Production of S-adenosyl- L-methionine by a mutant strain of Kluyveromyces lactis

S-Adenosyl-l-methionine (AdoMet) was produced by a mutant strain Kluyveromyces lactis AM-65 grown on whey. A full factorial design method of three factors – (NH₄)₂SO₄ (factor x ₁), corn steep liquor (factor x ₂) and l-methionine (factor x ₃) on three levels – was used to determine the optimal medium conditions for the production of AdoMet. A time course shake-flask experiment in optimal whey medium (x ₁=3.1 g l^–1, x ₂=12.7 g l^–1, x ₃=4.6 g l^–1) was also carried out and the results confirmed the results of the factorial design and subsequent quadratic modelling and optimization of AdoMet production which reached 90 mg g^–1 cell dry wt.     

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.     

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.     

Selective production of bikaverin in a fluidized bioreactor with immobilized Gibberella fujikuroi

The best culture medium composition for the production of bikaverin by Gibberella fujikuroi in shake-flasks, i.e. 100 g glucose l^–1; 1 g NH₄Cl l^–1; 2 g rice flour l^–1; 5 g KH₂PO₄ l^–1 and 2.5 g MgSO₄ l^–1, was obtained through a fractional factorial design and then scaled-up to a fluidized bioreactor. The effects of carbon and nitrogen concentrations, inoculum size, aeration, flow rate and bead sizes on batch bikaverin production using immobilized G. fujikuroi in a fluidized bioreactor were determined by an orthogonal experimental design. Concentrations of up to 6.83 g bikaverin l^–1 were obtained when the medium contained 100 g glucose l^–1 and 1 g NH₄Cl l^–1 with an inoculum ratio of 10% v/v, an aeration rate of 3 volumes of air per volume of medium min^–1, and a bead size of 3 mm. Based on dry weight, the bikaverin production was 30–100 times larger than found in submerged culture and approximately three times larger than reported for solid substrate fermentation.     

Mixotrophic growth ofChlorella sorokiniana in outdoor enclosed photobioreactor

Chlorella sorokiniana was cultured in heterotrophic or mixotrophic mode in outdoor enclosed tubular photobioreactor. The culture temperature was maintained at 32–35 °C. At night, theChlorella culture grew heterotrophically, and 0.1 M glucose was completely consumed. The biomass growth yield of glucose was 0.35 ± 0.001 g-biomass g-glucose^–1. During the day, the algal culture grew mixotrophically and the biomass growth yield was 0.49 g-biomass g-glucose^–1 in low density culture (initial biomass concentration, X_o = 2 g l^–1), 0.56 g-biomass g-glucose^–1 in medium density culture (X_o = 4 g l^–1) and 0.46 g-biomass g-glucose^–1 in high density culture (X_o = 7 g l^–1). The daily area productivity of the culture, with X_o = 4 g l^–1 corresponded to 127 g-biomass m^–2 d^–1 during the day and 79 g-biomass m^–2 d^–1 during the night. In all the cultures, the dissolved O₂ concentration increased in the morning, reached the maximum value at noon, and then decreased in the afternoon. The dissolved CO₂ concentration remained at 3 mBar in the morning and increased in the afternoon. Glycolate was not found to accumulate in culture medium.     

Promotion of indole alkaloid production in Catharanthus roseus cell cultures by rare earth elements

Production of the indole alkaloids, ajmalicine or catharanthine, in cell suspension cultures of Catharanthus roseus was enhanced by cerium (CeO₂ and CeCl₃), yttrium (Y₂O₃) and neodymium (NdCl₃). The yield of ajmalicine in these treated-cultures reached 51 mg l^–1 (CeO₂), 40 mg l^–1 (CeCl₃), 41 mg l^–1 (Y₂O₃) and 49 mg l^–1 (NdCl₃) while catharanthine production reached to 36 mg l^–1 (CeO₂) and 31 mg l^–1 (CeCl₃). A major portion of increased alkaloids was released into medium in these treatments. But Sm₂O₃, SmCl₃, La₂O₃, LaCl₃, complex of chromium (III)-titanium (IV) and NaSeO₄ treatments had little effect on alkaloid production of C. roseus cell cultures.     

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.     

