Lactose uptake rate by kefir yeast using C-labelled lactose to explain kinetic aspects in its fermentation

Τhe present work shows the relation between kefir fermentation ability and carbohydrate uptake rate. This was examined in a model system containing kefir co-culture and lactose in order to study fermentation induced by yeasts and bacteria at the same time. Lactose uptake rate was recorded by using ¹⁴C-labelled lactose. The effect of lactose, cell concentration and pH on lactose fermentation was examined. Results have shown increase of lactose uptake rate at lower cell concentrations and specifically the maximum values of lactose uptake rate were obtained at 30 °C, 5.5 pH value and initial lactose and cell concentration 10% w/v and 16 g/L, respectively. Likewise, lighten that the increase of the fermentation rate by immobilized cells can be attributed also, in addition to other factors, to lower cell concentration on the surface of the support or of the promoter. Besides, it is shown that the effect of pH value on the biochemical reactions, carried out by intracellular enzymes can be attributed, except to the effect of pH on enzyme ability, in addition to the effect of pH on carbohydrate uptake rate.     

16种茯苓菌株液体发酵产胞内多糖与三萜的比较研究

筛选茯苓高产胞内多糖和胞内三萜的优良液体发酵出发菌株。采用PDA富集固体平板培养与液体发酵培养测定菌丝体生长速率;采用液体发酵策略分析16种茯苓菌株产胞内多糖与胞内三萜的潜能。实验结果表明菌株生长于固体培养基与种子培养基的生长速率之间没有关联性;降低一级种子培养基初始pH值到4.0时能有效缓解茯苓菌株培养物褐化现象;AS5.137胞内多糖含量最高,达377.60±0.10 mg/g,而DB菌株显示出最高的胞内多糖产量,达1.01±0.13 g/L;Y1菌株胞内三萜含量最高,达83.89±4.28 mg/g,而Jingzhou28菌株胞内三萜产量最高,达136.63±26.66 mg/L。就生产茯苓胞内多糖与胞内三萜而言,AS5.137与DB菌株适合作为液体发酵产胞内多糖的出发菌株;Y1,Jingzhou28,Z(z)与Xingpinzhong菌株均较适合作为液体发酵产胞内三萜的出发菌株。     

Measurement and analysis of intracellular ATP levels in metabolically engineered Zymomonas mobilis fermenting glucose and xylose mixtures

Intracellular adenosine-5'-triphosphate (ATP) levels were measured in a metabolically engineered Zymomonas mobilis over the course of batch fermentations of glucose and xylose mixtures. Fermentations were conducted over a range of pH (5-6) in the presence of varying initial amounts of acetic acid (0-8 g/L) using a 10% (w/v) total sugar concentration (glucose only, xylose only, or 5% glucose/5% xylose mixture). Over the design space investigated, ethanol process yields varied between 56.6% and 92.3% +/- 1.3% of theoretical, depending upon the test conditions. The large variation in process yields reflects the strong effect pH plays in modulating the inhibitory effect of acetic acid on fermentation performance. A corresponding effect was observed on maximum cellular specific growth rates, with the rates varying between a low of 0.15 h(-1) observed at pH 5 in the presence of 8 g/L acetic acid to a high of 0.32 +/- 0.02 h(-1) obtained at pH 5 or 6 when no acetic acid was initially present. While substantial differences were observed in intracellular specific ATP concentration profiles depending upon fermentation conditions, maximum intracellular ATP accumulation levels varied within a relatively narrow range (1.5-3.8 mg ATP/g dry cell mass). Xylose fermentations produced and accumulated ATP at much slower rates than mixed sugar fermentations (5% glucose, 5% xylose), and the ATP production and accumulation rates in the mixed sugar fermentations were slightly slower than in glucose fermentations. Results demonstrate that higher levels of acetic acid delay the onset and influence the extent of intracellular ATP accumulation. ATP production and accumulation rates were most sensitive to acetic acid at lower values of pH.     

