A phenomenological model to represent the kinetics of growth by <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> for lysine production

Corynebacterium glutamicum is commonly used for lysine production. In the last decade, several metabolic engineering approaches have been successfully applied to C. glutamicum. However, only few studies have been focused on the kinetics of growth and lysine production. Here, we present a phenomenological model that captures the growth and lysine production during different phases of fermentation at various initial dextrose concentrations. The model invokes control coefficients to capture the dynamics of lysine and trehalose synthesis. The analysis indicated that maximum lysine productivity can be obtained using 72 g/L of initial dextrose concentration in the media, while growth was optimum at 27 g/L of dextrose concentration. The predictive capability was demonstrated through a two-stage fermentation strategy to enhance the productivity of lysine by 1.5 times of the maximum obtained in the batch fermentation. Two-stage fermentation indicated that the kinetic model could be further extended to predict the optimal feeding strategy for fed-batch fermentation.     

Absorption des acides amines par les lutoïdes du latex d'Hevea brasiliensis

Absorption of Amino Acids by Lutoids from the Latex of Hevea brasiliensis. The latex of Hevea brasiliensis is a fluid protoplasm containing organelles with a single membrane that are called lutoids. They are microvacuoles of a lysosomal character. The intact lutoids can easily be isolated in an isotonic medium by the usual procedures of cellular fractionation. Previous studies have shown the existence of a compartmentation of the free amino acids in latex. While acidic components dominate in the cytoplasmic serum, the lutoid serum contains mainly basic components. These findings, as well as the part played by the lutoids in the latex flow and in the process of latex coagulation, led the authors to study the penetration of acidic, neutral and basic amino acids into the lutoids. Labelled amino acids were used for the purpose. Special interest was given to the uptake of lysine, which is transported into the lutoids against a concentration gradient in the absence of a metabolic energy source. The process is linear for at least 30 min and follows Michaelis–Menten kinetics as a function of the lysine concentration. The uptake is strictly temperature and pH dependent. It increases in the presence of ATP. Lysine uptake by lutoids is also increased by application of Ethrel, ethylene generator, to the bark of tapped trees. 2,4-Dinitrophenol (2,4-DNP), ammonium chloride and N-ethylmaleimide (NEM) inhibit the influx. Neutral l -amino acids do not affect the uptake of l -lysine, while l arginine inhibits lysine transport competitively. d -lysine is without effect on l -lysine uptake by lutoids. Under conditions used in this study no lysine efflux is observed. A mechanism governing the penetration of basic amino acids against a concentration gradient is discussed, and the possible role of a proton gradient is suggested.     

Utilization of high lysine-producing strains of Lactobacillus plantarum as starter culture for nutritional improvement of ogi

A high lysine-producing mutant of Lactobacillus plantarum (OG 261-5) derived from a wild type strain (OG 261) previously isolated from fermenting ogi was evaluated for nutritional improvement of ogi in a modified fermentation process. Results indicate that ogi obtained by fermentation with the pure culture of the mutant compared to traditional ogi increased in concentration of available lysine from 228.5 ± 12.0 mg/100 g to 525.1 ± 25.8 mg/100 g, tryptophan from 58.6 ± 8.0 mg/100 g to 114.3 ± 11.0 mg/100 g and tyrosine from 408.5 ± 13.7 mg/100 g to 4636.5 ± 11.3 mg/100 g. However, the contents of valine, leucine, isoleucine and phenylalanine were substantially reduced which may affect the protein quality of the modified ogi. The modified process shortened the period of traditional ogi production from five days to one by reducing the two-stage fermentation (i.e. soaking and souring stages) to a one-stage process and the total protein recovery was better compared to traditional ogi processing. There was no significant difference (P > 0.05) in organoleptic quality attributes of colour, flavour, and overall acceptability of ogi produced by the modified process and the traditional ogi.     

