Effect of trace metals on ethanol production from synthesis gas by the ethanologenic acetogen, <Emphasis Type="Italic">Clostridium</Emphasis><Emphasis Type="Italic">ragsdalei</Emphasis>

The effect of trace metal ions (Co²⁺, Cu²⁺, Fe²⁺, Mn²⁺, Mo⁶⁺, Ni²⁺, Zn²⁺, SeO₄ ⁻ and WO₄ ⁻) on growth and ethanol production by an ethanologenic acetogen, Clostridium ragsdalei was investigated in CO:CO₂-grown cells. A standard acetogen medium (ATCC medium no. 1754) was manipulated by varying the concentrations of trace metals in the media. Increasing the individual concentrations of Ni²⁺, Zn²⁺, SeO₄ ⁻ and WO₄ ⁻ from 0.84, 6.96, 1.06, and 0.68 μM in the standard trace metals solution to 8.4, 34.8, 5.3, and 6.8 μM, respectively, increased ethanol production from 35.73 mM under standard metals concentration to 176.5, 187.8, 54.4, and 72.3 mM, respectively. Nickel was necessary for growth of C. ragsdalei. Growth rate (μ) of C. ragsdalei improved from 0.34 to 0.49 (day⁻¹), and carbon monoxide dehydrogenase (CODH) and hydrogenase (H₂ase)-specific activities improved from 38.45 and 0.35 to 48.5 and 1.66 U/mg protein, respectively, at optimum concentration of Ni²⁺. At optimum concentrations of WO₄ ⁻ and SeO₄ ⁻, formate dehydrogenase (FDH) activity improved from 32.3 to 42.6 and 45.4 U/mg protein, respectively. Ethanol production and the activity of FDH reduced from 35 mM and 32.3 U/mg protein to 1.14 mM and 8.79 U/mg protein, respectively, upon elimination of WO₄ ⁻ from the medium. Although increased concentration of Zn²⁺ enhanced growth and ethanol production, the activities of CODH, FDH, H₂ase and alcohol dehydrogenase (ADH) were not affected by varying the Zn²⁺ concentration. Omitting Fe²⁺ from the medium decreased ethanol production from 35.7 to 6.30 mM and decreased activities of CODH, FDH, H₂ase and ADH from 38.5, 32.3, 0.35, and 0.68 U/mg protein to 9.07, 7.01, 0.10, and 0.24 U/mg protein, respectively. Ethanol production improved from 35 to 54 mM when Cu²⁺ was removed from the medium. The optimization of trace metals concentration in the fermentation medium improved enzyme activities (CODH, FDH, and H₂ase), growth and ethanol production by C. ragsdalei.     

Effects of macroelements and nitrogen source on biomass accumulation and withanolide-A production from cell suspension cultures of <Emphasis Type="Italic">Withania somnifera</Emphasis> (L.) Dunal

Withania somnifera is an important medicinal plant that contains withanolides and withaferins, both bioactive compounds. We have tested the effects of macroelements and nitrogen source in W. somnifera cell suspension cultures with the aim of optimizing the production of biomass and withanolide A. The effects of the macroelements NH₄NO_3, KNO_3, CaCl_2, MgSO₄ and KH₂PO₄ at concentrations of 0.0, 0.5, 1.0, 1.5 and 2.0× strength and of the nitrogen source [NH₄ ⁺/NO₃ ⁻ (mM/mM) ratio of: 0.00/18.80, 7.19/18.80, 14.38/18.80, 21.57/18.80, 28.75/18.80, 14.38/0.00, 14.38/9.40, 14.38/18.80, 14.38/28.20, and 14.38/37.60 (mM)] in Murashige and Skoog medium were tested for biomass and withanolide A production. The highest accumulation of biomass [147.81 g l⁻¹ fresh weight (FW) and 14.02 g l⁻¹ (dry weight (DW)] was recorded in the medium containing a 0.5× concentration of NH₄NO₃, and the highest production of withanolide A content was recorded in the medium with 2.0× KNO₃ (4.36 mg g⁻¹ DW). The NH₄ ⁺/NO₃ ⁻ ratio also influenced cell growth and withanolide A production, with both parameters being larger when the NO₃ ⁻ concentration was higher than that of NH₄ ⁺. Maximum biomass growth (110.45 g l⁻¹ FW and 9.29 g l⁻¹ DW) was achieved at an NH₄ ⁺/NO₃ ⁻ ratio of 7.19/18.80, while withanolide A production was greatest (3.96 mg g⁻¹ DW) when the NH₄ ⁺/NO₃ ⁻ ratio was 14.38/37.60 mM.     

