Effect of medium components and time of cultivation on chitin production by Mucor circinelloides (Mucor javanicus IFO 4570) -- a factorial study

Chitin production of mycelia from Mucor circinelloides (Mucor javanicus) was studied with a two-level factorial design in all combinations of the following factors in the culture medium: time of cultivation, concentration of D-glucose, L-asparagine and thiamine. Chitin was characterised by infrared and nuclear magnetic resonance spectroscopy. The four factors showed statistically significant (95%) positive main effects on chitin production, without interactions between them. The highest chitin yield (23.9%) was obtained with the medium containing 60 g/l of glucose, 3 g/l of asparagine and 0.008 mg/l of thiamine and is comparable to the highest in the literature.     

Co-production of lactic acid and chitin using a pelletized filamentous fungus Rhizopus oryzae cultured on cull potatoes and glucose

Aims: This paper developed a novel process for lactic acid and chitin co-production of the pelletized Rhzious oryzae NRRL 395 fermentation using underutilized cull potatoes and glucose as nutrient source. Methods and Results: Whole potato hydrolysate medium was first used to produce the highest pelletized biomass yield accompanying the highest chitin content in biomass. An enhanced lactic acid production then followed up using batch, repeated batch and fed batch culture with glucose as carbon source and mixture of ammonia and sodium hydroxide as neutralizer. The lactic acid productivity peaked at 2·8 and 3 g l⁻¹ h⁻¹ in repeated batch culture and batch culture, respectively. The fed batch culture had the highest lactate concentration of 140 g l⁻¹. Conclusions: Separation of the biomass cultivation and the lactic acid production is able to not only improve lactic acid production, but also enhance the chitin content. Cull potato hydrolysate used as a nutrient source for biomass cultivation can significantly increase both biomass yield and chitin content. Significance and Impact of the Study: The three-step process using pelletized R. oryzae fermentation innovatively integrates utilization of agricultural residues into the process of co-producing lactic acid and chitin, so as to improve the efficiency, revenues and cost of fungal lactic acid production.     

Chitin-glucan complex production by Schizophyllum commune submerged cultivation

Chitin-glucan complex is a fungal origin copolymer that finds application in medicine and cosmetics. Traditionally, the mycelium of Micromycetes is considered as an industrial chitin-glucan complex source. Basidiomycete Schizophyllum commune submerged cultivation for chitin-glucan complex production was studied. In different S. commune strains chitin-glucan complex composed 15.2 +/- 0.4 to 30.2 +/- 0.2% of mycelium dry weight. Optimized conditions for chitin-glucan complex production (nutrient medium composition in g/l: sucrose - 35, yeast extract - 4, Na2HPO4*12H2O - 2.5, MgSO4*7 H2O - 0.5; medium initial pH 6.5; aeration intensity 21 of air per 11 of medium; 144 hours of cultivation) resulted in 3.5 +/- 0.3 g/l complex yield. Redirection of fungal metabolism from exopolysaccharide synthesis to chitin-glucan complex accumulation was achieved most efficiently by aeration intensity increase. Chitin-glucan complex from S. commune had the structure of microfibers with diameter 1-2 microm, had water-swelling capacity of 18 g/g, and was composed of 16.63% chitin and 83.37% glucan with a degree of chitin deacetylation of 26.9%. S. commune submerged cultivation is a potent alternative to Micromycetes for industrial-scale chitin-glucan complex production.     

