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.     

Optimization of culture conditions for the production of an extracellular ribonuclease by <Emphasis Type="Italic">Aspergillus niger</Emphasis> in a benchtop bioreactor

SummarySelf-directing optimization was successfully employed to determine the optimal combination of engineering parameters, viz., pH, aeration rate and agitation rate, for extracellular ribonuclease production by Aspergillus niger SA-13-20 in a batch bioreactor. Maximal RNase production of 5.38 IU ml^–1 was obtained at controlled pH of 2.33, aeration rate of 1.67 v/v/m and agitation rate of 850 rev/min. The effect of oxygen on the fermentation was also investigated. With increase in volumetric oxygen transfer coefficients (K_La), cell growth and RNase production first increased and then decreased. RNase production was further increased to 7.10 IU ml^–1 and the fermentation time was shortened from 96 to 72 h by controlling dissolved oxygen concentration at 10% saturation by aerating oxygen after about 28 h of fermentation under the above optimal condition. The kinetic model showed that RNase production by A. niger SA-13-20 was growth-associated.     

Optimization of fermentation conditions for production of xylanase by a newly isolated strain,Penicillium thiersii ZH-19

The objective of this study was to maximize production of xylanase by a newly isolated strain Penicillium thiersii ZH-19. Response surface methodology was employed to study the effects of significant factors such as pH, temperature, xylan concentration, and cultivation time, on the production of xylanase by Penicillium thiersii ZH-19. The optimal fermentation parameters for enhanced xylanase production were found to be pH 7.72, temperature 24.8°C, xylan 13.2 g l⁻¹ and the fermentation time 125.8 h. The model predicted a xylanase activity of 75.24 U ml⁻¹. Verification of the optimization showed that the maximum xylanase production reached 73.50 U mL⁻¹ in the flask experiments and 80.23 U mL⁻¹ in the scale of 15-L fermenter under the optimal condition.     

Growth and laccase production by Pleurotus ostreatus in submerged and solid-state fermentation

Pleurotus ostreatus showed atypical laccase production in submerged vs. solid-state fermentation. Cultures grown in submerged fermentation produced laccase at 13,000 U l⁻¹, with a biomass production of 5.6 g l⁻¹ and four laccase isoforms. However, cultures grown in solid-state fermentation had a much lower laccase activity of 2,430 U l⁻¹, biomass production of 4.5 g l⁻¹, and three laccase isoforms. These results show that P. ostreatus performs much better in submerged fermentation than in solid-state fermentation. This is the first report that shows such atypical behavior in the production of extracellular laccases by fungi.     

Acid phosphatase production by recombinant <Emphasis Type="Italic">Arxula adeninivorans</Emphasis>

Acid phosphatase production by recombinant Arxula adeninivorans was carried out in submerged fermentation. Using the Plackett–Burman design, three fermentation variables (pH, sucrose concentration, and peptone concentration) were identified to significantly affect acid phosphatase and biomass production, and these were optimized using response surface methodology of central composite design. The highest enzyme yields were attained in the medium with 3.9% sucrose and 1.6% peptone at pH 3.8. Because of optimization, 3.86- and 4.19-fold enhancement in enzyme production was achieved in shake flasks (17,054 U g⁻¹ DYB) and laboratory fermenter (18,465 U g⁻¹ DYB), respectively.     

