Efficient itaconic acid production by Aspergillus terreus: Overcoming the strong inhibitory effect of manganese

Itaconic acid (IA), a building block platform chemical, is produced industrially by Aspergillus terreus utilizing glucose. Lignocellulosic biomass can serve as a low cost source of sugars for IA production. However, the fungus could not produce IA from dilute acid pretreated and enzymatically saccharified wheat straw hydrolyzate even at 100-fold dilution. Furfural, hydroxymethyl furfural and acetic acid were inhibitory, as is typical, but Mn²⁺ was particularly problematic for IA production. It was present in the hydrolyzate at a level that was 230 times over the inhibitory limit (50 ppb). Recently, it was found that PO₄³⁻ limitation decreased the inhibitory effect of Mn²⁺ on IA production. In the present study, a novel medium was developed for production of IA by varying PO₄³⁻, Fe³⁺ and Cu²⁺ concentrations using response surface methodology, which alleviated the strong inhibitory effect of Mn²⁺. The new medium contained 0.08 g KH₂PO₄, 3 g NH₄NO₃, 1 g MgSO₄·7H₂O, 5 g CaCl₂·2 H₂O, 0.83 mg FeCl₃·6H₂O, 8 mg ZnSO₄·7H₂O, and 45 mg CuSO₄·5H₂O per liter. The fungus was able to produce IA very well in the presence of Mn²⁺ up to 100 ppm in the medium. This medium will be extremely useful for IA production in the presence of Mn²⁺. This is the first report on the development of Mn²⁺ tolerant medium for IA production by A. terreus.     

Optimizing Production of Extracellular Laccase from Grammothele Subargentea CLPS No. 436 Strain

The production of extracellular laccase by the Grammothele subargentea CLPS no. 436 strain in liquid cultures grown on a carbon-limited basal medium was significantly enhanced when culture conditions, including the addition of CuSO₄·5H₂O or veratryl alcohol, were consecutively optimized. A laccase activity as high as 1954.5 mU ml⁻¹ of liquid medium was obtained under optimum conditions, which corresponded to non-agitated cultures supplemented with 0.6 mM CuSO₄·5H₂O. Veratryl alcohol at 1 mM was less effective than CuSO₄·5H₂O for increasing laccase activity levels; the supplementation of veratryl alcohol resulted only in maximum levels of 44 mU ml⁻¹ in non-agitated cultures. This revised version was published online in July 2006 with corrections to the Cover Date.     

MEDIUM OPTIMIZATION OF ANTIFUNGAL ACTIVITY PRODUCTION BY Bacillus amyloliquefaciens USING STATISTICAL EXPERIMENTAL DESIGN

In order to overproduce biofungicides agents by Bacillus amyloliquefaciens BLB371, a suitable culture medium was optimized using response surface methodology. Plackett–Burman design and central composite design were employed for experimental design and analysis of the results. Peptone, sucrose, and yeast extract were found to significantly influence antifungal activity production and their optimal concentrations were, respectively, 20 g/L, 25 g/L, and 4.5 g/L. The corresponding biofungicide production was 250 AU/mL, corresponding to 56% improvement in antifungal components production over a previously used medium (160 AU/mL). Moreover, our results indicated that a deficiency of the minerals CuSO₄, FeCl₃ · 6H₂O, Na₂MoO₄, KI, ZnSO₄ · 7H₂O, H₃BO₃, and C₆H₈O₇ in the optimized culture medium was not crucial for biofungicides production by Bacillus amyloliquefaciens BLB371, which is interesting from a practical point of view, particularly for low-cost production and use of the biofungicide for the control of agricultural fungal pests.     

