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.     

Process for the Stereoselective Biotransformation of Acetoacetic Acid Esters Using Yeasts

A process for the stereospecific reduction of acetoacetic acid esters to the 3-(S)-hydroxy-butanoic acid esters by the yeasts Saccharomyces cerevisiae and Candida utilis grown on glucose and ethanol media was developed. A continuous single stage steady state production system was found to be superior to pulse-, batch- and fed-batch systems in terms of optical product purity, biomass concentration and production rates.

Optical purity of 3-(S)-hydroxybutanoic acid esters produced with Saccharomyces cerevisiae and Candida utilis was dependent on pH. A maximal optical purity was obtained at pH2.2 from S. cerevisiae growing on ethanol medium. The specific product formation rate of the chemostat cultures was 0.02…0.05 gg^?1 h^?1. C. utilis was more productive than S. cerevisiae but it reconsumed the product under carbon limited growth conditions.     

Isolation and purification of a new protease from Aspergillus niger LCF no 9

Summary Aspergillus niger LCF N ^o 9 synthesizes large amounts of a semi-alkaline protease highly active on Benzoyl arginine p-nitroanilide (BAPNA) that is likely to find industrial use. An industrial-grade enzyme of around 80% purity was prepared and a reference enzyme was obtained in high yield from the industrial product by ultrafiltration and HPIEC on a mono Q column. The industrial-grade enzyme was produced on a pilot scale with a yield of 0.52% of medium solid starting material by adsorption on CM-Sephadex A₅₀, precipitation with acetone at –30°C, ion-exchange chromatography on DEAE-Sepharose and diafiltration.     

Regulatory flexibility of methylotrophic yeasts in chemostat cultures: Simultaneous assimilation of glucose and methanol at a fixed dilution rate

The influence of the composition of methanol/glucose-mixtures as only sources of carbon and energy on growth and regulation of the synthesis of enzymes involved in methanol-dissimilation was studied under chemostat conditions at a fixed dilution rate with the methylotrophic yeasts Hansenula polymorpha and Kloeckera sp. 2201. Both carbon sources were found to be utilized completely independently of the composition of the C₁/C₆ mixture. Using mixtures of ¹⁴C-labelled methanol and glucose the growth yield for glucose was found to be constant for all C₁/C₆-mixtures tested and both yeasts. The growth yield for methanol, however, was reduced by up to 25% when the proportion of methanol in the inflowing medium was lower than 20% (w/w with respect to glucose) for H. polymorpha and 50% (w/w with respect to glucose) for Kloeckera sp. 2201 respectively. During growth with C₁/C₆-mixtures containing higher C₁-proportions of methanol regular growth yields for methanol were recorded which corresponded to the growth yields found with methanol as the only carbon source.The regulation of the synthesis of the enzymes of the dissimilatory pathway for methanol was found to be under multiple control. Although glucose was present in the medium methanol had a positive effect on the synthesis of these enzymes. Thus, in addition to derepression induction by methanol was also observed. This inductive effect was found to increase with increasing proportions of methanol in the mixture. Depending on the enzyme, 10–40% methanol in the mixture resulted in a maximal induction with enzyme specific activities equal to those found in cells grown with methanol as the only carbon source. No further enhancements in enzyme specific activities were observed during growth on mixtures containing more than 40% methanol.Abbreviations and terms C₁ Methanol - C₆ glucose - C₁/C₆ mixture compositions are given in % (w/w) - C₀ concentration of ¹⁴C in the inflowing medium (DPM ml^-1) - C(t) concentration of ¹⁴C incorporated in cells as a function of time t (DPM ml^-1) - d dilution rate (h^-1) - DPM disintegrations per minute - q _s q _C1 and q _C6 are specific rates of consumption of substrate, methanol and glucose respectively [g (g cell dry weight)^-1 h^-1] - q _O2 and q _CO2 are the specific rates of oxygen consumption and carbon dioxide release [mmol (g cell dry weight)^-1 h^-1] - RQ respiration quotient (q _CO2 q _O2 ^-1) - s _C1 and s _C6 are the residual concentrations of methanol and glucose in the culture liquid (g l^-1) - s _O/C1 and s _O/C6 are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - Sp.A. enzyme specific activity - x cell dry weight concentration (g l^-1) - Y _X/C1 and Y _X/C6 are growth yields on methanol and glucose respectively (g cell dry weight (g substrate)^-1 - Y _C/C1 growth yield with methanol with respect to carbon (g carbon assimilated (g carbon supplied)^-1 - _m maximum specific growth rate (h^-1)     