Effect of n-dodecane on Crypthecodinium cohnii fermentations and DHA production

The potential use of n-dodecane as an oxygen vector for enhancement of Crypthecodinium cohnii growth and docosahexaenoic acid (DHA) production was studied. The volumetric fraction of oxygen vector influenced the gas–liquid volumetric mass transfer coefficient k _L a positively. The k _L a increased almost linearly with the increase of volumetric fraction of n-dodecane up to 1%. The stirring rate showed a higher influence on the k _L a than the aeration rate. The effects of this hydrocarbon on C. cohnii growth and DHA production were then investigated. A control batch fermentation without n-dodecane addition (CF) and a batch fermentation where n-dodecane 1% (v/v) was added (DF) were carried out simultaneously under the same experimental conditions. It was found that, before 86.7 h of fermentation, the biomass concentration, the specific growth rate, the DHA, and total fatty acids (TFA) production were higher in the CF. After this fermentation time, the biomass concentration, the DHA and TFA production were higher in the DF. The highest DHA content of biomass (6.14%), DHA percentage of TFA (51%), and DHA production volumetric rate r _DHA (9.75 mg l⁻¹ h⁻¹) were obtained at the end of the fermentation with n-dodecane (135.2 h). The dissolved oxygen tension (DOT) was always higher in the DF, indicating a better oxygen transfer due to the oxygen vector presence. However, since the other C. cohnii unsaturated fatty acids percentages did not increase with the oxygen availability increase due to the n-dodecane presence, a desaturase oxygen-dependent mechanism involved in the C. cohnii DHA biosynthesis was not considered to explain the DHA production increase. A selective extraction through the n-dodecane was suggested.     

Enhanced continuous production of lovastatin using pellets and siran supported growth of Aspergillus terreus in an airlift reactor

Lovastatin, a hypocholesterolemic agent, is a secondary metabolite produced by filamentous microorganism Aspergillus terreus in submerged batch cultivation. Lovastatin production by pellets and immobilized siran cells was investigated in an airlift reactor. The process was carried out by submerged cultivation in continuous mode with the objective of increasing productivity using pellet and siran supported growth of A terreus. The continuous mode of fermentation improves the rate of lovastatin production. The effect of dilution rate and aeration rate were studied in continuous culture. The optimum dilution rate for pellet was 0.02 h⁻¹ and for siran carrier was 0.025 h⁻¹. Lovastatin productivity using immobilized siran carrier (0.0255 g/L/h) was found to be greater than pellets (0.022 g/L/h). The productivity by both modes of fermentation was found higher than that of batch process which suggests that continuous cultivation is a promising strategy for lovastatin production.     

Production of conjugated linoleic acid by isolated Bifidobacterium strains

Two isolates from Korean faecal samples converted linoleic acid (LA) into conjugated linoleic acid (CLA), and were identified as Bifidobacterium breve and Bifidobacterium pseudocatenulatum by analysis of 16S rRNA sequences. In both cases, the major CLA was the cis-9, trans-11 isomer and CLA production paralleled the increase in cell biomass with both bacteria and was maximal at 30 h. The quantities of supernatant CLA produced by B. breve and B. pseudocatenulatum were 160 and 135 mg l^–1, from 500 mg LA l^–1, respectively. In the presence of 0.05% LA, the growth of B. breve was weakly inhibited but that of B. pseudocatenulatum was not affected over 6 days fermentation. During fermentation, the majority of CLA isomers were in the culture supernatant, but with washed cells obtained at the early stationary phase, 36 h, about 40% was detected in the cellular lipid. The optimal culture age with equal concentrations of washed cells for CLA production by the two bifidobacteria was determined to be 36 h. At this culture age, total CLA conversion of supernatant and cell pellets was 78% in B. breve and 69% in B. pseudocatenulatum from 0.01% LA.     

Application of response surface methodology in medium optimization for spore production of <Emphasis Type="Italic">Coniothyrium minitans</Emphasis> in solid-state fermentation

Summary Spore production of Coniothyrium minitans was optimized by using response surface methodology (RSM), which is a powerful mathematical approach widely applied in the optimization of fermentation process. In the first step of optimization, with Plackett–Burman design, soluble starch, urea and KH²PO⁴ were found to be the important factors affecting C. minitans spore production significantly. In the second step, a 2³ full factorial central composite design and RSM were applied to determine the optimal concentration of each significant variable. A second-order polynomial was determined by the multiple regression analysis of the experimental data. The optimum values for the critical components for the maximum were obtained as follows: soluble starch 0.643 (36.43 g. l⁻¹), urea −0.544 (3.91 g l⁻¹) and KH²PO⁴ 0.049 (1.02 g l⁻¹) with a predicted value of maximum spore production of 9.94 × 10⁹ spores/g IDM. Under the optimal conditions, the practical spore production was 1.04 × 10¹⁰ spores/g IDM. The determination coefficient (R²) was 0.923, which ensure an adequate credibility of the model.     

