Glucose uptake of Cytophaga johnsonae studied in batch and chemostat culture

The influence of different physiological states on the glucose uptake and mineralization by Cytophaga johnsonae, a freshwater isolate, was examined in batch and chemostat cultures. At different growth rates under glucose limitation in chemostat cultures, different uptake patterns for ¹⁴C labeled glucose were observed. In batch culture and at high growth rates the glucose uptake potential showed a higher maximum velocity and a much lower substrate affinity than at lower growth rates. These findings and the results of short-term labeling patterns could be explained by two different glucose uptake mechanisms which enable the strain to grow efficiently both at high and low substrate concentrations. Substrate specificity studies showed that a structural change of the C-2 atom of the glucose molecule was tolerated by both systems. The consequences of these results for the ecophysiological classification of the Cytophaga group and for the operation of continuous cultures are discussed.     

Production of gluconic acid and 2-ketogluconic acid by Klebsiella aerogenes NCTC 418

2-Ketogluconic acid and, to a lesser extent, gluconic acid were found to be major products of glucose catabolism by phosphate-limited cultures of Klebsiella aerogenes NCTC 418, and together accounted for up to 46% of the glucose carbon that was metabolized.Although the concentrations of both acids increased sub-stantially at low growth rates, their specific rates of synthesis decreased markedly, as did the proportion of glucose converted into these products.Determination of the affinity constant, for glucose, of phosphate-limited organisms showed it to be not significantly different from that of glucose-limited organisms (K _s 50 M), indicative of the phosphotransferase uptake system. And since these organisms possessed an active glucose 6-phosphate dehydrogenase, and had no detectable glucose dehydrogenase activity, it was concluded that gluconic acid and 2-ketogluconic acid arose from their corresponding phosphorylated metabolites, and not directly from glucose.     

Mixed substrate growth of methylotrophic yeasts in chemostat culture: Influence of the dilution rate on the utilisation of a mixture of glucose and methanol

The growth of Hansenula polymorpha and Kloeckera sp. 2201 with a mixture of glucose and methanol (38.8%/61.2%, w/w) and the regulation of the methanol dissimilating enzymes alcohol oxidase, catalase, formaldehyde dehydrogenase and formate dehydrogenase were studied in chemostat culture, as a function of the dilution rate. Both organisms utilized and assimilated glucose and methanol simultaneously up to dilution rates of 0.30 h^-1 (H. polymorpha) and 0.26h^-1, respectively (Kloeckera sp. 2201) which significantly exceeded _max found for the two yeasts with methanol as the only source of carbon. At higher dilution rates methanol utilisation ceased and only glucose was assimilated. Over the whole range of mixed-substrate growth both carbon sources were assimilated with the same efficiency as during growth with glucose or methanol alone.In cultures of H. polymorpha, however, the growth yield for glucose was lowered by the unmetabolized methanol at high dilution rates. During growth on both carbon sources the repression of the synthesis of all catabolic methanol enzymes which is normally caused by glucose was overcome by the inductive effect of the simultaneously fed methanol. In both organisms the synthesis of alcohol oxidase was found to be regulated differently as compared to catalase, formaldehyde and formate dehydrogenase. Whereas increasing repression of the synthesis of alcohol oxidase was found with increasing dilution rates as indicated by gradually decreasing specific activities of this enzyme in cell-free extracts, the specific activities of this enzyme in cell-free extracts, the specific activities of catalase and the dehydrogenases increased with increasing growth rates until repression started. The results indicate similar patterns of the regulation of the synthesis of methanol dissimilating enzymes in different methylotrophic yeasts.Abbreviations and Terms C₁ Methanol - C₆ glucose; D dilution rate (h^-1) - D _c critical dilution rate (h^-1) - q _s specific, rate of substrate consumption (g substrate [g cell dry weight]^-1 h^-1) - q _CO2 and q _O2 are the specific rates of carbon dioxide release and oxygen consumption (mmol [g cell dry weight]^-1 h^-1) - RQ respiration quotient (q _CO2 q _O2 ¹ ) - s ₀(C₁) and s ₀(C₆) are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - s residual substrate concentration in the culture liquid (g l^-1) - Sp. A. enzyme specific activity - x cell dry weight concentration (gl^-1) - Y _X/C6 growth yield on glucose (g cell dry weight [g substrate]^-1     