Ca<Superscript>2+ </Superscript>and Cu<Superscript>2+ </Superscript>supplementation increases mannitol production by <Emphasis Type="Italic">Candida magnoliae</Emphasis>

Supplementation with CaCl₂·2H₂O (50 mg l⁻¹) or CuSO₄·5H₂O (10 mg l⁻¹) improved mannitol production by Candida magnoliae by 14.5 and 18.6% (25 and 32 g/L), respectively. When used in combination, they acted synergistically: Ca²⁺ decreased the intracellular concentration of mannitol 30%, whereas Cu²⁺ increased the intracellular activity of mannitol dehydrogenase 1.6-times more than control. Ca²⁺ probably works by altering the permeability of cells to mannitol, whereas, Cu²⁺ increases the activity of an enzyme responsible for mannitol biosynthesis.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> using semicontinuous fermentation in bioreactor

Semicontinuous fermentation using pellets of Rhizopus oryzae has been recognized as a promising technology for l-lactic acid production. In this work, semicontinuous fermentation of R. oryzae AS 3.819 for l-lactic acid production has been developed with high l-lactic acid yield and volumetric productivity. The effects of factors such as inoculations, CaCO₃ addition time, and temperature on l-lactic acid yield and R. oryzae morphology were researched in detail. The results showed that optimal fermentation conditions for the first cycle were: inoculation with 4% spore suspension, CaCO₃ added to the culture medium at the beginning of culture, and culture temperature of 32–34°C. In orthogonal experiments, high l-lactic acid yield was achieved when the feeding medium was (g/l): glucose, 100; (NH₄)₂SO₄, 2; KH₂PO₄, 0.1; ZnSO₄·7H₂O, 0.33; MgSO₄·7H₂O, 0.15; CaCO₃, 50. Twenty cycles of semicontinuous fermentation were carried out in flask culture. l-lactic acid yield was 78.75% for the first cycle and 80–90% for the repeated cycles; the activities of lactate dehydrogenases (LDH) were 7.2–9.2 U/mg; fermentation was completed in 24 h for each repeated cycle. In a 7-l magnetically stirred fermentor, semicontinuous fermentation lasted for 25 cycles using pellets of R. oryzae AS 3.819 under the optimal conditions determined from flask cultures. The final l-lactic acid concentration (LLAC) reached 103.7 g/l, and the volumetric productivity was 2.16 g/(l·h) for the first cycle; in the following 19 repeated cycles, the final LLAC reached 81–95 g/l, and the volumetric productivities were 3.40–3.85 g/(l·h).     

Effects of molten-salt/ionic-liquid mixture on extraction of docosahexaenoic acid (DHA)-rich lipids from Aurantiochytrium sp. KRS101

In this study, lipid extraction from Aurantiochytrium sp. was performed using a molten-salt/ionic-liquid mixture. The total fatty acid content of Aurantiochytrium sp. was 478.8 mg/g cell, from which 145 mg/g cell (30.3 % of total fatty acids) of docosahexaenoic acid (DHA) was obtained. FeCl₃·6H₂O showed a high lipid extraction yield (207.9 mg/g cell), when compared with that of [Emim]OAc, which was only 118.1 mg/g cell; notably however, when FeCl₃·6H₂O was mixed with [Emim]OAc (5:1, w/w), the yield was increased to 478.6 mg/g cell. When lipid was extracted by the FeCl₃·6H₂O/[Emim]OAc mixture at a 5:1 (w/w) blending ratio under 90 °C, 30 min reaction conditions, the fatty acid content of the extracted lipid was a high purity 997.7 mg/g lipid, with most of the DHA having been extracted (30.2 % of total fatty acids). Overall, lipid extraction from Aurantiochytrium sp. was enhanced by the synergistic effects of the molten-salt/ionic-liquid mixture with different ions.     