Solid-state cultivation of Bacillus thuringiensis R 176 with shrimp shells and rice straw as a substrate for chitinase production

In this study, shrimp shell powder, prepared by treating shrimp-processing waste by boiling and crushing, was used as a substrate for isolation of chitinase-producing microorganism. These organisms may have an important economic role in the biological control of rice and other fungal pathogens. Two hundred strains of bacteria with the ability to degrade chitin from shrimp shell waste were isolated from paddy soil, and of these, 40 strains showed chitinase activity in a solid state cultivation. One of the most potent isolates (strain R 176) was identified as Bacillus thuringiensis. Identification was carried out using morphological and biochemical properties along with 16S rRNA sequence analysis. This strain was able to produce high levels of extracellular chitinase in solid media containing shrimp shells as sole carbon source [1.36 U/g initial dry substrate (IDS)], which was 0.36-fold higher than the productivity in a liquid culture with colloidal chitin. The effects of medium composition and physical parameters on chitinase production by this organism were studied. The optimal medium contained shrimp shell mixed with rice straw in 1:1 ratio added with ball-milled chitin 0.5 % (w/v) and ammonium sulfate 0.5 % (w/v). The highest enzyme production (3.86 U/g IDS) by B. thuringiensis R 176 was obtained at pH 7, 37 °C after 14 days growth. With respect to the high amount of chitinase production by this strain in a simple medium, this strain could be a suitable candidate for the production of chitinase from chitinous solid substrates, and further investigations into its structure and characteristics are merited.     

Production of Alcaligenes xylosoxydans EMS33 in a Bench-scale Fermenter

Summary Optimization of medium composition and pH for chitinase production by the Alcaligenes xylosoxydans mutant EMS33 was carried out in the present study and the optimized medium composition and conditions were evaluated in a fermenter. The medium components screened initially using Plackett–Burman design were (NH₄)₂SO₄, MgSO₄ 7H₂O, KH₂PO₄, yeast extract, Tween 20 and chitin in shake flask experiments. The significant medium components identified by the Plackett–Burman method were MgSO₄ 7H₂O, Tween 20 and chitin. Central composite response surface methodology was applied to further optimize chitinase production. The optimized values of MgSO₄ 7H₂O, Tween 20, chitin and pH were found to be 0.6 g/l, 0.05 g/l, 11.5 g/l and 8.0, respectively. Chitinase and biomass production of Alcaligenes xylosoxydans EMS33, was studied in a 2-l fermenter containing (g/l): chitin, 11.5; yeast extract, 0.5; (NH₄)₂SO₄, 1; MgSO₄ 7H₂O, 0.6; KH₂PO₄, 1.36 and Tween 20, 0.05. The highest chitinase production was 54 units/ml at 60 h and pH 8.0 when the dissolved O₂ concentration was 60%, whereas the highest biomass production was achieved at 36 h and pH 7.5 without any dissolved O₂ control.     

Optimization of culture medium and growth conditions for production of L-arabinose isomerase and D-xylose isomerase by Lactobacillus bifermentans

Lactobacillus bifermentans was used to produce the intracellular enzymes L-arabinose isomerase and D-xylose isomerase. Various factors of cultivation (temperature, pH, or incubation period) and culture medium composition (mineral salts, carbon and nitrogen source) were studied to select the conditions that maximize production of these enzymes. Arabinose isomerase and xylose isomerase activities were 9.4 and 7.24 U/ml, respectively. They were highest at 9 h of cultivation in the optimized medium, 1.6 times higher than that in the basic MRS broth. The optimal medium composition and cultivation conditions were determined. On the other hand, the strain required for growth Tween 80 (1 g/l) and a source of inorganic nitrogen (e.g. ammonium citrate). The bacterium had no requirement for sodium acetate for both growth and production of isomerases. The production rate of enzymes was increased when metal ions were added and mainly manganese (2.5 mM).     