Effect of pH and nonionic surfactant on profile of intracellular and extracellular Monascus pigments

The uptake of nutrients and export of intracellular products are essential issues of microbial fermentation. Two-stage of Monascus fermentation using monosodium glutamate (MSG) as the sole nitrogen source, i.e., the first stage microbial fermentation in an aqueous solution and the second stage perstractive fermentation in a nonionic surfactant micelle aqueous solution, was carried out under different initial pH conditions. The results revealed that extracellular pH influences on the uptake of MSG and the export of water-soluble red pigment derivates into its extracellular broth. On the other hand, the export of intracellular hydrophobic pigments is affected by perstractive fermentation in nonionic surfactant micelle aqueous solution. All of those factors exhibit strong effect on the profile of Monascus pigments. This information is key to controlling profile of extracellular Monascus pigments by perstractive fermentation in nonionic surfactant micelle aqueous solution.     

Comparison of glucose fermentation by suspended and gel-entrapped yeast cells: An in vivo nuclear magnetic resonance study

Phosphorus-31 nuclear magnetic resonance ((31)P NMR) was used to compare the anaerobic metabolism of glucose by suspended and gel-entrapped Saccharomyces bayanus cells. The fermentation of glucose was carried out in a reaction system with continuous circulation through the NMR sample tube. The intracellular pH and the levels of some phosphorylated compounds were the levels of some phosphorylated compounds were noninvasively monitored by (31)P NMR while glucose, fermentation products, and biomass were determined by analytic techniques comparisons showed that no significant differences are observed in the relative concentrations in the spectra, but distinct profiles for the variation of both intracellular and extracellular pH are found. The internal pH of immobilized cells is maintained at a constant value throughout the fermentation as opposed to freely suspended cells for which a steady decrease in the internal pH occurs. A faster and stronger acidification is also observed in the external medium of the assays with suspended cells. Furthermore, higher yields for ethanol and biomass production and lower yields of fermentation by-products are obtained with immobilized cells. It is concluded that the higher intracellular pH achieved in the presence of the gel matrix had a regulatory effect on the metabolism which favored the ethanol production pathway. (c) 1993 John Wiley & Sons, Inc.     

pH对灵芝液态发酵代谢物及抗氧化活性的影响

已有研究报道灵芝栽培生长的最适pH在中性偏酸环境,在碱性范围的生长及代谢情况鲜见报道。本研究主要探究广泛pH对灵芝液态发酵代谢物及其抗氧化活性的影响。采用摇瓶液态培养后分析代谢物中灵芝三萜、胞内外多糖、菌丝体蛋白及抗氧化活性等指标,系统比较灵芝菌丝体在pH值2-11的生长和代谢情况。研究结果表明,灵芝菌丝体生长、合成灵芝三萜、胞内多糖、30E胞外多糖、菌丝体蛋白和菌丝体水解氨基酸的最适pH值分别为10、3、2、7、2和2。对应结果分别为17.13 g/L、33.86 mg/g、72.73 mg/g、7.86 g/L、71.42 mg/g和107.10 mg/g。比对照分别提高28.5%、77.3%、22.4%、96.5%、97.1%和70.8%。胞内多糖组分1和组分2最高分子量均在初始pH 4,分别为1.016×10⁸ g/mol和9.280×10⁴ g/mol,胞外多糖组分1最高分子量在初始pH 10,为4.946×10⁶ g/mol;对菌丝体的总抗氧化能力、1,1-二苯基-2-三硝基苯肼(1,1-diphenyl-2- picrylhydrazyl,DPPH)自由基清除能力、羟自由基清除能力分析结果表明最佳的初始pH分别为3、7、9。本研究为液态发酵方式下灵芝生长及其代谢物定向调控发酵的工艺优化提供参考依据,同时发现灵芝菌丝体中优质蛋白及抗氧化活性可在功能性食品和化妆品领域推广应用。     

Effect of benzoic acid on glycolytic metabolite levels and intracellular pH in Saccharomyces cerevisiae.

Low concentrations of benzoic acid stimulated fermentation rates in Saccharomyces cerevisiae. At concentrations near the maximum permitting growth, there was inhibition of fermentation, lowered ATP and intracellular pH, and relatively greater accumulation of benzoate. Changes in the levels of glycolytic intermediates suggested that fermentation was inhibited as a result of high ATP usage rather than of lowered intracellular pH. Specific inhibition of phosphofructokinase or of several other glycolytic enzymes was not observed.     

Effect of benzoic acid on glycolytic metabolite levels and intracellular pH in Saccharomyces cerevisiae.

Low concentrations of benzoic acid stimulated fermentation rates in Saccharomyces cerevisiae. At concentrations near the maximum permitting growth, there was inhibition of fermentation, lowered ATP and intracellular pH, and relatively greater accumulation of benzoate. Changes in the levels of glycolytic intermediates suggested that fermentation was inhibited as a result of high ATP usage rather than of lowered intracellular pH. Specific inhibition of phosphofructokinase or of several other glycolytic enzymes was not observed.     