Enhancement of erythritol production by Trichosporonoides oedocephalis ATCC 16958 through regulating key enzyme activity and the NADPH/NADP ratio with metal ion supplementation

Erythritol, a well-known natural sweetener, is mainly produced by microbial fermentation. Various metal ions (Al³⁺, Cu²⁺, Mn²⁺, and Ni²⁺) were added to the culture medium of Trichosporonoides oedocephalis ATCC 16958 at 30?mg/L in shake flask cultures. Compared with controls, Cu²⁺ increased the erythritol content by 86% and decreased the glycerol by-product by 31%. After 48 hr of shake flask culture, sodium dodecyl sulfate polyacrylamide gel electrophoresis showed that expression levels of erythrose reductase (ER) in the presence of 30?mg/L CuSO₄?·?5H₂O were higher than those obtained after treatment with other examined metal ions. Furthermore, after 108 hr of batch culture in a 5-L bioreactor, supplementation with 30?mg/L of CuSO₄?·?5H₂O increased the specific erythritol content by 27%. Further studies demonstrated that ER activity under 30?mg/L CuSO₄?·?5H₂O supplementation in a fermentor was overtly increased compared with the control after 60 hr, while glycerol-3-phosphate dehydrogenase activity was clearly reduced in most of the fermentation process. Furthermore, the NADPH/NADP ratio was slightly lower in T. oedocephalis cells treated with Cu²⁺ compared with control cells. These results provide further insights into Cu²⁺ effects on erythritol biosynthesis in T. oedocephalis and should improve the industrial production of erythritol by biological processes.     

Optimization of fermentation conditions for production of anti-TMV extracellular ribonuclease by Bacillus cereus using response surface methodology

Bacillus cereus ZH14 was previously found to produce a new type of antiviral ribonuclease, which was secreted into medium and active against tobacco mosaic virus. In order to enhance the ribonuclease production, in this study the optimization of culture conditions using response surface methodology was done. The fermentation variables including culture temperature, initial pH, inoculum size, sucrose, yeast extract, MgSO₄·7H₂O, and KNO₃ were considered for selection of significant ones by using the Plackett–Burman design, and four significant variables (sucrose, yeast extract, MgSO₄·7H₂O, and KNO₃) were further optimized by a 2⁴ factorial central composite design. The optimal combination of the medium constituents for maximum ribonuclease production was determined as 8.50 g/l sucrose, 9.30 g/l yeast extract, 2.00 g/l MgSO₄·7H₂O, and 0.62 g/l KNO₃. The enzyme activity was increased by 60%. This study will be helpful to the future commercial development of the new bacteria-based antiviral ribonuclease fermentation process.     

Development of medium for enhanced production of glutaminase-free <Emphasis Type="SmallCaps">l</Emphasis>-asparaginase from <Emphasis Type="Italic">Pectobacterium carotovorum</Emphasis> MTCC 1428

Glutaminase-free l-asparaginase is known to be an excellent anticancer agent. In the present study, statistically based experimental designs were applied to maximize the production of glutaminase-free l-asparaginase from Pectobacterium carotovorum MTCC 1428. Nine components of the medium were examined for their significance on the production of l-asparaginase using the Plackett–Burman experimental design. The medium components, viz., glucose, l-asparagine, KH₂PO₄, and MgSO₄·7H₂O, were screened based on their high confidence levels (P < 0.04). The optimum levels of glucose, l-asparagine, KH₂PO₄, and MgSO₄·7H₂O were found to be 2.076, 5.202, 1.773, and 0.373 g L⁻¹, respectively, using the central composite experimental design. The maximum specific activity of l-asparaginase in the optimized medium was 27.88 U mg⁻¹ of protein, resulting in an overall 8.3-fold increase in the production compared to the unoptimized medium.     

Structures and luminescent sensors of mixed‐counterions based salen‐type lanthanide coordination polymers

Reactions of N,N′‐bis (salicylidene)‐1,2‐cyclohexanediamine (H₂L) with mixed lanthanide counterions of LnCl₃·6H₂O and Ln (NO₃)₃·6H₂O afford six H₂L lanthanide coordination polymers, e.g. {[Pr(H₂L)₂(NO₃)₂Cl]·2CH₂Cl₂}_n ( 1 ); {[Ln(H₂L)_1.5(NO₃)₃]₂·5CHCl₃·mCH₃OH}_n [Ln = Sm ( 2 ), Eu ( 3 ), Gd ( 4 ), Tb ( 5 ) and Yb ( 6 ); m = 1 ( 2 – 5 ); m = 0 ( 6 )]. X‐ray crystallographic analysis reveals that complex 1 exhibits three‐dimensional diamondoid topologic structure and complexes 2 – 6 are of two‐dimensional structure. Luminescent spectra show that complexes 1 and 6 have characteristic near‐infrared (NIR) emission of praseodymium (III) and ytterbium (III) ions and complexes 2 – 5 emit luminescence in the visible region. Complexes 3 and 6 reveal sensitive luminescence responses to formaldehyde.     