Electron transport chain of Zymomonas mobilis

The interaction of the membrane-bound glucose dehydrogenase from the anaerobic but aerotolerant bacterium Zymomonas mobilis with components of the electron transport chain has been studied. Cytoplasmic membranes showed reduction of oxygen to water with the substrates glucose or NADH. The effects of the respiratory chain inhibitors piericidin, capsaicin, rotenone, antimycin, myxothiazol, HQNO, and stigmatellin on the oxygen comsumption rates in the presence of NADH or glucose as substrates indicated that a complete and in the most parts identical respiratory chain is participating in the glucose as well as in the NADH oxidation. Furthermore, the presence of coenzyme Q₁₀ (ubiquinone 10) in Z. mobilis was demonstrated. Extraction from and reincorporation of the quinone into the membranes revealed that ubiquinone is essential for the respiratory activity with glucose and NADH. In addition, a membrane-associated tetramethyl-p-phenylene-diamine-oxidase activity could be detected in Z. mobilis.Abbreviations ABTS 2,2-Azino-di-[3-ethyl-benzthiazolinesulfonate (6)] - GDH glucose dehydrogenase - HQNO 2-heptyl-4-hydroxy-quinoline-N-oxide - PQQ pyrroloquinoline quinone - TMPD N,N,N,N-tetramethyl-p-phenylene-diamine     

The effect of growth factors on anoxic chemostat cultures of two Saccharomyces cerevisiae strains

In anoxic chemostat cultures of Saccharomyces cerevisiae ATCC 4126 and CBS 8066 grown in a medium containing yeast extract, a sharp increase in the steady-state residual glucose concentration occurred at relatively low dilution rates, contrary to the expected Monod kinetics. However, supplementation with vitamins and amino acids facilitated efficient glucose uptake. This enhanced requirement for growth factors under anoxic conditions and at high growth rates could explain the exceptionally high apparent k _s values for S. cerevisiae reported in the literature.     

An analysis of the growth of Gluconobacter oxydans in chemostat cultures

Gluconobacter oxydans was grown successively in glucose and nitrogen-limited chemostat cultures. Construction of mass balances of organisms growing at increasing dilution rates in glucose-limited cultures, at pH 5.5, revealed a major shift from extensive glucose metabolism via the pentose phosphate pathway to the direct pathway of glucose oxidation yielding gluconic acid. Thus, whereas carbon dioxide production from glucose accounted for 49.4% of the carbon input at a dilution rate (D)=0.05 h^-1, it accounted for only 1.3% at D=0.26 h^-1. This decline in pentose phosphate pathway activity resulted in decreasing molar growth yields on glucose. At dilution rates of 0.05 h^-1 and 0.26 h^-1 molar growth yields of 19.5 g/mol and 3.2 g/mol, respectively, were obtained. Increase of the steady state glucose concentration in nitrogen-limited chemostat cultures maintained at a constant dilution rate also resulted in a decreased flow of carbon through the pentose phosphate pathway. Above a threshold value of 15–20 mM glucose in the culture, pentose phosphate pathway activity almost completely inhibited. In G. oxydans the coupling between energy generation and growth was very inefficient; yield values obtained at various dilution rates varied between 0.8–3.4 g/cells synthesized per 0.5 mol of oxygen consumed.     

Physiological and environmental effects on metabolic flux change caused by heterologous gene expression inEscherichia coli

Expression of theZymomonas mobilis pyruvate decarboxylase (pdc) and alcohol dehydrogenase (adh) genes inEscherichia coli has been known to reduce acetate accumulation by shifting carbon flow from acetate to ethanol. In this study, we investigated the effects of physiological and environmental conditions on the metabolic flux alteration caused by the expression of thepdc andadh genes. In the batch cultures, no significant differences, regardless of medium composition, were found in growth rate and glucose uptake rate between the host strains and the recombinant strains expressing thepdc andadh genes. In the continuous cultures performed with glucose minimal medium, however, the recombinant strains gave more biomass than the host strains at the same specific growth rates. On the contrary, in the continuous cultures with complex medium, the host strains yielded more biomass than the recombinant strains. Analysis of the culture supernatants revealed that the effect of thepdc andadh expression on byproduct formation was more significant at low specific growth rates than at high specific growth rates. This study suggests that physiological and environmental conditions should be carefully considered and precisely defined in assessing the effects of heterologous gene expression on metabolic activities of recombinantE. coli.     