Effect of nitrogen forms on growth,cell composition and N<Subscript>2</Subscript> fixation of <Emphasis Type="Italic">Cylindrospermopsis raciborskii</Emphasis> in phosphorus-limited chemostat cultures

The aim of this research was to test whether NH₄ ⁺ and NO₃ ⁻ affect the growth, P demand, cell composition and N₂ fixation of Cylindrospermopsis raciborskii under P limitation. Experiments were carried out in P-limited (200 μg l⁻¹ PO₄-P) chemostat cultures of C. raciborskii using an inflowing medium containing either 4,000 μg l⁻¹ NH₄-N, 4,000 μg l⁻¹ NO₃-N or no combined N. The results showed the cellular N:P and C:P ratios of C. raciborskii decreased towards the Redfield ratio with increasing dilution rate (D) due to the alleviation of P limitation. The cellular C:N and carotenoids:chlorophyll-a ratios also decreased with D, predominantly as a result of an increase in the chlorophyll-a and N content. The NH₄ ⁺ and NO₃ ⁻ supply reduced the P maintenance cell quota of C. raciborskii. Consequently, the biomass yield of the N₂-grown culture was significantly lower. The maximum specific growth rate of N₂-grown culture was also the lowest observed. It is suggested that these differences in growth parameters were caused by the P and energy requirement for heterocyte formation, nitrogenase synthesis and N₂ fixation. N₂ fixation was partially inhibited by NO₃ ⁻ and completely inhibited by NH₄ ⁺. It was probably repressed through the high N content of cells at high dissolved N concentrations. These results indicate that C. raciborskii is able to grow faster and maintain a higher biomass under P limitation where a sufficient supply of NH₄ ⁺ or NO₃ ⁻ is maintained. Information gained about the species-specific nutrient and pigment stoichiometry of C. raciborskii could help to access the degree of nutrient limitation in water bodies. Handling editor: Luigi Naselli-Flores     

Bioethanol production in batch mode by a native strain of <Emphasis Type="Italic">Zymomonas mobilis</Emphasis>

Two wild strains of Zymomonas mobilis were isolated (named as ML1 and ML2) from sugar cane molasses obtained from different farms of Santander, Colombia. Initially, selection of the best ethanol-producer strains was carried out using ethanol production parameters obtained with a commercial strain Z. mobilis DSM 3580. Three isolated strains were cultivated in a culture medium containing yeast extract, peptone, glucose and salts, at pH 6 and 32°C with stirring rate of 65 rpm during 62 h. The best results of ethanol production were obtained with the native strain ML1, reaching a maximum ethanol concentration of 79.78 g l⁻¹. ML1 and ML2 strains were identified as Z. mobilis, according to the morphology, biochemical tests and molecular characterization by PCR of specific DNA sequences from Z. mobilis. Subsequently, the effect of different nitrogen sources on production of ethanol was evaluated. The best results were obtained using urea at a 0.73 g/l. In this case, maximum concentration of ethanol was 83.81 g l⁻¹, with kinetic parameters of yield of ethanol on biomass (Y_P/X) = 69.01(g g⁻¹), maximum volumetric productivity of ethanol (Qp_max) = 2.28 (g l⁻¹ h⁻¹), specific productivity of ethanol (q_P) = 3.54 (h⁻¹) and specific growth rate (μ) = 0.12 h⁻¹. Finally, we studied the effect of different culture conditions (pH, temperature, stirring, C/N ratio) with a Placket-Burman′s experimental design. This optimization indicated that the most significant variables were temperature and stirring. In the best culture conditions a significant increase in all variables of response was achieved, reaching a maximum ethanol concentration of 93.55 g l⁻¹.     