Response surface methodology for optimization of medium components in submerged culture of Aspergillus flavus for enhanced heparinase production

Aims: Aim of the study was to develop a medium for optimal heparinase production with a strain of Aspergillus flavus (MTCC‐8654) by using a multidimensional statistical approach. Methods and Results: Statistical optimization of intracellular heparinase production by A. flavus, a new isolate, was investigated. Plackett–Burman design was used to evaluate the affect of medium constituents on heparinase yield. The experimental results showed that the production of heparinase was dependent upon heparin, the inducer; chitin, structurally similar to heparin and NH₄NO_3, the nitrogen source. A central composite design was applied to derive a statistical model for optimizing the composition of the fermentation medium for the production of heparinase enzyme. The optimum fermentation medium consisted of (g l^?1) Mannitol, 8·0; NH₄NO₃, 2·5; K₂HPO₄, 2·5; Na₂HPO₄, 2·5; MgSO₄.7H₂O, 0·5; Chitin, 17·1; Heparin, 0·6; trace salt solution (NaMoO₄.2H₂O, CoCl₂.6H₂O, CuSO₄.5H₂O, FeSO₄.7H₂O, CaCl₂), 10^?4 mol l^?1. Conclusions: A 2·37‐fold increase in heparinase production was achieved in economic and effective manner by the application of statistical designs in medium optimization. Significance and Impact of the Study: Heparinase production was doubled by statistical optimization in a cost‐effective manner. This heparinase can find application in pharmaceutical industry and for the generation of low‐molecular‐weight heparins, active as antithrombotic and antitumour agents.     

Optimization of culture medium for the continuous cultivation of the microalga Haematococcus pluvialis

The freshwater microalga Haematococcus pluvialis is one of the best microbial sources of the carotenoid astaxanthin, but this microalga shows low growth rates and low final cell densities when cultured with traditional media. A single-variable optimization strategy was applied to 18 components of the culture media in order to maximize the productivity of vegetative cells of H. pluvialis in semicontinuous culture. The steady-state cell density obtained with the optimized culture medium at a daily volume exchange of 20% was 3.77 · 10⁵ cells ml⁻¹, three times higher than the cell density obtained with Bold basal medium and with the initial formulation. The formulation of the optimal Haematococcus medium (OHM) is (in g l⁻¹) KNO₃ 0.41, Na₂HPO₄ 0.03, MgSO₄ · 7H₂O 0.246, CaCl₂ · 2H₂O 0.11, (in mg l⁻¹) Fe(III)citrate · H₂O 2.62, CoCl₂ · 6H₂O 0.011, CuSO₄ · 5H₂O 0.012, Cr₂O₃ 0.075, MnCl₂ · 4H₂O 0.98, Na₂MoO₄ · 2H₂O 0.12, SeO₂ 0.005 and (in μg l⁻¹]) biotin 25, thiamine 17.5 and B₁₂ 15. Vanadium, iodine, boron and zinc were demonstrated to be non-essential for the growth of H. pluvialis. Higher steady-state cell densities were obtained by a three-fold increase of all nutrient concentrations but a high nitrate concentration remained in the culture medium under such conditions. The high cell productivities obtained with the new optimized medium can serve as a basis for the development of a two-stage technology for the production of astaxanthin from H. pluvialis. Received: 10 September 1999 / Received revision: 2 December 1999 / Accepted: 3 December 1999     