Pilot-Scale Fermentation and Purification of the Recombinant Allophycocyanin Over-Expressed in <Emphasis Type="Italic">Escherichia coli</Emphasis>

A recombinant allophycocyanin (rAPC), used for treatment of tumors, has been expressed in E. coli which was grown in glucose fed-batch culture in a 30 l fermentor. Recombinant allophycocyanin was purified from soluble E. coli cell lysate using hydrophobic interaction chromatography followed by chromatography using amylose affinity column. The purity of product was greater than 98% and yielded an average of 5.5 g kg⁻¹ dry cells. Recombinant allophycocyanin significantly inhibited H₂₂ hepatoma (p ( 0.01) in mice with inhibition rates ranging from 36% to 62% with doses from 6.25 to 50 mg kg⁻¹ d⁻¹.     

Diacetyl production and growth of Lactobacillus rhamnosus on multiple substrates

Lactobacillus rhamnosus is a heterolactic acid bacterium, which can be used to produce flavour compounds like diacetyl and acetoin. Various startegies have been applied to improve the growth rate and diacetyl yield. The use of multiple substrates affected growth as well as the yield of diacetyl. Growth on a medium containing glucose demonstrated a diauxic growth profile, with the second phase of growth being on the product, lactic acid. L. rhamnosus also grew on a medium containing citrate. Growth on medium containing glucose+citrate demonstrated simultaneous utilization of carbon sources. L. rhamnosus did not grow in a medium containing acetate and also did not co-metabolize it with glucose. Maximum specific growth rate ( _max) was found to increase in the case of simultaneous utilization of glucose+citrate (0.38 h^–1) as compared to glucose as the sole carbon source (0.28 h^–1). The yields of diacetyl were also found to increase for glucose + pyruvate and glucose + citrate (0.10 and 0.05 g g^–1 of glucose, respectively) as compared to glucose alone (0.01 g g^–1 of glucose). The productivity of diacetyl on medium containing glucose and citrate was double that of a medium containing only citrate, although the yields were comparable.     

CHARACTERIZATION OF BLEACHING IN CHLORELLA INDUCED BY SUBOPTIMAL GROWTH TEMPERATURES1

Incubation of cultures of a high-temperature strain of chlorella at 10 C stopped growth and bleached all chlorophyll in the cells in 24 hr. Optimal conditions of light (3.0 mw/cm²), gas (1% CO₂-in-air), and inorganic medium for maximal growth at 39 C were maintained in the transfer from 39 to 12, 10, or 5 C. The bleaching process at 10 C is characterized by a lag period for the first few hours followed by a linear decrease in chlorophyll content of cultures. The amounts of time required to bleach half of the chlorophyll initially present (effective half-times) at 10 C were 14 hr for chlorophyll a and 17 hr for chlorophyll b. Effective half-times of bleaching for total chlorophyll were 47 hr at 12 C and 6 hr at 5 C. Addition of glucose to inorganic medium delayed but did not prevent bleaching. Use of argon gas instead, of 1% CO₂-in-air prevented cells from bleaching in both inorganic and glucose media, and indicated an oxygen requirement for bleaching. Incubation of 6 additional strains of Chlorella at 10 C resulted in responses ranging from bleaching to no growth to growth.     

Production of a Novel Extracellular Polysaccharide by a Bacillus Strain Isolated from Soil

A bacterium that was isolated from soil and identified as Bacillus circulans was found to produce a highly viscous extracellular polysaccharide when it was grown aerobically in a medium containing glucose as a sole source of carbon. The product was characterized by TLC and GC analyses as a novel heteropolysaccharide consisted of rhamnose, mannose, galactose, and mannuronic acid as sugar components. A maximal yield of polysaccharide reached about 2 g/liter by jar-fermentor culture at 30°C for 48 hr with a medium containing 1% glucose, 0.05% asparagine, 0.005% yeast extract, and small amounts of inorganic salts. Some culture conditions for the production of polysaccharide were investigated with flask culture; an optimal production was attained with a medium containing 0.1–1 % glucose and 0.01–0.05% asparagine, pH 7–8, at 30°C under aerobic conditions.     