Biooxidation of ferrous iron by immobilized Acidithiobacillus ferrooxidans in poly(vinyl alcohol) cryogel carriers

PVA-cryogels entrapping about 10⁹ cells of Acidithiobacillus ferrooxidans per ml of gel were prepared by freezing-thawing procedure, and the biooxidation of Fe²⁺ by immobilized cells was investigated in a 0.365 l packed-bed bioreactor. Fe²⁺ oxidation fits a plug-flow reaction model well. A maximum oxidation rate of 3.1 g Fe²⁺ l^–1 h^–1 was achieved at the dilution rate of 0.4 h^–1 or higher, while no obvious precipitate was determined at this time. In addition, cell-immobilized PVA-cryogels packed in bioreactor maintained their oxidative ability for more than two months under non-sterile conditions. Nomenclature: C _A0 – Concentration of Fe²⁺ in feed stream (g l^–1) C _A – Concentration of Fe^{2 +} in outlet stream (g l^{– 1}) D – Dilution rate of the packed-bed bioreactor (h^–1) F – Volumetric flow rate of iron solution (l h^–1) F _A0 – Mass flow rate of Fe²⁺ in the feed stream (g h^–1) K – Kinetic constant (l l^–1 h^–1) r _A – Oxidation rate of Fe²⁺ (g l^–1 h^–1) V – Volume of packed-bed bioreactor (l) X _A – Conversion ratio of Fe²⁺ (%)     

ε-Caprolactam-degradation by Alcaligenes faecalis for bioremediation of wastewater of a nylon-6 production plant

Alcaligenes faecalis G utilized 95–97% of 5–15 g -caprolactam l^–1 in 24–48 h over a pH range of 6–8.5 and at 23–40 °C, without complex nutrient requirement. In the absence of KH₂PO₄ and K₂HPO₄/MgSO₄ in the medium, only 7.6% and 0.2% of 10 g caprolactam l^–1 was utilized, respectively. The chemical oxygen demand (COD) of the wastewater of nylon-6 plant was mainly due to its caprolactam content. A. faecalis G decreased the caprolactam content and COD of the wastewater by 80–90% of the original in spite of the wastewater having higher caprolactam content (3600 mg l^–1) and COD (7700 mg l^–1) than those of any of the previous reports.     

A reproducible procedure for plant regeneration from seedling hypocotyl protoplasts of Vigna sublobata L.

Viable protoplasts of Vigna sublobata L. were isolated enzymatically from hypocotyls of axenic seedlings. Protoplast yields were dependent upon seedling age, with maximum yields (2.25 ± 0.35 × 10⁶ g fwt^–1) from seedlings aged 6 d. Protoplasts regenerated cell walls and underwent sustained divisions when cultured in either agarose-solidified or liquid K8P medium. The plating density affected the division frequency and plating efficiency; the division frequency (68 ±0 6.0%) was maximum at 4.0 × 10⁴ ml^–1 while plating efficiency was maximum (1.3 ± 0.1%) at 5.0 × 10⁴ ml^–1. Dividing protoplasts developed into microcalli, which produced glossy green compact nodular calli on transfer to 8.0 gl^–1 w/v agar-solidified medium containing MS salts, B5 organic components, 30 g l^–1 sucrose, NAA (0.2–0.5 mg l^–1), zeatin riboside (0.5–2.0 mg l^–1) and GA₃ (0.5–1.0 mg l^–1). These calli, after sub-culture on the same medium, produced shoot buds which underwent elongation following transfer of tissues to 6.0 g l^–1 agar-solidified B5 medium containing 30g l^–1 sucrose, IBA (0.01 mg l^–1) and BAP (1.0 mg l^–1). Elongated shoots developed roots after transfer to 8.0g l^–1 agar-solidified, hormone-free MS medium with 30 g l^–1 sucrose.Abbreviations IAA indole-3-acetic acid - IBA indole-3-butyric acid - BAP 6-benzyladenine or benzylaminopurine - B5 medium after Gamborg et al (1968) - 2,4-D 2,4-dichlorophenoxyacetic acid - GA³ gibberellic acid - 2,i-P 6-(--dimethylallylamino) purine - MS medium after Murashige and Skoog (1962) - NAA 1-naphthaleneacetic acid     

Cells of <Emphasis Type="BoldItalic">Candida utilis</Emphasis> for <Emphasis Type="BoldItalic">in vitro</Emphasis> (<Emphasis Type="BoldItalic">R</Emphasis>)-phenylacetylcarbinol production in an aqueous/octanol two-phase reactor