Continuous butanol production with reduced byproducts formation from glycerol by a hyper producing mutant of <Emphasis Type="Italic">Clostridium pasteurianum</Emphasis>

Butanol, a four-carbon primary alcohol (C₄H₁₀O), is an important industrial chemical and has a good potential to be used as a superior biofuel. Bio-based production of butanol from renewable feedstock is a promising and sustainable alternative to substitute petroleum-based fuels. Here, we report the development of a process for butanol production from glycerol, which is abundantly available as a byproduct of biodiesel production. First, a hyper butanol producing strain of Clostridium pasteurianum was isolated by chemical mutagenesis. The best mutant strain, C. pasteurianum MBEL_GLY2, was able to produce 10.8 g l⁻¹ butanol from 80 g l⁻¹ glycerol as compared to 7.6 g l⁻¹ butanol produced by the parent strain. Next, the process parameters were optimized to maximize butanol production from glycerol. Under the optimized batch condition, the butanol concentration, yield, and productivity of 17.8 g l⁻¹, 0.30 g g⁻¹, and 0.43 g l⁻¹ h⁻¹ could be achieved. Finally, continuous fermentation of C. pasteurianum MBEL_GLY2 with cell recycling was carried out using glycerol as a major carbon source at several different dilution rates. The continuous fermentation was run for 710 h without strain degeneration. The acetone–butanol–ethanol productivity and the butanol productivity of 8.3 and 7.8 g l⁻¹ h⁻¹, respectively, could be achieved at the dilution rate of 0.9 h⁻¹. This study reports continuous production of butanol with reduced byproducts formation from glycerol using C. pasteurianum, and thus could help design a bioprocess for the improved production of butanol.     

Dynamic microbial response under ethanol stress to monitor <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> activity in different initial physiological states

Dynamic Saccharomyces cerevisiae responses to increasing ethanol stresses were investigated to monitor yeast viability and to optimize bioprocess performance when gradients occurred due to the specific configuration of multi-stage bioreactors with cell recycling or of large volume industrial bioreactors inducing chemical heterogeneities. Twelve fed-batch cultures were carried out with initial ethanol concentrations (P _in) ranging from 5 g l⁻¹ to 110 g l⁻¹ with three different inoculums in different physiological states in terms of viability and quantity of ethanol produced (P _o). For a given initial cell viability of 50%, the time to reach the maximum growth rate and maximum ethanol production rate was dependent on the difference P _in − P _o. Whatever the initial physiological state, when the initial ethanol concentration P _in reached 100 g l⁻¹, the yeasts died. Experimental results showed that the initial physiological state of the yeast was the major parameter to determine, the microorganisms’ capacities to adapt and resist environmental changes.     

<Emphasis Type="Italic">Clostridium beijerinckii</Emphasis> mutant with high inhibitor tolerance obtained by low-energy ion implantation

Clostridium beijerinckii mutant strain IB4, which has a high level of inhibitor tolerance, was screened by low-energy ion implantation and used for butanol fermentation from a non-detoxified hemicellulosic hydrolysate of corn fiber treated with dilute sulfuric acid (SAHHC). Evaluation of toxicity showed C. beijerinckii IB4 had a higher level of tolerance than parent strain C. beijerinckii NCIMB 8052 for five out of six phenolic compounds tested (the exception was vanillin). Using glucose as carbon source, C. beijerinckii IB4 produced 9.1 g l⁻¹ of butanol with an acetone/butanol/ethanol (ABE) yield of 0.41 g g⁻¹. When non-detoxified SAHHC was used as carbon source, C. beijerinckii NCIMB 8052 grew well but ABE production was inhibited. By contrast, C. beijerinckii IB4 produced 9.5 g l⁻¹ of ABE with a yield of 0.34 g g⁻¹, including 2.2 g l⁻¹ acetone, 6.8 g l⁻¹ butanol, and 0.5 g l⁻¹ ethanol. The remarkable fermentation and inhibitor tolerance of C. beijerinckii IB4 appears promising for ABE production from lignocellulosic materials.     

Fungal autolysate as a nutrient supplement for ethanol and chitosan production by <Emphasis Type="Italic">Mucor indicus</Emphasis>

Mucor indicus can be used to produce ethanol from a variety of sugars, including pentose’s. An extract of it, produced by autolysis, could replace yeast extract in culture medium with improved production of ethanol. At 10 g l⁻¹, the extract gave a higher ethanol yield (0.47 g g⁻¹) and productivity (0.71 g l⁻¹ h⁻¹) compared to medium containing yeast extract (yield 0.45 g g⁻¹; productivity 0.67 g l⁻¹ h⁻¹).     