Glucose transport into the extremely halophilic archaebacteria

Penetration of glucose into cells of several extremely halophilic archaebacteria of the Halobacterium and Haloferax genera (Halobacterium saccharovorum and Halobacterium salinarium, Haloferax volcanii and Haloferax mediterranei) has been studied. Some characteristics of transport systems of carbohydrate-utilizing halobacteria Halobacterium saccharovorum, Haloferax mediterranei and Haloferax volcanii (pH and temperature optima, stereospecificity, kinetic parameters) have been determined. Inability of H. salinarium cells for active glucose transport has been shown. The dependence of glucose transport on the Na⁺ ions gradient (on the whole cells and membrane vesicles) has been demonstrated. Cells or membrane vesicles of carbohydrate-utilizing halobacteria grown in media containing this sugar indicated the activation of glucose transport, whereas cells grown in media without sugars did not. This fact has allowed us to conclude that corresponding transport systems are inducible.     

Role of veratryl alcohol in lignin degradation by Phanerochaete chrysosporium

Several aromatic compounds increased initial lignin degradation rates in cultures of Phanerochaete chrysosporium. This activation was connected to increased H₂O₂ production and glucose oxidation rates. Veratryl alcohol, a natural secondary metabolite of P. chrysosporium, also activated the lignin-degrading system. In the presence of added veratryl alcohol the ligninolytic system appeared 6–8 h earlier than in reference cultures. This effect was only seen when lignin was added after the primary growth was completed because lignin itself also caused earlier appearance of the degradative system. In cultures which received no added lignin or veratryl alcohol the ligninolytic activity only appeared once the alcohol started to accumulate. The degradation patterns of veratryl alcohol and lignin were similar. The activity levels of lignin degradation and glucose oxidation could be regulated by veratryl alcohol concentration. It is suggested that either veratryl alcohol itself or a metabolite derived from it is actually responsible for the low levels of ligninolytic activity in glucose grown cultures.     

Legume-Rhizobium interactions: host induced alterations in capsular polysaccharides and infectivity of cowpea Rhizobia

Klebsiella aerogenes NCTC418 was cultured anaerobically under glucose-limited conditions in chemostat cultures at various growth rates, ranging from 0.13 h^-1 to 0.82 h^-1. It was found that the specific uptake rate of glucose varied linearly with the growth rate and that under these conditions glucose was fermented solely to acetate and ethanol plus CO₂+H₂ and formate.When steady-state cultures were pulsed with cell saturating concentrations of glucose, the specific glucose aptake rate increased immediately and substantially. However, at steady-state growth rates lower than 0.5 h^-1, this increase was not accompanied by a change in the growth rate, in contrast to cultures growing at higher rates. It was found that relief of the glucose limitation resulted in a shift in fermentation pattern: at the lower growth rates 50% or more of the extra glucose taken up was fermented to D-lactate.Incubation experiments with sonified cells revcaled that K. aerogenes possessed all the enzymes needed to convert dihydroxyacetone phosphate to methylglyoxal and subsequently to D-lactate, and that the rate at which this overall conversion occurred in vitro was in close agreement with the production rate of D-lactate in vivo. Moreover, it was found that the activities of the enzymes of the methylglyoxal bypass were dependent on the imposed growth rate. At higher growth rates, where cells possessed the potential to increase their growth rate immediately, the activity of methylglyoxal synthase was relatively low.it could be shown that, under low growth rate conditions, the uncoupling effect of the methylglyoxal bypass was highly effective and that, as a consequence thereof, a significant increase in the uptake rate of the energy source was accompanied by only a marginal increase in the rate at which ATP was synthesized.     