Evaluation of electrocoagulation,flocculation, and sedimentation harvesting methods on microalgae consortium grown in anaerobically digested abattoir effluent

Microalgae dewatering is a major bottleneck for biomass production in a large-scale microalgal production system which accounts for 20–60% of production cost. In this study, three dewatering systems of electrocoagulation, flocculation, and pH-induced flocculation were evaluated for microalgal consortium grown in anaerobically digested abattoir effluent at pH 6.5 and 9.5. At the shortest time (15 min) and the highest current density (0.08 A cm^?2), the highest microalgae recoveries of 78 and 84% were obtained with the corresponding power consumptions of 1.25 and 1.07 kWh kg^?1 for cultures at pH 6.5 and 9.5. For microalgae suspension at pH 6.5, the highest biomass recovery of 77% was obtained when 100 mg L^?1 of FeCl₃·6H₂O (after 15 min) or 100 mg L^?1 of Al₂(SO₄)₃·18H₂O (after 30 min) was added. However, microalgal recoveries significantly increased when FeCl₃·6H₂O or Al₂(SO₄)₃·18H₂O was used with the culture at pH 9.5. pH-Induced experiments showed that cultures adjusted at pH 10.5 had 36% higher biomass recovery compared to that in cultures at pH 8.5 after 2 h. The results of this study showed that cultures at higher pH (9.5) had a better microalgae recovery in all dewatering systems than cultures at lower pH (6.5).

     

Isolation of Amylase Inhibitor-producing Microorganism

An amylase inhibitor-producing microorganism was identified as a subspecies of Strepto- myces diastaticus from morphological and physiological studies and was named Streptomyces diastaticus subsp. amylostaticus No. 2476.

When this strain was aerobically cultured in a shaking flask containing 100 ml of medium consisting of 4% corn starch, 2% soy bean flake extract, 0.3 % NaCl, 0.1 % K₂HPO₄, 0.05% MgSO₄·7H₂O, 0.001% FeS0₄ · 7H₂O, 0.0001% CuSO₄-5H₂O, 0.0001% ZnSO₄·7H₂O, and 0.0001% MnS0₄ nH₂O (pH 7.0) at 30°C, the highest inhibitory activity was obtained after 70 ~ 80 hr of cultivation.

This amylase inhibitor (S-AI) had inhibitory activity on α-amylases and glucoamylase, but not on β-amylases and pullulanase.     

Induction of manganese peroxidase and laccase by <Emphasis Type="Italic">Lentinula edodes</Emphasis> under liquid culture conditions and their isozyme detection by enzymatic staining on native-PAGE

The white-rot basidomycete Lentinula edodes often produces the lignin-degrading enzymes manganese peroxidase (MnP; EC 1.11.1.13) and laccase (Lcc; EC 1.10.3.2) in sawdust-based media. In the present study, MnP from L. edodes was induced under liquid culture supplemented with sawdust extracts of Castanopsis cuspidata. Lcc activity was induced by the addition of 2 mM CuSO₄·5H₂O into the same media 7 days after initial inoculation. Phenoloxidase enzymes were distinguished by polyacrylamide gel electrophoresis (native-PAGE), followed by sequential enzymatic staining with an improved staining solution. The isozyme bands detected under MnP-induced conditions were identified as manganese peroxidase (lemnp2) and bands detected under Lcc-induced conditions were identified as laccase (lcc1) by Q-TOF mass spectrometry.     

Statistical optimization of medium components for avilamycin production by <Emphasis Type="Italic">Streptomyces viridochromogenes</Emphasis> Tü57-1 using response surface methodology

A fermentation medium for avilamycin production by Streptomyces viridochromogenes Tü57-1 has been optimized. Important components and their concentrations were investigated using fractional factorial design and Box–Behnken Design. The results showed that soybean flour, soluble starch, MgSO₄·7H₂O and CaCl₂·2H₂O are important for avilamycin production. A polynomial model related to medium components and avilamycin yield had been established. A high coefficient of determination (R ² = 0.92) was obtained that indicated good agreement between the experimental and predicted values of avilamycin yield. Student’s T-test of each coefficient showed that all the linear and quadratic terms had significant effect (P > |T| < 0.05) on avilamycin yield. The significance of tested components was related to MgSO₄·7H₂O (0.37 g/L), CaCl₂·2H₂O (0.39 g/L), soybean flour (21.97 g/L) and soluble starch (37.22 g/L). The yield of avilamycin reached 88.33 ± 0.94 mg/L (p < 0.05) that was 2.8-fold the initial yield.     