Enzymatic Studies on the Conversion of Citric Acid Fermentation to Polyol Fermentation in Hydrocarbon-assimilating Yeast Candida zeylanoides

Production of polyols such as erythritol, d-mannitol and d-arabitol by citric acid-producing yeasts occurred only when the medium-pH was controlled at acidic pH, as described in the previous papers.

In order to elucidate the conversion mechanism of citric acid fermentation to polyol fermentation, the effect of pH on the activities of enzymes involved in polyol synthesis and tricarboxylic acid cycle was studied. Shifting down of the medium-pH from 5.5 to 3.5 led immediately to the change of intracellular pH, from 6.5~6.7 to 5.5~5.7. Such the change affected remarkably on the activities of intracellular enzymes. Citrate synthase was significantly depressed at pH 5.7, but isocitrate lyase and phosphoenolpyruvate carboxykinase were reversely stimulated at this pH.

In some yeast strains incapable of polyol production, the change of medium-pH reflected directly on intracellular pH, whereby almost all enzymes were inhibited.

From these results, the conversion of citric acid production to polyol production was explained by the change in the enzyme activities caused by lowering of intracellular pH.     

Bioconversion of inulin to 2,3-butanediol by a newly isolated Klebsiella pneumoniae producing inulinase

Inulin could be converted to bio-based chemicals by an inulinase producer without external inulinase, and the production of 2,3-butanediol was less than 50 g/L. In this work, a novel inulinase producer of Klebsiella pneumoniae H3 was isolated, and inulinase catalytic properties as well as 2,3-butanediol fermentation were investigated. The enzyme was an intracellular inulinase with an optimal pH of 6 ∼ 7 and a temperature of 30 °C. The use of inulin by H3 was dependent on the degree of polymerization (DP), and the average DP of inulin in fermentation broth increased from 2.82 to 8.08 in 24-h culture of batch fermentation. Acidic pretreatment was developed to increase inulin utilization by adjusting medium pH to 3.0 prior to sterilization. In batch fermentation with optimized medium and fermentation conditions, the concentration of target product (2,3-butanediol and acetoin) was 80.4 g/L with a productivity of 2.23 g/(L⋅h), and a yield of 0.426 g/g inulin.     

Optimization of ectoine synthesis through fed-batch fermentation of Brevibacterium epidermis

A production process for ectoine has been developed, using Brevibacterium epidermis DSM20659 as the producer strain. First, the optimal conditions for intracellular synthesis of ectoine were determined. The size of the intracellular ectoine pool is shown to be dependent on the external salt concentration, type of carbon source, and yeast extract concentration. Under the optimized conditions of 1 M NaCl, 50 g/L monosodium glutamate, and 2.5 g/L yeast extract, a maximum concentration of intracellular ectoine of 0.9 g/L was obtained in shake flask cultures. After optimizing the batch fermentation parameters of temperature, pH, agitation, and aeration, the yield could be further increased by applying the fed-batch fermentation principle in 1.5- to 2-L fermentors. Glutamate and yeast extract were fed to the bacterial cells such that the total glutamate concentration in the broth remained constant. A total yield of 8 g ectoine/L fermentation broth was obtained with a productivity of 2 g ectoine/L/day. After the bacterial cells were harvested from the culture broth, the ectoine was recovered from them by a two-step extraction with water and ethanol. Crystallization of the product was obtained after concentration of the extract via evaporation under reduced pressure. After this downstream process, 55% of the ectoine produced in the fermentor could be crystallized in four fractions. The first fractions were of very high purity (98%). This production process can compete with other described production processes for ectoine in productivity and simplicity. Further advantages are the relatively low amounts of NaCl needed and the absence of hydroxyectoine, often a byproduct, in the final product.     