(R)-Phenylacetylcarbinol (PAC), a pharmaceutical precursor, was produced from benzaldehyde and pyruvate by pyruvate decarboxylase (PDC) of Candida utilis in an aqueous/organic two-phase emulsion reactor. When the partially purified enzyme in this previously established in vitro process was replaced with C. utilis cells and the temperature was increased from 4 to 21 °C, a screen of several 1-alcohols (C4–C9) confirmed the suitability of 1-octanol as the organic phase. Benzyl alcohol, the major by-product in the commercial in vivo conversion of benzaldehyde and sugar to PAC by Saccharomyces cerevisiae, was not formed. With a phase volume ratio of 1:1 and 5.6 g C. utilis l⁻¹ (PDC activity 2.5 U ml⁻¹), PAC levels of 103 g l⁻¹ in the octanol phase and 12.8 g l⁻¹ in the aqueous phase were produced in 15 h at 21 °C. In comparison to our previously published process with partially purified PDC in an aqueous/octanol emulsion at 4 °C, PAC was produced at a 4-times increased specific rate (1.54 versus 0.39 mg U⁻¹ h⁻¹) with simplified catalyst production and reduced cooling cost. Compared to traditional in vivo whole cell PAC production, the yield on benzaldehyde was 26% higher, the product concentration increased 3.9-fold (or 6.9-fold based on the organic phase), the productivity improved 3.1-fold (3.9 g l⁻¹ h⁻¹) and the catalyst was 6.9-fold more efficient (PAC/dry cell mass 10.3 g g⁻¹).*Dedicated with gratitude to Prof. Dr. Franz Lingens – “Theo”.     

Levan production using mutant strains of Zymomonas mobilis in different culture conditions

Several levan hyperproducing mutants of Zymomonas mobilis strains were selected by mutagenesis with N-methyl-N-nitro-nitrosoguanidine and caffeine. Highest levan production (41 g l^–1) was obtained with a mutant strain HL 29 in a culture medium containing 200 g sucrose l^–1 and 0.5 g (NH₄)₂SO₄ l^–1 stored at 7 °C for 29 days. This is the first report describing the levan synthesis by Z. mobilis at 7 °C.     

Reducing by-product formation in L-lactic acid fermentation by Rhizopus oryzae

During L-lactic acid fermentation by Rhizopus oryzae, increasing the phosphate level in the fermentation medium from 0.1 g l^–1 to 0.6 g l^–1 KH₂PO₄ reduced the maximal concentration of L-lactic acid and fumaric acid from 85 g l^–1 to 71 g l^–1 and from 1.36 g l^–1 to 0.18 g l^–1, respectively; and it decreased the fermentation time from 72 h to 52 h. Phosphate at 0.40 g l^–1 KH₂PO₄ was suitable for both minimizing fumaric acid accumulation and benefiting L-lactic acid production.     

Efficient production by Escherichia coli of recombinant protein using salting-out effect protecting against proteolytic degradation

To produce glucoamylase efficiently as a recombinant protein, E. coli was grown with 20 g (NH₄)₂SO₄ l^–1 which removed proteolytic activity but did not effect cell growth. Growth in M9 medium with 20 g (NH₄)₂SO₄ l^–1 produced 11 U glucoamylase ml^–1 compared to 7 U ml^–1 without addition. Furthermore, the glucoamylase activity was maintained at about 9 U ml^–1.     

Biomass production in mixotrophic culture of Euglena gracilis under acidic condition and its growth energetics

When Euglena gracilis was grown in the heterotrophic condition with glucose and (NH₄)₂SO₄ as the carbon and nitrogen source, a high cell yield (4.28–4.48 g l^–1) was obtained and the culture pH decreased to 1.6–2. The biomass production in the heterotrophic culture was compared to those in the autotrophic and mixotrophic cultures. Autotrophic growth was 4.7–6.3% of the heterotrophic one, whereas about 15–19% higher growth was obtained in the mixotrophic culture. Moreover, good production of chlorophyll (39.4 mg l^–1) and carotenoids (13.8 mg l^–1) were attained in the mixotrophic culture, giving the highest fermenter productivity with respect to biomass as well as chlorophyll and carotenoids. Through an energetic analysis in the mixotrophic culture, it was estimated about 25–28% of the total ATP requirement is formed in the photochemical reactions. This resulted in an improved biomass production in the mixotrophic culture of E. gracilis.     

In vitro production of sedative galphimine B by cell suspension cultures of Galphimia glauca

The sedative triterpene, galphimine B (1), was detected in cell suspension-batch cultures of Galphimia glauca. The effect of inoculum size, growth regulators and different concentrations of sucrose, nitrates and phosphates was evaluated. A two-stage batch process for biomass production and accumulation of compound 1 was established. Major cellular growth (15 g l^–1 dry wt) was obtained in the first stage with naphthaleneacetic acid (2 mg l^–1) + kinetin (2 mg l^–1). Adding 4 mg 2,4-dichlorophenoxyacetic l^–1 acid in the second stage resulted in the highest accumulation of 1 (0.21 mg g^–1 dry wt) which was 36% higher with respect to calluses and comparable to that obtained from wild plants.     