The white-rot fungus Cerrena unicolor strain 137 produces two laccase isoforms with different physico-chemical and catalytic properties

Cerrena unicolor secreted two laccase isoforms with different characteristics during the growth in liquid media. In a synthetic low-nutrient nitrogen glucose medium (Kirk medium), high amounts of laccase (4,000 U l⁻¹) were produced in response to Cu²⁺. Highest laccase levels (19,000 U l⁻¹) were obtained in a complex tomato juice medium. The isoforms (Lacc I, Lacc II) were purified to homogeneity with an overall yield of 22%. Purification involved ultrafiltration and Mono Q separation. Lacc I and II had M _w of 64 and 57 kDa and pI of 3.6 and 3.7, respectively. Both isoforms had an absorption maximum at 608 nm but different pH optima and thermal stability. Optimum pH ranged from 2.5 to 5.5 depending on the substrate. The pH optima of Lacc II were always higher than those of Lacc I. Both laccases were stable at pH 7 and 10 but rapidly lost activity at pH 3. Their temperature optimum was around 60°C, and at 5°C they still reached 30% of the maximum activity. Lacc II was the more thermostable isoform that did not lose any activity during 6 months storage at 4°C. Kinetic constants (K _m, k _cat) were determined for 2,2′-azino-bis(3-ethylthiazoline-6-sulfonate) (ABTS), 2,6-dimethoxyphenol and syringaldazine.     

Biodegradation of phenanthrene by Arthrobacter polychromogenes isolated from a contaminated soil

Summary Degradation of phenanthrene by Arthrobacter polychromogenes isolated from a contaminated soil was investigated. In experiments in which [9-¹⁴C]-phenanthrene was incubated with cultures of A. polychromogenes containing 150 mg phenanthrene/l it was shown that after 26 h of incubation 47.7% of the recovered radiolabelled carbon originally present was metabolized to ¹⁴CO₂, 47.8% was recovered from the aqueous fraction, and 4.5% remained in the dichloromethane fraction. Increasing phenanthrene concentration in the culture medium resulted in improved growth and degradation rates, probably due to the higher amount of phenanthrene crystals in the medium. Shifting the temperature from 30°C to 35°C did not influence phenanthrene degradation significantly but inhibited cell division of A. polychromogenes. Medium supplementation with glucose led to stimulation of phenanthrene degradation at low amounts of glucose (0.45 g/l) whereas at higher concentrations (3 g/l) phenanthrene mineralization decreased.Professor Dr. D. Behrens dedicated to his 65th birthdayOffprint requests to: H.-J. Rehm     

Formation and identification of trimethylimidazole during tetramethylpyrazine production from glucose by <Emphasis Type="Italic">Bacillus</Emphasis> strains

During 2,3,5,6-tetramethylpyrazine production from glucose by Bacillus strains, a novel product was detected and identified as 2,4,5-trimethylimidazole (TMI) by GC/MS. TMI appeared in the culture medium only after glucose had been depleted and then increased to 0.25–0.31 g l⁻¹ in 90–120 h. When the ammonium source was changed from (NH₄)₂SO₄ to (NH₄)₂HPO₄, only about one tenth of TMI was detected. Although the mechanistic events largely remain unclear, both microbial strains tested demonstrated similar dynamic processes of TMI production, suggesting that TMI formation is a genuine feature of Bacillus species. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Screening of lipid high producing mutant from rhodotorula glutinis by low ion implantation and study on optimization of fermentation medium

In order to obtain lipid producing strain with high-yield, the wild type stain Rhodotorula glutinis was treated by low ion implantation, and optimization of fermentation medium for higher lipid yield was carried out using mutant strain. It was found that the strain had a higher positive mutation rate when the output power was 10 keV and the dose of N⁺ implantation was 80 × 2.6 × 10¹³ ions/cm². Then a high-yield mutant strain D30 was obtained through cid-heating coupling ultrasonic method and lipid yield was 3.10 g/L. Additionally, the surface response method was used to optimize fermentation medium. The three significant factors (glucose, peptone, KH₂PO₄) were optimized using response surface methodology (RSM), and the optimized parameters of fermentation medium were as follows: glucose 73.40 g/L, peptone 1.06 g/L and KH₂PO₄ 3.56 g/L. Finally the fermentation characteristic of high-yield mutation strain D30 was studied, when fermentation time was 10 days, which lipid yield increased to 7.81 g/L. Fatty acid composition of the lipid was determined by GC, and the most represented fatty acids of mutant D30 were C16:0 (11.4 %), C16:1 (5.66 %), C18:1 (49.3 %), and C18:2 (27.0 %).     

Effect of Darkness on Growth and Flowering of Chenopodium rubrum and C. murale Plants in vitro

Chenopodium rubrum, a short-day plant, and C. murale, a long-day plant, were grown in vitro in continuous darkness. Control C. rubrum plants exposed to continuous darkness for 15 d at cotyledonary phase, did not flower, while 80 % of plants flowered on the medium with 5 % glucose and 10 mg dm⁻³ GA₃. Control C. murale plants exposed to continuous darkness for 10 d at the age of 4^th pair of leaves, did not flower, while GA₃ (1 – 5 mg dm⁻³) stimulated flowering up to 65 %. This revised version was published online in July 2006 with corrections to the Cover Date.     