Optimization of fermentation process for the production of intracellular polysaccharide from Paecilomyces cicadae and the immuno-stimulating activity of intracellular polysaccharide

Optimization of fermentation process for the production of intracellular polysaccharide (IPS) from the fungus Paecilomyces cicadae and the immuno-stimulating activity of IPS were carried out. The quantitative effects of initial pH, fermentation temperature and time on the yield of IPS content produced by P. cicadae in submerged fermentation were investigated separately using response surface methodology (RSM). The three factors chosen for the present investigation were based on the results of a previous Plackett?CBurman (PB) design. The experimental data obtained were fitted to a second-order polynomial equation using multiple regression analysis and also analyzed by appropriate statistical methods. RSM analysis showed good correspondence between experimental and predicted values. It was found that three parameters represented significant effect. Probability value (p?<?0.0001) demonstrated a very high significance for the regression model. By solving the regression equation and analyzing the response surface contour plots, the optimal process parameters were determined, i.e. fermentation temperature 24.53?°C, initial pH 7.46 and fermentation time 73.9?h. The maximum predicted yield of IPS was 356.02???g/ml under the optimal conditions. Meanwhile, IPS from P. cicadae was found to have direct immuno-stimulating activity in vitro on murine macrophage RAW264.7 proliferative response and to stimulate nitric oxide generation in a dose-dependent manner.     

Optimizing medium constituents and fermentation conditions for citric acid production from palmyra jaggery using response surface method

The quantitative effects of pH, temperature, time of fermentation, sugar concentration, nitrogen concentration and potassium ferrocyanide on citric acid production were investigated using a statistical experimental design. It was found that palmyra jaggery (sugar syrup from the palmyra palm) is a suitable substrate for increasing the yield of citric acid using Aspergillus niger MTCC 281 by submerged fermentation. Regression equations were used to model the fermentation in order to determine optimum fermentation conditions. Higher yields were obtained after optimizing media components and conditions of fermentation. Maximum citric acid production was obtained at pH 5.35, 29.76 °C, 5.7 days of fermentation with 221.66 g of substrate/l, 0.479 g of ammonium nitrate/l and 2.33 g of potassium ferrocyanide/l.     

Influence of pH and undissociated butyric acid on the production of acetone and butanol in batch cultures of Clostridium acetobutylicum

Summary The kinetics of growth and acid and solvent production are examined in batch fermentation of Clostridium acetobutylicum at pH between 4.5 and 6.0. At the lower pH, growth occurs in two consecutive phases and solvents are the main excreted metabolites. At the higher pH, there is a single growth phase with only acid formation. The influence of the pH can be correlated with a critical role of the concentration of undissociated butyric acid in the medium: cellular growth is inhibited above 0.5 g/l and solvent production starts at an undissociated acid level of 1.5 g/l. Reducing the intracellular acid dissociation by lowering the intracellular pH also favours the production of acetone and butanol.     

Effect of pH on the metabolic flux of Klebsiella oxytoca producing 2,3-butanediol in continuous cultures at different dilution rates

The efficiency of the bioconversion process and the achievable end-product concentration decides the economic feasibility of microbial 2,3-butanediol (2,3-BDO) production. In 2,3-BDO production, optimization of culture condition is required for cell growth and metabolism. Also, the pH is an important factor that influences microbial performance. For different microorganisms and substrates, it has been shown that the distribution of the metabolites in 2,3-BDO fermentation is greatly affected by pH, and the optimum pH for 2,3-BDO production seems dependently linked to the particular strain and the substrate employed. Quantification analysis of intracellular metabolites and metabolic flux analysis (MFA) were used to investigate the effect of pH on the Klebsiella oxytoca producing 2,3-BDO and other organic acids. The main objectives of MFA are the estimation of intracellular metabolic fluxes and the identification of rate-limiting step and the key enzymes. This study was conducted under continuous aerobic conditions at different dilution rates (0.1, 0.2, and 0.3 h^?1) and different pH values (pH 5.5 and 7.0) for the steady-state experimental data. In order to obtain the flux distribution, the extracellular specific rates were calculated from the experimental data using the metabolic network model of K. oxytoca. Intracellular metabolite concentration profiles were generated using ultra-performance liquid chromatography/quadrupole time-of-flight mass spectrometry.     