Influence of short chain fatty acids and lysine on Salmonella typhimurium cadA expression

In Salmonella typhimurium, cadA has a role in virulence expression and is an inducible gene that responds to external lysine concentration. In this study, a strain of S. typhimurium carrying a cadA: lacZ fusion was used to determine if the induction of cadA occurred under different lysine concentrations and mildly acid conditions in the presence of short chain fatty acids. Aliquots of an 18-h culture of S. typhimurium were placed on fresh media containing different lysine concentrations at pH 5.8 adjusted by addition of HCl or by 1 M short chain fatty acids (SCFA, acetic, propionic and butyric acid) stock solution. After an induction period of 2 h, -galactosidase activities were assayed. Expression of cadA in rich medium was significantly higher than that of minimal medium at neutral pH and different lysine concentrations. In contrast, at pH 5.8, there was a significant increase in cadA expression, particularly when pH was adjusted using HCl at all lysine levels. Addition of a mixture of organic acids yielded an overall lower cadA expression at all lysine levels studied when compared to HCl. However, each SCFA challenge (individual or as a mixture) caused a high level of expression, both at neutral and acidic pH. Based on these results it is apparent that in the presence of external lysine, SCFA and nutrient availability can influence cadA expression in S. typhimurium.     

Isolation of regulatory mutants of Pseudomonas acidovorans by use of amino acid analogs

Mutants resistant to various combinations of threonine, lysine and/or their analogs were obtained and characterized in Pseudomonas acidovorans. In particular, mutants resistant to aminoethylcysteine had a dihydrodipicolinate synthetase insensitive to lysine inhibition whereas mutants resistant to threonine plus a low concentration of aminoethylcysteine had a feedback-insensitive aspartokinase.     

Changes in the intracellular concentrations of the adenosine phosphates and nicotinamide adenine dinucleotides ofSaccharomyces cerevisiae during batch fermentation

Significant changes in the intracellular concentrations of adenosine phosphates and nicotinamide adenine dinucleotides were observed during fermentation of grape must by three different strains ofSaccharomyces cerevisiae: S. cerevisiae var.cerevisiae, a typical fermentative yeast strain and two flor-veil-forming strains,S. cerevisiae var.bayanus andS. cerevisiae var.capensis. The intracellular concentration of ATP was always higher inS. cerevisiae var.cerevisiae than in the flor-veil-forming strains. NAD⁺ and NADP⁺ concentrations decreased at faster rates in the flor-veil-forming yeasts than in the other yeast but NADH concentration was the same in all yeasts for the first 10 days of fermentation. NADPH concentration was always lower inS. cerevisiae var.cerevisiae than in the other yeasts and this yeast also showed higher rates of growth and fermentation during the early stages of the fermentation and the presence of non-viable cells at the end of fermentation. In contrast, the flor-veil-forming strains maintained growth and fermentation capabilities for a relatively long time and viable cells were present throughout the entire fermentation process (31 days).The authors are with the Department of Microbiology, Faculty of Sciences, University of Cordoba, Avda. San Alberto Magno s/n, 14004-Córdoba, Spain     

Expression of the <Emphasis Type="BoldItalic">Escherichia coli pntAB</Emphasis> genes encoding a membrane-bound transhydrogenase in <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> improves <Emphasis Type="SmallCaps">l</Emphasis>-lysine formation

A critical factor in the biotechnological production of l-lysine with Corynebacterium glutamicum is the sufficient supply of NADPH. The membrane-integral nicotinamide nucleotide transhydrogenase PntAB of Escherichia coli can use the electrochemical proton gradient across the cytoplasmic membrane to drive the reduction of NADP⁺ via the oxidation of NADH. As C. glutamicum does not possess such an enzyme, we expressed the E. coli pntAB genes in the genetically defined C. glutamicum lysine-producing strain DM1730, resulting in membrane-associated transhydrogenase activity of 0.7 U/mg protein. When cultivated in minimal medium with 10% (w/v) carbon source, the presence of transhydrogenase slightly reduced glucose consumption, whereas the consumption of fructose, glucose plus fructose, and, in particular, sucrose was stimulated. Biomass was increased by pntAB expression between 10 and 30% on all carbon sources tested. Most importantly, the lysine concentration was increased in the presence of transhydrogenase by ∼10% on glucose, ∼70% on fructose, ∼50% on glucose plus fructose, and even by ∼300% on sucrose. Thus, the presence of a proton-coupled transhydrogenase was shown to be an efficient way to improve lysine production by C. glutamicum. In contrast, pntAB expression had a negative effect on growth and glutamate production of C. glutamicum wild type.     