Ethanol and xylitol production from glucose and xylose at high temperature by <Emphasis Type="Italic">Kluyveromyces</Emphasis> sp. IIPE453

A yeast strain Kluyveromyces sp. IIPE453 (MTCC 5314), isolated from soil samples collected from dumping sites of crushed sugarcane bagasse in Sugar Mill, showed growth and fermentation efficiency at high temperatures ranging from 45°C to 50°C. The yeast strain was able to use a wide range of substrates, such as glucose, xylose, mannose, galactose, arabinose, sucrose, and cellobiose, either for growth or fermentation to ethanol. The strain also showed xylitol production from xylose. In batch fermentation, the strain showed maximum ethanol concentration of 82 ± 0.5 g l⁻¹ (10.4% v/v) on initial glucose concentration of 200 g l⁻¹, and ethanol concentration of 1.75 ± 0.05 g l⁻¹ as well as xylitol concentration of 11.5 ± 0.4 g l⁻¹ on initial xylose concentration of 20 g l⁻¹ at 50°C. The strain was capable of simultaneously using glucose and xylose in a mixture of glucose concentration of 75 g l⁻¹ and xylose concentration of 25 g l⁻¹, achieving maximum ethanol concentration of 38 ± 0.5 g l⁻¹ and xylitol concentration of 14.5 ± 0.2 g l⁻¹ in batch fermentation. High stability of the strain was observed in a continuous fermentation by feeding the mixture of glucose concentration of 75 g l⁻¹ and xylose concentration of 25 g l⁻¹ by recycling the cells, achieving maximum ethanol concentration of 30.8 ± 6.2 g l⁻¹ and xylitol concentration of 7.35 ± 3.3 g l⁻¹ with ethanol productivity of 3.1 ± 0.6 g l⁻¹ h⁻¹ and xylitol productivity of 0.75 ± 0.35 g l⁻¹ h⁻¹, respectively.     

Succinic acid production from sugarcane bagasse hemicellulose hydrolysate by <Emphasis Type="Italic">Actinobacillus succinogenes</Emphasis>

Succinic acid, a four-carbon diacid, has been the focus of many research projects aimed at developing more economically viable methods of fermenting sugar-containing natural materials. Succinic acid fermentation processes also consume CO₂, thereby potentially contributing to reductions in CO₂ emissions. Succinic acid could also become a commodity used as an intermediate in the chemical synthesis and manufacture of synthetic resins and biodegradable polymers. Much attention has been given recently to the use of microorganisms to produce succinic acid as an alternative to chemical synthesis. We have attempted to maximize succinic acid production by Actinobacillus succinogenes using an experimental design methodology for optimizing the concentrations of the medium components. The first experiment consisted of a 2⁴⁻¹ fractional factorial design, and the second entailed a Central Composite Rotational Design so as to achieve optimal conditions. The optimal concentrations of nutrients predicted by the model were: NaHCO₃, 10.0 g l⁻¹; MgSO₄, 3.0 g l⁻¹; yeast extract, 2.0 g l⁻¹; KH₂PO₄. 5.0 g l⁻¹; these were experimentally validated. Under the best conversion conditions, as determined by statistical analysis, the production of succinic acid was carried out in an instrumented bioreactor using sugarcane bagasse hemicellulose hydrolysate, yielding a concentration of 22.5 g l⁻¹.     

Enhanced decolourization of Direct Red-80 dye by the white rot fungus <Emphasis Type="Italic">Phanerochaete chrysosporium</Emphasis> employing sequential design of experiments