Growth and β-Glucan 10C3K Production by a Mutant of Alcaligenes faecalis var. myxogenes in Defined Medium

A defined medium was developed in which Alcaligenes faecalis var. myxogenes 10C3 mutant K produced a large quantity of β-glucan 10C3K. The medium contained 4% glucose together with 0.1% citrate, succinate or fumarate as the carbon source, 0.15% (NH₄)₂HPO₄ as the nitrogen source and mineral salts. When NaNH₄HPO₄, KNO₃ or urea was used at a concentration of 0.03% nitrogen as the sole nitrogen source, salts of organic acid were not needed in addition to glucose.

In culture medium containing phosphate buffer (M/15, pH 6.5~8.0) large amounts of polysaccharide were formed and its yield from the 4% glucose added was about 50%. Thus, it was shown that polysaccharide production is enhanced greatly if a suitable pH for polysaccharide production is maintained during incubation.     

Production and Characterization of an Exopolysaccharide by Yeast

Antarctic yeast strains were investigated for exopolysaccharide biosynthesis and the Sporobolomyces salmonicolor AL₁ strain was selected. It was studied for exopolysaccharide biosynthesis on different carbon and nitrogen sources. The investigations showed that sucrose and ammonium sulphate were suitable culture medium components for polymer biosynthesis. Exopolysaccharide formation by the yeast strain was accompanied by a decrease in the culture medium pH value from the initial pH 5.3 to pH 1.7–2.0. During the biosynthetic process, the dynamic viscosity of the culture broth increased to the maximum value of 15.37 mPas and the polysaccharide yield reached 5.63 g/l on a culture medium containing 5.00% sucrose and 0.25% ammonium sulphate at a temperature of 22 °C for 120 h. The crude polysaccharide obtained from Sp. salmonicolor AL₁ featured high purity (90.16% of carbon content) and consisted of glucose (54.1%), mannose (42.6%) and fucose (3.3%). Pure mannan containing 98.6% of mannose was isolated from it.     

Contribution of Extracellular Glutamine as An Anaplerotic Substrate to Neuronal Metabolism: A Re-Evaluation by Multinuclear NMR Spectroscopy in Primary Cultured Neurons

Multinuclear NMR spectroscopy is used to investigate the effect of glutamine on neuronal glucose metabolism. Primary neurons were incubated with [1-¹³C]glucose in the absence or presence of glutamine (2 mM) and/or NH₄Cl (5 mM). After ammonia-treatment, the concentrations of high-energy phosphates decreased up to 84% of control, which was aggravated in glutamine-containing medium (up to 42% of control). These effects could not be attributed to changes in mitochondrial glucose oxidation. Withdrawal of glutamine decreased amino acid concentrations, e.g. of glutamate to 53%, but also considerably lessened the ¹³C enrichment in [4-¹³C]glutamate to 8.3% of control, and decreased the ¹³C-enrichment in acetyl-CoA entering the Krebs cycle (P<0.001). Thus, although glutamine is potent in replenishing neuronal glutamate stores, glutamate formation is mainly attributed to its de novo synthesis from glucose. Furthermore, mitochondrial glucose metabolism strongly depends on the supply of carbons from glutamine, indicating that exogenous glutamine is a well-suited substrate to replenish neuronal Krebs cycle intermediates.     

High-yield fermentative preparation of tetramethylpyrazine by Bacillus sp. using an endogenous precursor approach

A spore-forming Bacillus sp. was isolated from a high-temperature Daqu, a starter culture of Chinese Maotai-flavor liquor, using an endogenous precursor screening strategy. The Bacillus sp. was capable of producing a high level of 2,3,5,6-tetramethylpyrazine (TTMP) via a precursor of 3-hydroxy-2-butanone (HB). The strain was characterized as Bacillus subtilis based on morphological, physiological, and biochemical properties as well as on partial 16S rRNA gene sequences. Different carbon and nitrogen sources as well as fermentation conditions were investigated. Optimization tests showed that oxygen supply and fermentation temperature were the most important parameters determining the production process. The production of >4.08 g/l TTMP was achieved together with a high level of endogenous precursor HB accumulation (>20 g/l) in both flask and fermentor cultures when the optimized medium and cultivation conditions were applied. Our data demonstrates the effectiveness of the endogenous precursor strategy for screening microorganisms that produce flavor compounds with structure-related precursors. The high yield of TTMP and the inexpensiveness of the agro-industrial product used as the substrate (soybean meal) indicate the potential of this process for industrial application.     