Efficient production of ε-poly-l-lysine from glucose by two-stage fermentation using pH shock strategy

In this study, a pH shock strategy was employed to enhance ε-poly-l-lysine (ε-PL) production from glucose. In the conventional fermentation, in the early stage, only 13% of total ε-PL production is achieved in 25% of the entire fermentation period, which severely affected ε-PL productivity. To improve the efficiency of ε-PL production during fermentation, a novel two-stage fermentation, namely culture and fermentation stages, was proposed on the basis of the analysis of conventional pH shock fermentation. After optimization of parameters such as inoculum growth conditions, initial fermentation pH, and inoculum volume, the ε-PL production and productivity achieved using the novel fermentation process in a 5-L fermenter reached 32.22 g/L and 5.86 g/L/day, which were 32.3% and 36.6% higher, respectively, when compared with those obtained in conventional fermentation. Furthermore, evaluation of acid tolerance of mycelia collected from the pH shock fermentation showed that pH shock enhanced ε-PL production, which might be related to the acid tolerance of Streptomyces albulus and pH stress (pH 3.0). The results obtained could be useful for large-scale ε-PL production and to provide new information on ε-PL biosynthesis mechanism.     

废弃活性污泥中产聚羟基脂肪酸酯菌株Bacillus sp. PB-3的发酵条件优化

通过尼罗红染色法结合荧光显微镜镜检,从废弃活性污泥中分离得到1株高产聚羟基脂肪酸酯(PHAs)的菌株Bacillus sp.PB-3,经气相色谱法鉴定该菌株胞内产物为聚β-羟基丁酸酯(PHB)。对培养基成分及发酵条件优化后,获得最佳培养方案:12 g/L的葡萄糖为C源,2 g/L的牛肉膏为N源,初始pH 7.5,培养基装液量80 mL,转速为200 r/min,37℃培养48 h,PHB质量分数可达菌体干质量的32.09%,比优化前提高30%。     

Enhanced butyric acid tolerance and bioproduction by Clostridium tyrobutyricum immobilized in a fibrous bed bioreactor

Repeated fed‐batch fermentation of glucose by Clostridium tyrobutyricum immobilized in a fibrous bed bioreactor (FBB) was successfully employed to produce butyric acid at a high final concentration as well as to adapt a butyric‐acid‐tolerant strain. At the end of the eighth fed‐batch fermentation, the butyric acid concentration reached 86.9 ± 2.17 g/L, which to our knowledge is the highest butyric acid concentration ever produced in the traditional fermentation process. To understand the mechanism and factors contributing to the improved butyric acid production and enhanced acid tolerance, adapted strains were harvested from the FBB and characterized for their physiological properties, including specific growth rate, acid‐forming enzymes, intracellular pH, membrane‐bound ATPase and cell morphology. Compared with the original culture used to seed the bioreactor, the adapted culture showed significantly reduced inhibition effects of butyric acid on specific growth rate, cellular activities of butyric‐acid‐forming enzyme phosphotransbutyrylase (PTB) and ATPase, together with elevated intracellular pH, and elongated rod morphology. Biotechnol. Bioeng. 2011; 108:31–40. © 2010 Wiley Periodicals, Inc.     

Optimization of medium constituents and fermentation conditions for the production of ethanol from palmyra jaggery using response surface methodology

The quantitative effects of sugar concentration, nitrogen concentration, EDTA, temperature, pH and time of fermentation on ethanol production were optimized using a Box-Wilson central composite design (CCD) experiment. It was found that palmyra jaggery (sugar syrup from the palmyra palm) is a suitable substrate for the production of high concentrations of ethanol using Saccharomyces cerevisiae NCIM 3090 by submerged fermentation. A maximum ethanol concentration of 129.4 g/l was obtained after optimizing media components and conditions of fermentation. The optimum values were a temperature of 26.2 °C, pH of 8.4, time of fermentation of 4.2 days with 398.5 g of substrate/l, 3.1 g of urea/l and 0.51 g of EDTA/l. Thus by using the CCD, it is possible to determine the accurate values of the fermentation parameters where maximum production of ethanol occurs.     

Optimization of fermentation conditions for the production of ethanol from sago starch using response surface methodology

The quantitative effects of temperature, pH and time of fermentation were investigated on simultaneous saccharification and fermentation (SSF) of ethanol from sago starch with glucoamylase (AMG) and Zymomonas mobilis ZM4 using a Box–Wilson central composite design protocol. The SSF process was studied using free enzyme and free cells and it was found that with sago starch, maximum ethanol concentration of 70.68 g/l was obtained using a starch concentration of 140 g/l, which represents an ethanol yield of 97.08%. The optimum conditions for the above yield were found to be a temperature of 36.74 °C, pH of 5.02 and time of fermentation of 17 h. Thus by using the central composite design, it is possible to determine the accurate values of the fermentation parameters where maximum production of ethanol occurs.