短小芽孢杆菌(Bacillus pumilus) WHK4以羽毛粉为底物产蛋白酶条件的优化

探索Bacillus pumilusWHK4以羽毛粉为底物产酶的最佳条件和最佳培养基组成。以羽毛粉发酵培养基为基础,首先采用单因子试验考察底物浓度、初始pH、接种量、外加碳源、外加氮源对WHK4产酶活力的影响。在单因子试验的基础上采用正交试验设计对底物浓度、温度、初始pH、接种量、外加(NH4)2SO4、外加麦芽糖进行优化。结果显示:Bacillus pumilusWHK4最佳的产酶条件为初始pH7.38,菌龄16 h,接种量5%,37℃。最佳的培养基组成为:1 L基础发酵培养基,40.0 g羽毛粉,10.0 g(NH4)2SO4和10.0 g麦芽糖。在优化的条件下Bacillus pumilusWHK4 24 h产蛋白酶活力为每毫升90 U。对培养条件和培养基的优化为Bacillus pumilusWHK4产蛋白酶的分离纯化奠定了基础。     

Optimization of culture medium and growth conditions for production of L-arabinose isomerase and D-xylose isomerase by <Emphasis Type="Italic">Lactobacillus bifermentans</Emphasis>

Lactobacillus bifermentans was used to produce the intracellular enzymes L-arabinose isomerase and D-xylose isomerase. Various factors of cultivation (temperature, pH, and incubation period) and culture medium composition (mineral salts, carbon source, and nitrogen source) were studied to select the conditions that maximize production of these enzymes. Arabinose isomerase and xylose isomerase activities were 9.4 and 7.24 U/ml, respectively. They were highest at 9 h of cultivation in the optimized medium, 1.6 times higher than that in the basic MRS broth. The optimal medium composition and cultivation conditions were determined. For optimal growth, the strain required Tween 80 (1 g/l) and a source of inorganic nitrogen (e.g., ammonium citrate). The bacterium had no requirement for sodium acetate for either growth or production of isomerases. The production rate of enzymes was increased when metal ions were added, primarily manganese (2.5 mM). The text was submitted by the authors in English.     

苏云金杆菌ZLL13晶体蛋白分析及其菌糠液态培养基的优化

食用菌栽培废料,简称菌糠(spent mushroom substrate, SMS)是食用菌栽培和生产的残留物,其含有丰富的甲壳素、木质纤维和蛋白质等,可为苏云金芽孢杆菌(Bacillus thuringiensis, Bt)的生长提供所需的营养物质。本研究以优化后的前处理条件制备的菌糠浸提液(2%硫酸, 121℃, 1 h)作为主要碳源,通过单因素试验、Plackett-Burman设计、最陡爬坡和响应面分析等方法来优化最佳培养基组分,结果表明,54%SMS浸提液,31.9 g/L大豆饼粉、0.88 g/L CaCO3、0.4 g/L MnSO4、0.5 g/L K2HPO4和0.4 g/L吐温100为最佳培养基配方,且优化后培养基(1.8×108/mL)产生的孢子数是原始SMS培养基(0.065×108/mL)的27倍,这不仅为菌糠的二次利用提供一种新的有效方法,而且也可以大大降低生产Bt所需要的发酵成本,具有良好的应用前景。     

Medium optimization for hen egg white lysozyme production by recombinant Aspergillus niger using statistical methods

Statistics-based experimental design was used to investigate the effect of medium components (starch, peptone, ammonium sulfate, yeast extract, and CaCl2.2H2O) on hen's egg white lysozyme production by Aspergillus niger HEWL WT-13-16. A 2(5-1) fractional factorial design augmented with center points revealed that peptone, starch, and ammonium sulfate were the most significant factors, whereas the other factors were not important within the levels tested. The method of steepest ascent was used to approach the proximity of optimum. This task was followed by a central composite design to develop a response surface for medium optimization. The optimum medium composition for lysozyme production was found to be: starch 34 g L-1, peptone 34 g L-1, ammonium sulfate 11.9 g L-1, yeast extract 0.5 g L-1, and CaCl2.2H2O 0.5 g L-1. This medium was projected to produce, theoretically, 212 mg L-1 lysozyme. Using this medium, an experimental maximum lysozyme concentration of 209+/-18 mg L-1 verified the applied methodology.     