Decolourization of Direct Red 80 (DR-80) by the white rot fungus Phanerochaete chrysosporium MTCC 787 was investigated employing sequential design of experiments. Media components for growing the white rot fungus were first screened using Plackett-Burman design and then optimized using response surface methodology (RSM), which resulted in enhancement in the efficiency of dye removal by the fungus. For determining the effect of media constituents on the dye removal, both percent dye decolourization and specific dye removal due to maximum enzyme activity were chosen as the responses from the experiments, and the media constituents glucose, veratryl alcohol, KH₂PO₄, CaCl₂ and MgSO₄ were screened to be the most effective with P values less than 0.05. Central composite design (CCD) followed by RSM in the optimization study revealed the following optimum combinations of the screened media constituents: glucose, 11.9 g l⁻¹; veratryl alcohol, 12.03 mM; KH₂PO₄, 23.08 g l⁻¹; CaCl₂, 2.4 g l⁻¹; MgSO₄, 10.47 g l⁻¹. At the optimum settings of the media constituents, complete dye decolourization (100% removal efficiency) and a maximum specific dye removal due to lignin peroxidase enzyme of 0.24 mg U⁻¹ by the white rot fungus were observed.     

Influence of nutritional conditions on exopolysaccharide production by submerged cultivation of the medicinal fungus <Emphasis Type="Italic">Shiraia bambusicola</Emphasis>

Maltose and yeast extract were the most favourable carbon and nitrogen sources for exopolysaccharide production by submerged culture of Shiraia bambusicola WZ-003, and initial maltose and yeast extract concentrations were at 30 and 3 g l⁻¹, respectively. Plant oils could increase the mycelial growth and exopolysaccharide production in tested concentration. K⁺ and Mg²⁺ could enhance the mycelial growth and exopolysaccharide biosynthesis. The optimal cultivation temperature and initial pH were found to be 26°C and 6.0, respectively. Exopolysaccharide concentration reached 0.53 g l⁻¹ in 15-l fermenter under optimal nutritional conditions.     

Aerobic cometabolic degradation of trichloroethene by methane and ammonia oxidizing microorganisms naturally associated with <Emphasis Type="Italic">Carex comosa</Emphasis> roots

The degradation potential of trichloroethene by the aerobic methane- and ammonia-oxidizing microorganisms naturally associated with wetland plant (Carex comosa) roots was examined in this study. In bench-scale microcosm experiments with washed (soil free) Carex comosa roots, the activity of root-associated methane- and ammonia-oxidizing microorganisms, which were naturally present on the root surface and/or embedded within the roots, was investigated. Significant methane and ammonia oxidation were observed reproducibly in batch reactors with washed roots incubated in growth media, where methane oxidation developed faster (2 weeks) compared to ammonia oxidation (4 weeks) in live microcosms. After enrichment, the methane oxidizers demonstrated their ability to degrade 150 μg l⁻¹ TCE effectively at 1.9 mg l⁻¹ of aqueous CH₄. In contrast, ammonia oxidizers showed a rapid and complete inhibition of ammonia oxidation with 150 μg l⁻¹ TCE at 20 mg l⁻¹ of NH₄ ⁺-N, which may be attributed to greater sensitivity of ammonia oxidizers to TCE or its degradation product. No such inhibitory effect of TCE degradation was detected on methane oxidation at the above experimental conditions. The results presented here suggest that microorganisms associated with wetland plant roots can assist in the natural attenuation of TCE in contaminated aquatic environments.     

Atrazine degradation by a simple consortium of <Emphasis Type="Italic">Klebsiella</Emphasis> sp. A1 and <Emphasis Type="Italic">Comamonas</Emphasis> sp. A2 in nitrogen enriched medium

A simple consortium consisted of two members of Klebsiella sp. A1 and Comamonas sp. A2 was isolated from the sewage of a pesticide mill in China. One member of Klebsiella sp. A1 is a novel strain that could use atrazine as the sole carbon and nitrogen source. The consortium showed high atrazine-mineralizing efficiency and about 83.3% of 5 g l⁻¹ atrazine could be mineralized after 24 h degradation. Contrary to many other reported microorganisms, the consortium was insensitive to some nitrogenous fertilizers commonly used, not only in presence of 200 mg l⁻¹ atrazine but also in 5 g l⁻¹ atrazine mediums. After 24 h incubation, 200 mg l⁻¹ atrazine was completely mineralized despite of the presence of urea, (NH₄)₂CO₃ and (NH₄)₂HPO₄ in the medium. Very minor influence was observed when NH₄Cl was added as additional nitrogen source. Advantages of the simple consortium, high mineralizing efficiency and insensitivity to most of exogenous nitrogen sources, all suggested application potential of the consortium for the bioremediation of atrazine-contaminated soils and waters.     