Optimization of a fermentation process for bioinsecticide production by <Emphasis Type="Italic">Bacillus thuringiensis</Emphasis>

In an attempt to develop a cost-effective process for bioinsecticide production by B. thuringiensis, the feeding regime during aerobic cultivation of the bacterium was investigated and optimized. The process was designed as a two-stage process; a first stage of active growth, where glucose and other nutrients were adequately supplied to the growing cells over 12 h, followed by a second stage of 2 h for spore formation and toxin release. In order to maximize spore and toxin yield and productivity, different quantities of glucose and nutrients were fed separately to the growing cells in four different fermentation runs. In all runs, glucose was converted to bacterial biomass during the first stage and subsequently to spores and crystal protein during the second phase. The best results were obtained with a fermentation run supplied with 190 g glucose in 1500 ml. Up to 20.1 g of bacterial insecticides/l were recovered from fermentation broth with a glucose to toxin conversion yield of 0.159 g/g. Also, a markedly high spore concentration of 2.31 × 10¹² c.f.u./ml was obtained. The spore–crystal protein mixture obtained was tested for its insecticidal activity against three of the most agronomically important pests. Among the bioinsecticide-treated insect pests, Egyptian cotton leafworm, Spodoptera littoralis was the most susceptible pest with the lowest LC₅₀ of the bioinsecticides against its larval instar and the highest virulence against adults emerged later on from the surviving larvae.     

A sodium ion gradient as energy source for Peptostreptococcus asaccharolyticus

The determination of enzymatic activities in cell-free extracts of Acidaminococcus fermentans and Peptostreptococcus asaccharolyticus led to a refined scheme for the pathway of glutamate fermentation via (R)-2-hydroxyglutarate to acetate and butyrate. From the ratio of these products the amount of ATP generated by substrate level phosphorylation was calculated. Growth experiments with the organisms including Clostridium symbiosum and Clostridium tetanomorphum indicated that a sodium gradient contributed additional energy for growth. The high growth yields found in organisms containing the biotin dependent sodium pump glutaconyl-CoA decarboxylase could be reduced by the sodium ionophor monensin. In P. asaccharolyticus energy equivalent up to 0.6 mol ATP per mol of glutaconyl-CoA decarboxylated was conserved via the Na⁺ gradient. The data may explain the growth promoting effects of monensin in cattle.     

响应面法优化赖氨酸发酵培养基

运用Ｂｏｘ－Ｂｅｈｋｅｎ设计的响应面试验（Ｒｅｓｐｏｎｓｅ－ｓｕｒｆａｃｅ ｅｘｐｅｒｉｍｅｎｔ）对黄色短杆菌（Ｂｒｅｕｉｂａｃｔｅｒｉｕｍ ｆｌａｕｕｍ）ＦＢ４２进行赖氨酸发酵的培养基进行了优化。响应面法对７２小时分批发酵结果的优化分析表明：硫酸铵、豆饼水解液及玉米浆三种因素对赖氨醚发酵无明显的交互作用,在硫酸铵、豆饼水解液和玉米浆的浓度分别为５％、２％和３％时,发酵液中的产酸达到５４．０６ｇ／     