A Study on the Synthetic Characteristics of the Extracellular Polysaccharide (EPS) of Ganoderma lucidum Cultured in Batch Fermentation Using a Kinetic Model

The synthetic characteristics of the extracellular polysaccharide (EPS) of Ganoderma lucidum in batch fermentation were studied. The result showed that the production of EPS was partially growth-associated. The cell dry weight (CDW) and EPS reached 15.56 g·L⁻¹ and 3.02 g·L⁻¹, respectively. The yield of EPS to cell dry weight (Y_p/x) was 0.19. On the basis of the test results of batch fermentation, a kinetic model was proposed by using the Logistic equation for cell growth, the Luedeking–Piret equation for EPS production, and the Luedeking-piret-like equation for the consumption of glucose as substrate. The calculated results using these models were satisfactorily compared with the experimental data under various concentrations of glucose, and the average of relative errors was found to be not more than 5%. The kinetic model had practical guidance interesting in producing PES by Ganoderma lucidum.     

Exopolysaccharides production in Lactobacillus bulgaricus and Lactobacillus casei exploiting microfiltration

The physiology of Lactobacillus delbrueckii ssp. bulgaricus and Lactobacillus casei, extensively used in the dairy industry, was studied in order to evaluate key parameters in the synthesis of exopolysaccharides and to improve their production through novel fermentation processes. Selected strains were studied in shake flasks and in fermentor experiments using glucose and lactose as main carbon sources and bacto casitone as the only complex component, in a temperature range between 35 and 42°C. The production of exopolysaccharides was monitored and correlated to the growth conditions using both a colorimetric assay and chromatographic methods. Fermentor experiments in batch mode yielded 100 mg l⁻¹ of EPS from L. bulgaricus and 350 mg l⁻¹ from L. casei. Moreover, the use of a microfiltration (MF) bioreactor resulted in exopolysaccharides (EPS) concentrations threefold and sixfold those of batch experiments, respectively. The monosaccharidic composition of the two analyzed polymers differed from those previously reported. The optimization of the production of EPSs using the MF fermentation strategy could permit the use of these molecules produced by generally recognised as safe (GRAS) microorganisms in the place of other polysaccharides in the food industry.     

Starch processing wastewater as a new medium for production of <Emphasis Type="Italic">Bacillus thuringiensis</Emphasis>

Production of Bacillus thuringiensis (Bt) based bioinsecticide was studied by using starch processing wastewater (SPW) as a raw material. Results indicated that the nutrients contained in SPW were sufficient for growth, sporulation and δ-endotoxin production of Bacillus thuringiensis subsp. kurstaki (Btk). The final cell counts and spore counts achieved in SPW medium were 72% and 107% respectively higher than those in the soybean meal based commercial medium. Higher δ-endotoxin yield of 2.67 mg mL⁻¹ and higher entomotoxicity of 1,050 IU μL⁻¹ were also obtained in SPW medium as compared with the commercial medium at the end of fermentation. The morphological observations also revealed that the fermentation cycle of Btk could be shortened in this new medium. This process provides solutions for safe SPW disposal and production of high potency and low cost bioinsecticide.     