Application of oscillation for efficiency improvement of continuous ethanol fermentation with Saccharomyces cerevisiae under very-high-gravity conditions

Compared with steady state, oscillation in continuous very-high-gravity ethanol fermentation with Saccharomyces cerevisiae improved process productivity, which was thus introduced for the fermentation system composed of a tank fermentor followed by four-stage packed tubular bioreactors. When the very-high-gravity medium containing 280 g l⁻¹ glucose was fed at the dilution rate of 0.04 h⁻¹, the average ethanol of 15.8% (v/v) and residual glucose of 1.5 g l⁻¹ were achieved under the oscillatory state, with an average ethanol productivity of 2.14 g h⁻¹ l⁻¹. By contrast, only 14.8% (v/v) ethanol was achieved under the steady state at the same dilution rate, and the residual glucose was as high as 17.1 g l⁻¹, with an ethanol productivity of 2.00 g h⁻¹ l⁻¹, indicating a 7% improvement under the oscillatory state. When the fermentation system was operated under the steady state at the dilution rate of 0.027 h⁻¹ to extend the average fermentation time to 88 h from 59 h, the ethanol concentration increased slightly to 15.4% (v/v) and residual glucose decreased to 7.3 g l⁻¹, correspondingly, but the ethanol productivity was decreased drastically to 1.43 g h⁻¹ l⁻¹, indicating a 48% improvement under the oscillatory state at the dilution rate of 0.04 h⁻¹.     

Production of tetramethylpyrazine by batch culture of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> with optimal pH control strategy

The effects of initial culture pH ranging from 5.0 to 7.5 on biomass content, precursor 3-hydroxy-2-butanone (HB) accumulation, and 2,3,5,6-tetramethylpyrazine (TTMP) formation by Bacillus subtilis CCTCC M 208157 were investigated in shake flask fermentation. Weak acidic conditions were found to favor cell growth and precursor HB accumulation, while TTMP could be synthesized more efficiently in conditions with initial pH towards neutrality. Batch bioprocess of TTMP fermentation by Bacillus subtilis CCTCC M 208157 at various controlled pH values ranging from 5.5 to 7.0 was then examined in 7.5-l fermentor. The results suggested that optimum pH for cell growth and precursor HB accumulation was 5.5 with maximum cell growth rate (Q _x) and precursor HB accumulation rate (Q _HB) of 0.833 g l⁻¹ h⁻¹ and 1.118 g l⁻¹ h⁻¹, respectively, while optimum pH for TTMP formation was 7.0 with maximum TTMP formation rate (Q _TTMP) of 0.095 g l⁻¹ h⁻¹. A pH-shifted strategy was accordingly developed to improve TTMP production in bioreactor fermentation by shifting the culture pH from 5.5 to 7.0 after 48 h of cultivation. By applying the strategy, final TTMP concentration of 7.43 g l⁻¹ was obtained, being 22.2% greater than that of constant-pH fermentation.     

Optimization and mechanism of diacetyl accumulation by <Emphasis Type="Italic">Enterobacter</Emphasis><Emphasis Type="Italic">aerogenes</Emphasis> mutant UV-3

A mutant designated as UV-3 was obtained from wild-type Enterobacter aerogenes 10293 through u.v. radiation. The activities of α-acetolactate decarboxylase (Ald), lactate dehydrogenase (Ldh) and diacetyl reductase (Dr) in UV-3 were strongly attenuated, with the lowest activities at pH 7.0–7.5, and temperature between 36 and 39°C. Compared to the wild-type, the yield of diacetyl by UV-3 was increased 18.7-fold, up to 1.05 ± 0.01 g l⁻¹. Acetoin and ethanol productions were decreased by 48.4 and 71.4%, respectively, but acetate yield was increased by 34.6%. Optimum medium for diacetyl production by UV-3 contained 10% glucose, 0.5% peptone, 0.5% yeast extract powder, 0.01% (NH₄)₂SO₄, 0.1% citric acid, 0.2% MnSO₄ and 0.2% MgSO_4, and this was determined by one-factor-at-a-time approach. Data from the five level central composite designs demonstrated that initial pH of 7.0, temperature of 37°C and rotational speed of 180 rev/min were optimum processing parameters for diacetyl production. The maximum yield of diacetyl could reach 1.35 g l⁻¹ in a 5-l bioreactor. These results showed an enhancement of the non-enzymatic oxidative decarboxylation of α-acetolactate and a decrease in the activities of Ald, Ldh and Dr as a consequence of diacetyl accumulation in UV-3.     

