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.     

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.     

Production of cyclohexanone monooxygenase from Acinetobacter calcoaceticus for large scale Baeyer–Villiger monooxygenase reactions

Cyclohexanone monooxygenase was produced from Acinetobacter calcoaceticus grown on a medium containing both glutamate (30 g l^–1) and cyclohexanol (1 g l^–1). Productivity was increased to 650 U l^–1, an order of magnitude greater than previous production methods, thereby enhancing the potential commercial utility of this enzyme.     

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.     

A novel thermotolerant methylotrophicBacillus sp. and its potential for use in single-cell protein production

A thermotolerant methylotrophicBacillus sp. (KISRI TM1A, NCIMB 40040), isolated from the Kuwaiti environment and belonging to the group II spore-forming, bacilli, could not be correlated with any knownBacillus sp. It may, therefore, be a new species. It grew at temperatures from 37° to 58°C from pH 6.5 to 9.0 and on methanol up to 40 g l^–1. It grew well in a chemostat. Its biomass yield coefficient was improved by about 30% by optimization of medium and growth conditions, reaching a maximum of 0.44g g^–1 at 45°C pH 6.8 to 7.0, dilution rate 0.25 h^–1 with methanol at 10 g l^–1. Average crude protein and amino acid content were 84% and 60%, respectively, and maximum productivity attained under laboratory conditions was 5.06 g l^–1h^–1. It was concluded that this strain has good potential for use in single-cell protein production.     

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.     

Glycerol production by Candida krusei employing NaCl as an osmoregulator in batch and continuous fermentations

Addition of 40 g NaCl l^–1 to a chemically defined medium containing 140 g glucose l^–1 in shake-flask culture improved glycerol production by Candida krusei from 16.5 g l^–1 to 47.7 g l^–1. With 40 g NaCl l^–1 at a dilution rate of 0.065 h^–1, glycerol concentration, glycerol yield (based on glucose consumed), and productivity in a four-stage cascade bioreactor were higher by 240%, 27% and 28%, respectively, than in a single-stage continuous culture system.     

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.     

Optimization of thermostable lipase production from a thermophilic Geobacillus sp. using Box-Behnken experimental design

Thermostable lipase production by Geobacillus thermoleovorans was optimized in shake-flask cultures using Box-Behnken experimental design. An empirical model was developed through response surface methodology to describe the relationship between tested variables (Tween 80, olive oil, temperature and pH) and enzyme activity. Maximum enzyme activity (495 U l^–1) was attained with Tween 80 at 5 g l^–1; olive oil at 60 g l^–1; 70 °C and pH 9. Experimental verification of the model showed a validation of 95%, which is more than 4-fold increase compared to the basal medium.     

Induced Activity of Superoxide Dismutase and Peroxidase of in vitro Plants by Low Concentrations of Ethanol

A rapid micropropagation protocol was established for Aloe vera L. var. chinensis (Haw.) Berger, Chinese Aloe. The effects of three factors, namely BA, NAA and sucrose, on bud initiation were evaluated by L₉ (3⁴) orthogonal design. The variance analysis of the experimental results showed that the actions of the three factors were all considerable. Among the three factors, sucrose was the most important for bud initiation followed by BA, and NAA had the weakest effect. The best medium for bud initiation was semi-solid MS supplemented with 2.0 mg l^–1 BA, 0.3 mg l^–1 NAA, 30 g l^–1 sucrose and 0.6 g l^–1 PVP (pH 5.8), on which Chinese aloe could multiply 15 times in 4 weeks. Some shoots rooted spontaneously on 1/2 strength MS medium, but the rooting percentage was improved in the presence of 0.2 mg l^–1 NAA. Rooted plantlets were acclimatized to greenhouse conditions. The young plantlets from tissue culture were transplanted successfully. In vitro propagation can be a useful tool in the conservation of this endangered medicinal species.     

Evaluation of the potential of Aspergillus niger species for the bioconversion of L-phenylalanine into 2-phenylethanol

Aspergillus niger was explored, for the first time, for the production of 2-phenylethanol (a rose-like aroma) using L-phenylalanine as precursor. Among the strains screened, A. niger CMICC 298302 was shown to produce, in a culture medium containing 6 g L-phenylalanine l^–1 and 60 g glucose l^–1, 1375 mg 2-phenylethanol l^–1 with a productivity of 153 mg l^–1 day^–1 and a molar yield of 74%. 2-Phenylethanol concentrations of 1 to 2 g l^–1 led to a two-fold and ten-fold decrease, respectively, in the mycelial radial growth rate. However, 2-phenylethanol was synthesized as the sole aromatic product and accumulated in the culture broth.     