Amino-acid transport into cultured tobacco cells

Arginine transport in suspension-cultured cells of Nicotiana tabacum L. cv. Wisconsin-38 was investigated. Cells that were preincubated in the presence of Ca²⁺ for 6 h prior to transport exhibited stimulated transport rates. After the preincubation treatment, initial rates of uptake were constant for at least 45 min. Arginine accumulated in the cells against a concentration gradient; this accumulation was not the result of exchange diffusion. Arginine uptake over a concentration range of 2.5 M to 1 mM was characterized by simple Michaelis-Menten kinetics with a K_m of 0.1 mM and a V_max of 9,000 nmol g^-1 fresh weight h^-1. Transport was inhibited by several compounds including carbonylcyanide-m-chlorophenylhydrazone, 2,4-dinitrophenol, N,N-dicyclohexylcarbodiimide, and N-ethylmaleimide. Inhibition by these compounds was not the result of increased efflux resulting from membrane damage. A variety of amino acids and analogs, with the exception of D-arginine, inhibited transport, indicating that arginine transport was mediated by a general L-aminoacid permease. Competition experiments indicated that arginine and lysine exhibited cross-competition for transport, with K_i values similar to respective K_m values. Arginine transport and low-affinity lysine transport are probably mediated by the same system in these cells.Abbreviations BTP Bis Tris Propane - CCCP Carbonylcyanide-m-chlorophenylhydrazone - DCCD N,N-dicyclohexylcarbodiimide - DNP 2,4-dinitrophenol - DTT Dithiothreitol - NEM N-ethylmaleimide - MES 2(N-morpholino)ethanesulfonic acid - TCA trichloroacetic acid This paper is the third in a series on amino-acid transport into cultured tobacco cells. For parts I and II, see Harrington and Henke (1981) and Harrington et al. (1981)     

Production of hydrogen from marine macro-algae biomass using anaerobic sewage sludge microflora

Hydrogen was produced from various marine macro-algae (seaweeds) through anaerobic fermentation using an undefined bacterial consortium. In this study, anaerobic fermentation from various marine macro-algae for Ulva lactuca, Porphyra tenera, Undaria pinnatifida, and Laminaria japonica was studied. From this analysis Laminaria japorica was determined to be the optimum substrate for hydrogen production. When L. japornica was used as the carbon source for enhanced hydrogen production, the optimum fermentation temperature, substrate concentration, initial pH, and pretreatment condition were determined to be 35°C, 5%, 7.5, and BT120 (Ball mill and thermal treatments at 120°C for 30 min), respectively. In addition, hydrogen production was improved when the sludge was heat-treated at 65°C for 20 min. Under these conditions, about 4,164 mL of hydrogen was produced from 50 g/L of dry algae (L. japonica) for 50 h, with a hydrogen concentration around 34.4%. And the maximum hydrogen production rate and yield were found to be 70 mL/L·h and 28 mL/g dry algae, respectively.     

Energetics of arginine and lysine transport by whole cells and membrane vesicles of strain SR, a monensin-sensitive ruminal bacterium.

Strain SR, a monensin-sensitive, ammonia-producing ruminal bacterium, grew rapidly on arginine and lysine, but only if sodium was present. Arginine transport could be driven by either an electrical potential or a chemical gradient of sodium. Arginine was converted to ornithine, and it appeared that ornithine efflux created a sodium gradient which in turn drove arginine transport. There was a linear decline in arginine transport as pH was decreased from 7.5 to 5.5, and the cells did not grow at a pH less than 6.0. The Eadie-Hofstee plot was biphasic, and arginine could also be taken by a high-capacity diffusion mechanism. Because arginine was a strong inhibitor of lysine transport and lysine was a weak inhibitor of arginine transport, it appeared that both lysine and arginine were taken up by an arginine-lysine carrier which had a preference for arginine. The rate of lysine fermentation was always proportional to the extracellular lysine concentration, and facilitated diffusion was the dominant mechanism of lysine transport. When SR was grown in continuous culture on arginine or lysine, the theoretical maximal growth yield was similar (13 g of cells per mol of ATP), but the apparent maintenance energy requirement for arginine was greater than lysine (9.4 versus 4.4 mmol of ATP per g of cells per h). On the basis of differences in yield and maintenance energy, it appeared that active arginine transport accounted for approximately 40% of the total ATP.     

Energetics of arginine and lysine transport by whole cells and membrane vesicles of strain SR, a monensin-sensitive ruminal bacterium.