Optimization of a chemically defined medium for mycelial growth and polysaccharide production by medicinal mushroom <Emphasis Type="Italic">Phellinus igniarius</Emphasis>

A chemically defined medium for mycelial growth and exopolysaccharide (EPS) production by submerged culture of Phellinus igniarius was investigated. The mainly defined medium compositions were optimized by using orthogonal matrix method. The optimal defined medium (per liter) was 40.0 g glucose, 4.0 g. glutamic acid, 4.0 g (NH₄)₂SO₄, and initial pH 6.0. Under the optimal medium, the maximal mycelial biomass and EPS production were 12.33 ± 0.89 and 1.21 ± 0.08 g l⁻¹ at 192 h in shake flask, while the maximal mycelial biomass and EPS production reached 13.86 ± 0.52 and 1.92 ± 0.07 g l⁻¹ at 168 h in 3 l fermenter, respectively. The molecular weights (g mol⁻¹) of four fractions isolated from EPS by gel permeation were about 6.4 × 10⁶, 3.3 × 10⁵, 2.7 × 10⁵ and 2.9 × 10³. This study should be widely applied to other secondary metabolites production from higher fungus in a chemically defined medium and quantitative regulation of the metabolic flux in polysaccharide biosynthesis.     

Increase of lycopene production by supplementing auxiliary carbon sources in metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

In the fed-batch culture of glycerol using a metabolically engineered strain of Escherichia coli, supplementation with glucose as an auxiliary carbon source increased lycopene production due to a significant increase in cell mass, despite a reduction in specific lycopene content. l-Arabinose supplementation increased lycopene production due to increases in cell mass and specific lycopene content. Supplementation with both glucose and l-arabinose increased lycopene production significantly due to the synergistic effect of the two sugars. Cell growth by the consumption of carbon sources was related to endogenous metabolism in the host E. coli. Supplementation with l-arabinose stimulated only the mevalonate pathway for lycopene biosynthesis and supplementation with both glucose and l-arabinose stimulated synergistically only the mevalonate pathway. In the fed-batch culture of glycerol with 10 g l⁻¹ glucose and 7.5 g l⁻¹ l-arabinose, the cell mass, lycopene concentration, specific lycopene content, and lycopene productivity after 34 h were 42 g l⁻¹, 1,350 mg l⁻¹, 32 mg g cells⁻¹, and 40 mg l⁻¹ h⁻¹, respectively. These values were 3.9-, 7.1-, 1.9-, and 11.7-fold higher than those without the auxiliary carbon sources, respectively. This is the highest reported concentration and productivity of lycopene.     

Controlling the oxidoreduction potential of the culture of <Emphasis Type="Italic">Clostridium acetobutylicum</Emphasis> leads to an earlier initiation of solventogenesis,thus increasing solvent productivity

Fermentative production of solvents (acetone, butanol, and ethanol) by Clostridium acetobutylicum is generally a biphasic process consisting of acidogenesis and solventogenesis. We report that the biphasic metabolism of C. acetobutylicum could be changed by oxidoreduction potential (ORP) regulation. When using air to control the ORP of the fermentation broth at −290 mV, an earlier initiation of solventogenesis was achieved. Solvent production reached 25.6 g l⁻¹ (2.8 g acetone l⁻¹, 16.8 g butanol l⁻¹, 6.0 g ethanol l⁻¹), a 35% increase compared with the ORP uncontrolled process. Metabolic flux analysis revealed that there was a general increase of the central carbon flux in the first 24 h of fermentation when ORP was controlled at −290 mV, compared with the control. Specifically, the solvent ratio (acetone:butanol:ethanol) was changed from 25:64:11 to 11:66:23 at ORP level of −290 mV, which might have resulted from the rigidity at acetyl-CoA node and the flexibility at acetoacetyl-CoA and butyryl-CoA nodes in response to ORP regulation.