Production of a thermostable extracellular lipase by Kluyveromyces marxianus

Kluyveromyces marxianus was grown in submerged culture in a complex medium with several potential inducers of lipolytic activity (triacylglycerols, fatty acids). The highest extracellular lipolytic enzyme production (about 80 U ml^–1 in 3 d) was obtained when the medium was supplemented with 2 g urea l^–1 plus 5 g tributyrin l^–1. Addition of surfactants (1 g l^–1) did not improve production. The lipase had a high thermal stability in aqueous solution (73% residual activity after 9 d at 50 °C, 16 min half-life time at 100 °C). It was also stable at acidic pH and showed good tolerance to organic solvents (70% residual activity after 2 d in n-hexane of cyclohexane).     

Production of mannitol by a novel strain of Candida magnoliae

A novel microorganism was isolated which is able to produce mannitol when grown in the presence of fructose and glucose as carbon sources. In flask culture in a medium containing 150 g fructose l^–1, it yielded 67 g mannitol l^–1 after 168 h. In fed-batch culture with 3–12% (w/v) fructose, production reached a maximum of 209 g mannitol l^–1 after 200 h, corresponding to an 83% yield and a 1.03 g l^–1 h^–1 productivity. The isolated strain was identified as Candida magnoliae based on identical sequences in the D1/D2 domain of its 26S rDNA and a similar carbon source utilization pattern with C. magnoliae reference strains.     

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.     

Fungal biotransformation of p-coumaric acid into caffeic acid by Pycnoporus cinnabarinus: an alternative for producing a strong natural antioxidant

Fungal biotransformation of p-coumaric acid into caffeic acid, potentially a strong antioxidant, was evidenced in Pycnoporus cinnabarinus cultures grown with high feeding of p-coumaric acid. Preliminary experiments showed no toxicity of both p-coumaric and caffeic acids at concentrations ranging from 0 to 500 mg l^–1. Feeding 450 mg p-coumaric acid l^–1 into P. cinnabarinus cultures grown on 20 g l^–1 glucose medium resulted in the production of 257 mg caffeic acid l^–1with a molar yield of 21%.     

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.     

Micropropagation of zedoary (<Emphasis Type="Italic">Curcuma zedoaria</Emphasis> Roscoe) – a valuable medicinal plant

Tissue culture propagation system was developed for zedoary (Curcuma zedoaria Roscoe), a valuable medicinal plant, using rhizome sprout cultures. Shoots were induced from rhizomes on basal MS medium containing 20 g l^–1 sucrose and 5 g l^–1 agar, supplemented with 20 (v/v) coconut water (CW) and benzylaminopurine (BA) concentrations from 0.5 to 5.0 m g l^–1. The excised shoots were subcultured on Murashige-Skoog (MS) medium with 20 (v/v) CW and different concentrations of BA and kinetin (Kin), either alone or in combination with indolebutyric acid (IBA) or naphthaleneacetic acid (NAA). MS medium with 20 (v/v) CW, 3 mg l^–1 BA, and 0.5 mg l^–1 IBA resulted in a multiplication rate per shoot; 5.6 shoots per explant were obtained on average after 30 days of culture. Well-developed shoots (30–40 mm in length) were rooted on MS medium containing 20 g l^–1 sucrose and 8 g l^–1 agar, supplemented with 20 (v/v) CW and 2 mg l^–1 NAA. More than 95 of the rooted plants were established in pots after hardening.     

Different nitrogen sources and growth responses of Spirulina platensis in microenvironments

Spirulina platensis was cultivated, in comparative studies, using several sources of nitrogen. The standard source used (sodium nitrate) was the same as that used in the synthetic medium Zarrouk, whereas the alternative nitrogen sources consisted of ammonium nitrate, urea, ammonium chloride, ammonium sulphate or acid ammonium phosphate. The initial nitrogen concentrations tested were 0.01, 0.03 and 0.05 M in an aerated photobioreactor at 30 °C, with an illuminance of 1900 lux, and 12 h-light/12 h-dark photoperiod over a period of 672 h. Maximum biomass was produced in medium containing sodium nitrate (0.01–0.03–0.05 M), followed by ammonium nitrate (0.01 M) and urea (0.01 M). The final biomass concentrations were 1.992 g l^–1 (0.03 M sodium nitrate), 1.628 g l^–1 (0.05 M sodium nitrate), 1.559 g l^–1 (0.01 M sodium nitrate), 0.993 g l^–1 (0.01 M ammonium nitrate) and 0.910 g l^–1 (0.01 M urea). This suggested that it is possible to utilize nitrogen sources other than sodium nitrate for growing S. platensis, in order to decrease the production costs of scaled up projects.     

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.     

Oxalic acid production from lipids by a mutant of Aspergillus niger at different pH

Crude rapeseed oil and post-refining fatty acids were used as substrates for oxalic acid production by a mutant of Aspergillus niger. Both the final concentration and the yield of the product were highest at pH 4 to 5. With a medium containing 50 g lipids l^–1, production reached a maximum of 68 g oxalic acid l^–1 after 7 d. A high yield of the product (up to 1.4 g oxalic acid g^–1 lipids consumed) was achieved with oil and fatty acids combined.