Mn<Superscript>2+</Superscript> enhances theanine-forming activity of recombinant glutamine synthetase from <Emphasis Type="Italic">Bacillus subtilis</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Bacillus subtilis glutamine synthetase (GS) was highly expressed (about 86% of total protein) as soluble protein in Escherichia coli BL21(DE3) containing pET28a-glnA, which was induced by 0.4 mM IPTG in LB medium, and maximal theanine-forming activity of the recombinant GS induced in LB is 6.4 U/mg at a series concentration (0–100 mM) of Mn²⁺ at optimal pH 7.5. In order to get GS with high theanine-forming activity, safety, and low cost for food and pharmaceutics industry, M9-A (details are described in “Materials and methods”) and 0.1% (w/v) lactose were selected as culture medium and inducer respectively. Recombinant GS was also highly expressed (84% of total protein) and totally soluble in M9-A and the specific activity of the recombinant GS is 6.2 U/mg which is approximate to that (6.4 U/mg) induced in LB in the presence of 10 mM Mn²⁺ at optimal pH 7.5. The activity is markedly higher activated by Mn²⁺ than that by other nine bivalent cations. Furthermore, M9-B (5 μM Mn²⁺ was added into M9-A) was used to culture the recombinant strain and theanine-forming activity of the recombinant GS induced in M9-B was improved 20% (up to 7.6 U/mg). Finally, theanine production experiment coupled with yeast fermentation system was carried out in a 1.0 ml reaction system with 0.1 mg crude GS from M9-B or M9-A, and the yield of theanine were 15.3 and 13.1 g/L by paper chromatography and HPLC, respectively.     

Simultaneous saccharification and ethanol fermentation of oxalic acid pretreated corncob assessed with response surface methodology

Response surface methodology was used to evaluate optimal time, temperature and oxalic acid concentration for simultaneous saccharification and fermentation (SSF) of corncob particles by Pichia stipitis CBS 6054. Fifteen different conditions for pretreatment were examined in a 2³ full factorial design with six axial points. Temperatures ranged from 132 to 180 °C, time from 10 to 90 min and oxalic acid loadings from 0.01 to 0.038 g/g solids. Separate maxima were found for enzymatic saccharification and hemicellulose fermentation, respectively, with the condition for maximum saccharification being significantly more severe. Ethanol production was affected by reaction temperature more than by oxalic acid and reaction time over the ranges examined. The effect of reaction temperature was significant at a 95% confidence level in its effect on ethanol production. Oxalic acid and reaction time were statistically significant at the 90% level. The highest ethanol concentration (20 g/l) was obtained after 48 h with an ethanol volumetric production rate of 0.42 g ethanol l⁻¹ h⁻¹. The ethanol yield after SSF with P. stipitis was significantly higher than predicted by sequential saccharification and fermentation of substrate pretreated under the same condition. This was attributed to the secretion of β-glucosidase by P. stipitis. During SSF, free extracellular β-glucosidase activity was 1.30 pNPG U/g with P. stipitis, while saccharification without the yeast was 0.66 pNPG U/g.     

Improved production of pristinamycin coupled with an adsorbent resin in fermentation by Streptomyces pristinaespiralis

Batch fermentation by Streptomyces pristinaespiralis with the addition of adsorbent resins was used to increase the production of pristinamycin. In consideration of the adsorption capacity and the desorption ability, a polymeric resin, JD-1, was finally selected. The maximum production of pristinamycin in Erlenmeyer flasks went up to 1.13 from 0.4 g l⁻¹, by adding 12% (w/v) resin JD-1 into the culture broth at 20 h after inoculation. In a 3 l bioreactor, pristinamycin fermentation with the addition of 12% (w/v) resin JD-1 at 20 h after inoculation reached 0.8 g l⁻¹, which was a 1.25-fold increase over fermentation without resin.     

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.     

Evaluation of plastic composite-supports for enhanced ethanol production in biofilm reactors