Chemically defined media for growth and sporulation of Entomophthora virulenta

Amino acids, salts, and vitamins were combined with dextrose to test their effect on growth and sporulation of Entomophthora virulenta in liquid shake culture. The addition of a vitamin solution to the tested media did not enhance growth or sporulation. MgSO₄·7H₂O was the only salt individually tested that allowed for good growth and sporulation. MgSO₄·7H₂O concentrations exceeding 250 mg/liter in media lacking other salts inhibited sporulation. A simple medium of l-arginine, l-leucine, glycine, and mineral salts allowed high growth and sporulation.     

Optimizing emulsan production of <Emphasis Type="Italic">A. venetianus</Emphasis> RAG-1 using response surface methodology

Statistical experimental design was used to optimize medium constituents for emulsan production by Acinetobacter venetianus RAG-1 in batch cultivation. The factors affecting emulsan production were screened by a two-level factorial design, and the optimal concentration of medium constituents for emulsan production were determined by the method of steepest path ascent and central composite experimental design. Experimental results showed that the optimal medium constituents were 9.16 g/L ethanol, 8.2 g/L KH₂PO₄, 23.32 g/L K₂HPO₄, 5.77 g/L (NH₄)₂SO₄ and 0.354 g/L MgSO₄•7H₂O. Under this optimal composition, the predicted emulsan production was 72.198 mg/L, and experimental value was 73.312 mg/L for 80 h culture in the shake flasks, and the emulsan yield by A. venetianus RAG-1 was enhanced nearly 1.48-fold (from 49.5 to 73.312 mg/L). Based on the results, we identify the optimal medium constituents for emulsan production and could take advantage of strategy for scale up the fermentation of emulsan production.     

Differential medium for revelation of bacterial producer strains of L-asparaginases

A specific, fast, and easy method for revelation of active plate producers of L-asparaginase using differential medium on the basis of LB or M9 with 1.5% agar was developed. Each 100 ml of LB or M9 medium additionally contained 6–7 ml of glycerol, 4 g of L-asparagine, 0.2 g of CaCO₃, and diagnostic components: 3 ml of 0.2 M CuSO₄ · 5H₂O and 2.5 ml of 0.1 M K₃Fe(CN)₆, pH 7.6–7.8. The results were counted 12–20 or 24–48 h after strain growth at 37°C in corresponding mediums. Red color of colonies and colored zone around them showed the ability of the strain under study to destroy asparaginic complexes. The recommended method allows revealing bacterial strains producing L-asparaginase with specific activity of not less than 0.1–3.0 MU/mg of protein.     

Optimization of nutrient parameters for lovastatin production by <Emphasis Type="Italic">Monascus purpureus</Emphasis> MTCC 369 under submerged fermentation using response surface methodology

Lovastatin, an inhibitor of HMG-CoA reductase, was produced by submerged fermentation using Monascus purpureus MTCC 369. Five nutritional parameters screened using Plackett–Burman experimental design were optimized by Box–Behnken factorial design of response surface methodology for lovastatin production in shake flask cultures. Maximum lovastatin production of 351 mg/l were predicted in medium containing 29.59 g/l dextrose, 3.86 g/l NH₄Cl, 1.73 g/l KH₂PO₄, 0.86 g/l MgSO₄·7H₂O, and 0.19 g/l MnSO₄·H₂O using response surface plots and point prediction tool of DESIGN EXPERT 7.0 (Statease, USA) software.