Screening of pyruvate-producing yeast and effect of nutritional conditions on pyruvate production

AIMS: To find a yeast strain that can overproduce pyruvate and to investigate the effect of nutrients on pyruvate production. METHODS AND RESULTS: Trichosporon cutaneum PD70, a yeast strain that can overproduce pyruvate, was isolated from shake-flask cultures of 132 yeast strains. Pyruvate was measured by the HPLC or DNP method (see Materials and methods). Pyruvate production reached approximately 30.0 +/- 1.0 g l(-1) in basal fermentation medium. Different nutrient supplements had great effects on pyruvate production. Some of the conditions that gave the highest yield are described. CONCLUSIONS: Exogenous thiamine supplement caused a decrease in pyruvate yield. Some amino acids, such as L-arginine, L-isoleucine and L-valine, caused a minor increase in pyruvate yield. Soybean peptone was the most suitable nitrogen source for pyruvate production. A glucose concentration of 15% in fermentation medium gave the highest yield (34.6 g l(-1)) and the highest yield against consumed glucose (0.429 g g(-1)). SIGNIFICANCE AND IMPACT OF THE STUDY: Nutrients have significant impacts on pyruvate production. As a pyruvate overproducing yeast strain independent of exogenous vitamins or amino acids, T. cutaneum PD70 provides an advantage for commercial pyruvate production.     

Cell growth and enzyme synthesis of a mutant of Arthrobacter sp. (DSM 3747) used for the production of L-amino acids from D,L-5-monosubstituted hydantoins.

A microorganism with the ability to form L-tryptophan from D,L-5-(3-indolyl-methyl)hydantoin (D,L-5-IMH) was isolated and identified as Arthrobacter sp. (DSM 3747). After isolation of a mutant with high tryptophan production activity but low tryptophan degradation, cultural conditions were optimized to achieve high amounts of biomass with good specific activities concerning the enzymatic hydantoin-cleaving reactions. The ability of the microorganism to perform these bioconversions was found to be inducible by D,L-5-IMH as well as to be dependent on the presence of Mn2+. The highest specific D,L-5-IMH-cleaving activity of the cells was observed in the exponential phase of growth. The addition of yeast extract to the mineral salts medium was found to be essential for obtaining biomass concentrations of about 25 g l-1 cell dry mass by bioreactor cultivations. In order to obtain a constantly high growth rate, feeding of the C-source was pO2-controlled. The inducer D,L-5-IMH had to be continuously fed to prevent a decline of the L-tryptophan-forming enzyme activities, because it was subjected to degradation with the enzymes induced and higher concentrations of D,L-5-IMH aggravated the growth significantly. The synthesis of the enzymes was also inducible, when inducer and Mn2+ were not added until the late growth phase. Using this process, the consumption of D,L-5-IMH was reduced remarkably. So, under these conditions biomass concentrations of 25 g l-1 cell dry weight with a specific enzymatic activity of 0.20 mmol g-1 h-1 (tryptophan per dry mass per time) could be obtained within 13 h. Using 1 g l-1 of the chemically modified inducer D,L-5-(3-indolylmethyl)-3-N-methylhydantoin, which was not degradable by the microorganisms, a biomass concentration of 28 g l-1 cell dry weight with a specific activity of 0.34 mmol g-1 h-1 (tryptophan per dry mass per time) could be obtained within 28 h.     