Strain SR, a monensin-sensitive, ammonia-producing ruminal bacterium, grew rapidly on arginine and lysine, but only if sodium was present. Arginine transport could be driven by either an electrical potential or a chemical gradient of sodium. Arginine was converted to ornithine, and it appeared that ornithine efflux created a sodium gradient which in turn drove arginine transport. There was a linear decline in arginine transport as pH was decreased from 7.5 to 5.5, and the cells did not grow at a pH less than 6.0. The Eadie-Hofstee plot was biphasic, and arginine could also be taken by a high-capacity diffusion mechanism. Because arginine was a strong inhibitor of lysine transport and lysine was a weak inhibitor of arginine transport, it appeared that both lysine and arginine were taken up by an arginine-lysine carrier which had a preference for arginine. The rate of lysine fermentation was always proportional to the extracellular lysine concentration, and facilitated diffusion was the dominant mechanism of lysine transport. When SR was grown in continuous culture on arginine or lysine, the theoretical maximal growth yield was similar (13 g of cells per mol of ATP), but the apparent maintenance energy requirement for arginine was greater than lysine (9.4 versus 4.4 mmol of ATP per g of cells per h). On the basis of differences in yield and maintenance energy, it appeared that active arginine transport accounted for approximately 40% of the total ATP.     

Peptide transport by germinating barley embryos

Glycylsarcosine, a dipeptide which is resistant to peptidase activity, was accumulated intact against a concentration gradient by germinating embryos of Hordeum vulgare L., var. Maris Otter, Winter. This is the first clear evidence for the presence of a dipeptide transport system involved in the movement of protein reserves across the scutellum from the endosperm to the embryo during germination.Abbreviations gly-sar glycylsarcosine - TCA trichloroacetic acid     

Controlled formation of volatile components in cider making using a combination of Saccharomyces cerevisiae and Hanseniaspora valbyensis yeast species

The effect of pure and mixed fermentation by Saccharomyces cerevisiae and Hanseniaspora valbyensis on the formation of major volatile components in cider was investigated. When the interaction between yeast strains of S. cerevisiae and H. valbyensis was studied, it was found that the two strains each affected the cell growth of the other upon inoculation of S. cerevisiae during growth of H. valbyensis. The effects of pure and mixed cultures of S. cerevisiae and H. valbyensis on alcohol fermentation and major volatile compound formation in cider were assessed. S. cerevisiae showed a conversion of sugar to alcohol of 11.5%, while H. valbyensis produced alcohol with a conversion not exceeding 6%. Higher concentrations of ethyl acetate and phenethyl acetate were obtained with H. valbyensis, and higher concentrations of isoamyl alcohol and isobutyl were formed by S. cerevisiae. Consequently, a combination of these two yeast species in sequential fermentation was used to increase the concentration of ethyl esters by 7.41–20.96%, and to decrease the alcohol concentration by 25.06–51.38%. Efficient control of the formation of volatile compounds was achieved by adjusting the inoculation time of the two yeasts.     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。     

Influence of Temperature and Oxygen Concentration on the Fermentation Behaviour of Candida Stellata in Mixed Fermentation with Saccharomyces Cerevisiae

Summary Candida stellata is a wine-yeast species that has been proposed for use as a starter in the wine industry in combination with selected Saccharomyces cerevisiae cultures. To improve our knowledge on the metabolic interactions between these two yeast species, we have investigated the influence of temperature and oxygen concentration on their fermentation behaviour in mixed fermentation. Trials were carried out with free and immobilized C. stellata cells followed by an inoculum of a commercial strain of S. cerevisiae, to determine the biomass evolution and the oenological profiles of the resulting wines. We show that the oxygen concentration does not influence the fermentation behaviour of the C. stellata cells, while a low temperature (16 °C) is a critical condition for the metabolic activity of C. stellata in free-cell trials. The immobilization procedures produce a significant improvement in the metabolic activity of C. stellata, with a consequent enhancement of the glycerol content also at the 16 °C fermentation temperature. High cell concentrations and the immobilization system appear to positively influence the fermentation behaviour of C. stellata. These results are of interest for the practical application of this process in winemaking.     

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.