Biofilms are a natural form of cell immobilization that result from microbial attachment to solid supports. Biofilm reactors with polypropylene composite-supports containing up to 25% (w/w) of various agricultural materials (corn hulls, cellulose, oat hulls, soybean hulls or starch) and nutrients (soybean flour or zein) were used for ethanol production. Pure cultures ofZymomonas mobilis, ATCC 31821 orSaccharomyces cerevisiae ATCC 24859 and mixed cultures with either of these ethanol-producing microorganisms and the biofilm-formingStreptomyces viridosporus T7A ATCC 39115 were evaluated. An ethanol productivity of 374g L^–1 h^–1 (44% yield) was obtained on polypropylene composite-supports of soybean hull-zein-polypropylene by usingZ. mobilis, whereas mixed-culture fermentations withS. viridosporus resulted in ethanol productivity of 147.5 g L^–1 h^–1 when polypropylene composite-supports of corn starch-soybean flour were used. WithS. cerevisiae, maximum productivity of 40 g L^–1 h^–1 (47% yield) was obtained on polypropylene composite-supports of soybean hull-soybean flour, whereas mixed-culture fermentation withS. viridosporus resulted in ethanol productivity of 190g L^–1 h^–1 (35% yield) when polypropylene composite-supports of oat hull-polypropylene were used. The maximum productivities obtained without supports (suspension culture) were 124 g L^–1 h^–1 and 5 g L^–1 h^–1 withZ. mobilis andS. cerevisiae, respectively. Therefore, forZ. mobilis andS. cerevisiae, ethanol productivities in biofilm fermentations were three- and eight-fold higher than suspension culture fermentations, respectively. Biofilm formation on the chips was detected by weight change and Gram staining of the support material at the end of the fermentation. The ethanol production rate and concentrations were consistently greater in biofilm reactors than in suspension cultures.This is Journal Paper No. J-16356 of the Iowa Agriculture and Home Economics Experiment Station, Ames, Iowa. Project No. 3253     

Co-production of S-adenosyl-l-methionine and glutathione from spent brewer’s yeast cells

Both S-adenosyl-l-methionine (AdoMet) and glutathione (GSH) are important small molecules with pharmaceutical importance. The co-production of AdoMet and GSH using abundant spent brewer’s yeast cells from the beer industry and with l-methionine supplement was successfully realized. Experimental data showed that improvement of GSH productivity was accompanied by AdoMet accumulation. AdoMet productivity of 40–45 mg g⁻¹ (DCW) was successfully achieved and an additional 13–18 mg g⁻¹ (DCW) GSH was synthesized in spent brewer’s yeast cells.     

Xylitol conversion by fermentation using five yeast strains and polyelectrolyte-assisted ultrafiltration

Batch fermentations for xylitol production were conducted using Candida boidinii (BCRC 21432), C. guilliermondii (BCRC 21549), C. tropicalis (BCRC 20520), C. utilis (BCRC 20334), and P. anomala (BCRC 21359) together with a mixture of sugars simulating lignocellulosic hydrolysates as the carbon source. C. tropicalis had the highest bioconversion yield (Y_P/S) of 0.79 g g⁻¹ (g xylitol·g xylose⁻¹) over 48 h. Additional fermentations with C. tropicalis achieved Y_P/S values of 0.6 and 0.39 g g⁻¹ after 96 and 72 h using urea and soybean meal as the nitrogen sources, respectively. Ethanol and arabitol were also produced in all fermentation. Xylitol in the fermentation broth was recovered by cross-flow ultrafiltration. With prior application of 2 mg polydiallyl dimethylammonium chloride l⁻¹ on the membrane surface, protein in the permeate was reduced from 7.1 to 1.5 mg l⁻¹ after 2 h.     

Temperature management strategy for efficient gene expression in a thermally inducible <Emphasis Type="Italic">Escherichia coli</Emphasis>/bacteriophage system

In a two-phase operation, E. coli containing λSNNU1 (Q ⁻ S ⁻) in the chromosome is typically cultured at 33°C and cloned gene expression is induced by elevating the temperature. At least 40°C is necessary for complete induction of cloned gene expression; however, temperatures above 40°C have been shown to inhibit cloned gene expression. This suggests that a three-phase operation, which has an induction phase between the growth and production phases, may result in higher gene expression. In this study, optimal temperature management strategies were investigated for the three-phase operation of cloned gene expression in thermally inducible E. coli/bacteriophage systems. The optimal temperature for the induction phase was determined to be 40°C. When the temperature of the production stage was 33°C, the optimal time period for the induction phase at 40°C was determined to be 60 min. In contrast, when the temperature of the production phase was 37°C, the optimal period for the induction phase at 40°C was 20∼30 min. When the three-phase temperature and temporal profile were set at a growth phase of 33°C, an induction phase at 40°C for 30 min, and a production phase at 37°C, the highest level of cloned gene expression was achieved.