南荻的组织培养与快速繁殖技术

以南荻幼穗为外植体,进行了组织培养与快速繁殖技术的研究。结果表明：最佳诱导培养基：MS＋2.0mg·L-12,4-D＋0.1mg·L-16-BA＋0.5g·L-1水解酪蛋白＋0.5g·L-1脯氨酸;最佳分化培养基：MS＋0.5mg·L-1NAA＋0.5mg·L-1KT＋0.5mg·L-1IAA＋2.0mg·L-16-BA＋0.5g·L-1水解酪蛋白＋0.5g·L-1脯氨酸;最佳生根培养基：MS＋1.0mg·L-1NAA＋0.25mg·L-1Met。炼苗后,移入营养土与珍珠岩（1：1）的基质中,移栽成活率高达100%。该体系的建立为南荻规模化生产及遗传改良提供了前提条件。     

Production of chitinolytic enzymes by a strain (BM17) of Paenibacillus pabuli isolated from crab shells samples collected in the east sector of central Tyrrhenian Sea

Nineteen bacterial isolates were grown in shaken cultures in media containing chitin as carbon source and different additional nitrogen sources such as yeast nitrogen base (YNB), yeast extract (YE), corn steep liquor (CSL) and ammonium sulfate. Strain BM17 showed the highest activity (200 U/l) in medium containing Chitin (1%) and YNB (0.5%). Molecular analysis of the 16S rRNA gene showed that strain BM17 belongs to the species Paenibacillus pabuli (99.72% homology). The enzyme activity started after 12-24 h; exponential enzyme production was recorded from the 24th h and lasted till the 96th h of incubation when activity peaked to decrease thereafter. Medium optimisation was carried out by Response Surface Methodology (RSM) considering the effects of chitin, corn steep liquor and yeast extract. BM17 chitinolytic activity was induced by chitin but the increase of its concentration did not have significant effects on the enzyme activity. By contrast, the nitrogen source, particularly YE, strongly affected the enzyme production.     

Effect of vitamin concentration on the synthesis of lactate, ethanol, pyruvate, and ethyl acetate in cells of the yeast Dipodascus magnusii

In the yeast Dipodascus magnusii, which is auxotrophic for thiamine and biotin, during cultivation on glucose with excessive thiamine concentration, pyruvate metabolism was shown to result in the synthesis of fermentation products, namely, ethanol and, to a lesser extent, lactate. Substantial synthesis of ethyl acetate was also observed under these conditions. Introduction of nicotinic acid (NA) into the medium resulted in time separation of ethanol and lactate production. It was shown that cultivation of the yeast under biotin deficiency resulted in nearly complete suppression of aerobic production of ethanol and cessation of ethyl acetate synthesis, whereas lactate synthesis was activated as early as in the first hours of cultivation. Upon introduction of NA under these conditions, lactate concentration sharply increased. These results show that the combination of thiamine and biotin with other vitamins can stimulate utilization of the pyruvate pool in yeasts towards formation of considerable amounts of lactate, which is typical only of cells of higher eukaryotes and bacteria.     

Production of Extracellular Polysaccharide by a Rhizobium Species from Root Nodules of the Leguminous Tree Dalbergia lanceolaria

The ability of the Rhizobium D1 10 species, which was isolated from the root nodules of the leguminous forest tree Dalbergia lanceolaria, for the production of extracellular polysaccharides (EPS) was investigated. High amounts of EPS (765 μg/mL) were produced by the bacteria (Rhizobium D1 10) in yeast extract mannitol medium. Both growth and EPS production started simultaneously, but the EPS production was at its maximum in the stationary phase of growth at 32 h. The EPS production was maximal when the medium was supplemented with mannitol (2 %), thiamine hydrochloride (1 μg/mL) and KNO₃ (0.1 %), which was accompanied by a great increase in the production compared to the control. The EPS contained xylose, rhamnose, glucose, galactose and arabinose. The possible role of rhizobial EPS production in root nodule symbiosis is discussed.     