Plant regeneration from protoplasts isolated from embryogenic suspension cultured cells of Cinnamomum camphora L.

An efficient and reproducible protocol is described for the regeneration of Cinnamomum camphora protoplasts isolated from cultured embryogenic suspension cells. Maximum protoplast yield (13.1±2.1×10⁶/g FW) and viability (91.8±3.8%) were achieved using a mixture of 3% (w/v) cellulase Onozuka R10 and 3% (w/v) macerozyme Onozuka R10 in 12.7% (w/v) mannitol solution containing 0.12% (w/v) MES, 0.36% (w/v) CaCl₂·2H₂O, and 0.011% (w/v) NaH₂PO₄·2H₂O. First divisions occurred 7–10 days following culture initiation. The highest division frequency (24.6±2.9%) and plating efficiency (6.88±0.8%) were obtained in liquid medium (MS) supplemented with 30 g l^–1 sucrose, 0.7M glucose, 0.1 mg l^–1 NAA, 1.0 mg l^–1 BA, and 1.0 mg l^–1 GA₃. After somatic embryo induction and then shoot induction, the protoplast-derived embryos produced plantlets at an efficiency of 17.5%. Somatic embryos developed into well-rooted plants on MS medium supplemented with 1.0 mg l^–1 3-indole butyric acid (IBA). Regenerated plants that transferred to soil have normal morphology.     

Influence of inorganic microelements on the production of camptothecin with suspension cultures of <Emphasis Type="Italic">Camptotheca acuminata</Emphasis>

The effects of eight microelements (I^–, BO₃ ^3–, MoO₄ ^2–, Co²⁺, Cu²⁺, Mn²⁺, Fe²⁺, Zn²⁺) on the biosynthesis of camptothecin and the growth of suspension cultures of Camptotheca acuminata were studied. The increase of I^– to 25 M l^–1, Cu²⁺ to 1 M l^–1, Co²⁺ to 2 M l^–1 and MoO₄ ^2– to 10 M l^–1 in Murashige and Skoog (MS) medium resulted in 1.66, 2.84, 2.53 and 2.04 times higher of camptothecin yield than that in standard MS medium respectively. Combined treatment of I^– (25 M l^–1), Cu²⁺ (1 M l^–1), Co²⁺ (2 M l^–1) and MoO₄ ^2– (10 M l^–1) lead to improve cell dry weight, camptothecin content, and camptothecin yield to 30.56 g l^–1, 0.0299%, and 9.15 mg l^–1, respectively, which were 20.2, 208.9 and 273.8% increment respectively when compared with those of control.     

Culture conditions of tannase production by Lactobacillus plantarum

Lactobacillus plantarum produced an extracellular tannase after 24 h growth on minimal medium of amino acids containing 2 g tannic acid l^–1. Enzyme production (6 U ml^–1) was optimal at 37 °C and pH 6 with 2 g glucose l^–1 and 7 g tannic acid l^–1 in absence of O₂.     

Effects of activated charcoal, explant size, explant position and sucrose concentration on plant and shoot regeneration of Lilium longiflorum via young stem culture

An efficient system for the in vitro plant and shootregeneration of Lilium longiflorum was developed andaccomplished using transverse thin cell layers (tTCL) of young stems.tTCLs were cut transversely along young stems from which the shoot-tipshad been removed. Sections were measured accurately using a graded gridand were cut in 4 mm × 4 mm × 1 mm cubes, eliminatingepidermal tissue, and were cultured on one-half MS medium containing 8 gl^–1 agar, different sucrose concentrations (10, 20, 30 or 40g l^–1), and with or without 1 mg l^–1 activatedcharcoal (AC). Plants formed on the surface of tTCLs within 60 days onone-half MS medium containing 8 g l^–1 agar and 20 gl^–1 sucrose. Sections of 1 mm taken just below the apicalarea developed buds within 15 days, whereas the sections closer to thebase required about 45 days. Shoot regeneration was enhanced whensucrose concentration was used at 30 or 40 g l^–1 after 60days of culture. No root formation occurred. Both shooting and rootingoccurred when sucrose was used at 20 g l^–1. The plantletswere transferred to soil and grew well under greenhouseconditions.