Glucose consumption decreased with decreasing light intensity. The energy yields of mixotrophic cultures were 4 to 6 times higher than that of photoautotrophic cultures. Light favored mixotrophic growth of Synechocystis sp. PCC 6803, especially at higher light intensities (5–7 klux).     

Preparation and testing of Sardinella protein hydrolysates as nitrogen source for extracellular lipase production by Rhizopus oryzae

Various fish protein hydrolysates (FPH) from sardinella (Sardinella aurita) were used as nitrogen sources for the production of extracellular lipase by the filamentous fungus Rhizopus oryzae. The best results were obtained with defatted meat–fish protein hydrolysates (DMFPH), indicating the presence in the lipid fraction of some constituents which may repress lipase synthesis. Furthermore, it was found that the extensive hydrolysis of fish proteins resulted in a higher lipase production. The use of 40 g DMFPH l^–1 for the growth of Rhizopus oryzae in medium R1 resulted in a lipase production of 394 U ml^–1, higher than the yield obtained with standard soy peptone as nitrogen source (373 U ml^–1). The most appropriate medium for the growth and the production of lipase is composed only of 24 g DMFPH l^–1 and 10 g glucose l^–1, indicating that the strain can obtain its nitrogen and salts requirements directly from fish substrate.     

Production of 4-hydroxyfuranones in simple media by fermentation

Both 2,5-dimethyl-3(2H)-furanone (DMHF) and 2(or 5)-ethyl-5(or 2)-methyl-3(2H)-furanone (EMHF) were produced at concentrations up to 4 mg l^–1 and 20 mg l^–1 respectively by yeast fermentation of a heated mixture of a single amino acid and a single sugar added to a yeast extract/peptone/glucose (YPG) medium. About 1 mg DMHF 1^–1 was also produced from precursors in the autoclaved YPG medium but EMHF formation depended entirely on the presence of a heated ribose/amino acid mixture. Glutamate was the best precursor amino acid for both furanones. Formation of EMHF showed a positive, non-linear response to ribose/glutamate concentration from 20 to 200 mM in the heated mixture.