The dynamics of neutral sugars in the rhizosphere of wheat. An approach by13C pulse-labelling and GC/C/IRMS

Rhizodeposition, i.e. the release of carbon into the soil by growing roots, is an important part of the terrestrial carbon cycle. However thein situ nature and dynamics of root-derived carbon in the soil are still poorly understood. Here we made an investigation of the latter in laboratory experiments using¹³CO₂ pulse chase labelling of wheat (Triticum aestivum L.). We analyzed the kinetics of¹³C-labelled carbon and more specially¹³C carbohydrates in the rhizosphere. Wheat seedlings-soil mesocosms were exposed to¹³CO₂ for 5 hours in controlled chambers and sampled repeatedly during two weeks for¹³C/C analysis of organic carbon. After a two-step separation of the soil from the roots, the amount of total organic¹³C was determined by isotope ratio mass spectrometry as well as the amounts of¹³C in arabinose, fructose, fucose, glucose, galactose, mannose, rhamnose and xylose. The amount and isotopic ratio of monosaccharides were obtained by capillary gas chromatography coupled with isotope ratio mass spectrometry (GC/C/IRMS) after trimethyl-silyl derivatization. Two fractions were analyzed : total (hydrolysable) and soluble monomeric (water extractable) soil sugars. The amount of organic¹³C found in the soil, expressed as a percentage of the total photosynthetically fixed¹³C at the end of the labelling period, reached 16% in the day following labelling and stabilised at 9% after one week. We concluded that glucose under the form of polymers was the dominant moietie of rhizodeposits. Soluble glucose and fructose were also present. But after 2 days, these soluble sugars had disappeared. Forty percent of the root-derived carbon was in the form of neutral sugars, and exhibited a time-increasing signature of microbial sugars. The composition of rhizospheric sugars rapidly tended towards that of bulk soil organic matter.     

Effect of various carbon sources on microbial lipases biosynthesis

Summary The aim of these investigations was to study the conditions for the production of extracellular lipases fromPenicillium roqueforti S-86, which was isolated from a commercial sample of roqueforti chese type. As carbon sources there have been used the following compounds: 2% glucose, fructose and sucrosel 1% and 2% butterfat and 2% olive oil. Maximal amount of lipases was produced after six days of incubation grown in the medium with 2% of glucose, initial pH of medium 4.0 at 27°C. Cells ofPenicillium roqueforti grown in the presence of bacto-peptone instead of (NH₄)₂SO₄, as nitrogen source, synthesized maximum quantity of lipases after four days of incubation.The effect of temperature, pH, as well as mono, be and three valent cations: Na⁺, K⁺, Ca⁺⁺, Mn⁺⁺, Mg⁺⁺ and Fe⁺⁺⁺ on lipase activity was followed.     

Heterotrophic production of Chlorella sp. TISTR 8990—biomass growth and composition under various production conditions

The green microalga Chlorella sp. TISTR 8990 was grown heterotrophically in the dark using various concentrations of a basal glucose medium with a carbon‐to‐nitrogen mass ratio of 29:1. The final biomass concentration and the rate of growth were highest in the fivefold concentrated basal glucose medium (25 g L^?1 glucose, 2.5 g L^?1 KNO₃) in batch operations. Improving oxygen transfer in the culture by increasing the agitation rate and decreasing the culture volume in 500‐mL shake flasks improved growth and glucose utilization. A maximum biomass concentration of nearly 12 g L^?1 was obtained within 4 days at 300 rpm, 30°C, with a glucose utilization of nearly 76% in batch culture. The total fatty acid (TFA) content of the biomass and the TFA productivity were 102 mg g^?1 and 305 mg L^?1 day^?1, respectively. A repeated fed‐batch culture with four cycles of feeding with the fivefold concentrated medium in a 3‐L bioreactor was evaluated for biomass production. The total culture period was 11 days. A maximum biomass concentration of nearly 26 g L^?1 was obtained with a TFA productivity of 223 mg L^?1 day^?1. The final biomass contained (w/w) 13.5% lipids, 20.8% protein and 17.2% starch. Of the fatty acids produced, 52% (w/w) were saturated, 41% were monounsaturated and 7% were polyunsaturated (PUFA). A low content of PUFA in TFA feedstock is required for producing high quality biodiesel. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1589–1600, 2017