Effect of environmental conditions on the expression levels of a recombinant 11S amaranth globulin in Escherichia coli

The expression in Escherichia coli strain Rosetta of the recombinant acidic subunit from the 11S amaranth seed storage protein (protein ACM3) was studied at flask and at bioreactor levels. This subunit was modified by inserting four Val-Tyr antihypertensive peptides in tandem into its third variable region and also with the tripeptide Ile-Pro-Pro in the Cterminal region. Flasks experiments allowed us to define the best conditions for the preparation and expression and accumulation of the protein ACM3, including the certainty of its presence within the cells especially as an insoluble fraction. The effects of cultivation temperature, aeration rate and agitation speed on the production of the protein ACM3 was tested in a 5-L batch bioreactor. Applying response surface methodology (RSM) we found that the aeration rate was the most significant factor affecting in a positively way the production yields and productivity of the recombinant protein. Temperature had effect only in conjunction to aeration. The highest recombinant acidic subunit concentration (747 mg L-1) and the highest productivity (186 mg L-1 h-1) were attained in 4 h of cultivation when the factors evaluated were controlled at its central values: 0.1 vvm, 300 rpm, and 30.5° C. Results from this study indicate that RSM is an effective technique to maximize the production of this recombinant protein.     

Effect of process parameters on succinic acid production in Escherichia coli W3110 and enzymes involved in the reductive tricarboxylic acid cycle

The effect of process optimization on succinic acid production by Escherichia coli W3110 and on enzymes involved in the reverse tricarboxylic acid cycle was studied. Approximately, 7.02 g L-1 of succinic acid was produced in 60 h at pH 7.0 in 500 mL anaerobic bottles containing 300 mL of the medium, wherein the sucrose concentration was 2.5%, the ratio of tryptone to ammonium hydrogen phosphate was 1:1, and the concentration of magnesium carbon ate was 1.5%. When these optimized fermentation conditions were employed in a 10 L bioreactor, 11.2 g L-1 of succinic acid was produced in 48 h. This is a 10-fold increase in succinic acid production from the initial titer of 0.94 g L-1. This clearly indicates the importance of process optimization, where by manipulating the media composition and production conditions, a remarkable increase in the production of the desired biomolecule can be obtained. The production of succinic acid is a multi-step reaction through the reverse tricarboxylic acid cycle. A linear relationship was observed between succinic acid production and the enzyme activities. The enzyme activities were found to increase in the order phospho-enol-pyruvate carboxylase相似文献   

Effect of phosphate supply and aeration on poly-β-hydroxybutyrate production in Azotobacter chroococcum

The effects of phosphate supply and aeration on cell growth and PHB accumulation were investigated in Azotobacter chroococcum 23 with the aim of increasing PHB production. Phosphate limitation favoured PHB formation in Azotobacter chroococcum 23, but inhibited growth. Azotobacter chroococcum 23 cells demonstrated intensive uptake of orthophosphate during exponential growth. At the highest phosphate concentration (1·5 g/litre) and low aeration the amount of intracellular orthophosphate/g residual biomass was highest. Under conditions of fed-batch fermentation the possibility of controlling the PHB production process by the phosphate level in the cultivation medium was demonstrated. A 36 h fed-batch fermentation resulted in a biomass yield of 110 g/litre with a PHB cellular concentration of 75% dry weight, PHB content 82·5 g/litre, PHB yield Y_P/S = 0·24 g/g and process productivity 2·29 g/litre·h.     

Xylanase production in solid state fermentation by Aspergillus niger mutant using statistical experimental designs

The initial moisture content, cultivation time, inoculum size and concentration of basal medium were optimized in solid state fermentation (SSF) for the production of xylanase by an Aspergillus niger mutant using statistical experimental designs. The cultivation time and concentration of basal medium were the most important factors affecting xylanase activity. An inoculum size of 5 x 10(5) spores/g, initial moisture content of 65%, cultivation time of 5 days and 10 times concentration of basal medium containing 50 times concentration of corn steep liquor were optimum for xylanase production in SSF. Under the optimized conditions, the activity and productivity of xylanase obtained after 5 days of fermentation were 5,071 IU/g of rice straw and 14,790 IU l(-1) h(-1), respectively. The xylanase activity predicted by a polynomial model was 5,484 IU/g of rice straw.