Transport kinetics of maltotriose in strains ofSaccharomyces

Summary Maltotriose transport was studied in two brewer's yeast strains, an ale strain 3001 and a lager strain 3021, using laboratory-synthesized¹⁴C-maltotriose. The maltotriose transport systems preferred a lower pH (pH 4.3) to a higher pH (pH 6.6). Two maltotriose transport affinity systems have been indentified. The high affinity system hasK _m values of 1.3 mM for strain 3021 and 1.4 mM for strain 3001. The low affinity competitively inhibited by maltose and glucose withK _i values of 58 mM and 177 mM. respectively, for strain 3021, and 55 mM and 147 mM, respectively, for strain 3001. Cells grown in maltotriose and maltose had higher maltotriose and maltose transport rates, and cells grown in glucose had lower maltortriose and maltose transport rates. Early-logarithmic phase cells transported glucose faster than either maltose or maltotriose. Cells harvested later in the growth phase had increased maltotriose and maltose transport activity. Neither strain exhibited significant differences with respect to maltose and maltotriose transport activity.     

Glucose and acetate influences on the behavior of the recombinant strainEscherichia coli HB 101 (GAPDH)

Summary This study highlights data about the production of a recombinant protein (glyceraldehyde-3-phosphate dehydrogenase) byE. coli HB 101 (GAPDH) during batch and fed-batch fermentations in a complex medium. From a small number of experiments, this strain has been characterized in terms of protein production performance and glucose and acetate influences on growth and recombinant protein production. The present results show that this strain is suitable for recombinant protein production, in fed-batch culture 55 g L^–1 of biomass and 6 g L^–1 of GAPDH are obtained. However this strain, and especially GAPDH overproduction is sensitive to glucose availability. During fermentations, maximum yields of GAPDH production have been obtained in batch experiments for glucose concentration of 10 g L^–1, and in fed-batch experiments for glucose availability of 10 g h^–1 (initial volume 1.5 L). The growth of the strain and GAPDH overproduction are also inhibited by acetate. Moreover acetate has been noted as an activator of its own formation.     

Growth of Saccharomyces cerevisiae in a chemostat under high glucose conditions

Saccharomyces cerevisiae was grown in a chemostat under high glucose conditions (up to 300 g l^–1). The results support the view that higher glucose feed favors higher ethanol production regardless of the existence of osmotic stress. A low glucose utilization and yield coefficient provides an opportunity to improve continuous fermentation performance in the fuel alcohol industry. The possibility exists of reusing yeast cells and subsequently lower operating costs, and by using an optimal glucose feeding concentration between 100 and 200 g l^–1.     

Plasma glucose kinetics and tissue uptake in brown trout in vivo: effect of an intravascular glucose load

The object of the present study was to elucidate whether a glucose load modifies glucose uptake by tissues in brown trout in vivo. By the use of 2-[1,2-³H]-deoxyglucose, plasma glucose disappearance rate and tissue glucose uptake were measured after an intraaortic glucose load of 500 mg·kg^-1 (glucose load group) and under normoglycemic conditions (control). We also attempted to determine whether fasting modifies the glucose load disposal (fasted glucose load group). The procedure used to calculate 2-deoxyglucose uptake by tissues was evaluated, and the levels of 2-deoxyglucose uptake were compared with those of 2-deoxyglucose phosphorylation. Uptake and phosphorylation rates were similar in all tissues, except in brain and heart. In all the groups glucose uptake rates were highest in spleen, kidney, brain and gills, and lowest in red muscle, heart and white muscle. However, white muscle was the main site of glucose uptake on a whole tissue basis. The glucose load led to strong, long-lasting hyperglycemia, in spite of the increases observed in plasma insulin levels and in glucose uptake rate by the whole body (control: 4.9 mol·min^-1·kg^-1; glucose load group: 6.5 mol·min^-1·kg^-1). This higher rate was due to the higher glucose uptake only in white and red muscles (four- and threefold, respectively). Fasting halved the uptake of glucose by both red and white muscles in the load condition. In consequence the use of exogenous glucose decreased with fasting (fasted glucose load group: 5.1 mol·min^-1·kg^-1), causing still longer hyperglycemia.Abbreviations bw body weight - 2DG 2-[1,2-³H]-deoxyglucose - 2DG-P 2-[1,2-³H]-deoxyglucose phosphate - dpm disintegrations per min - FGL fasted glucose load group - GL glucose load group - G-6-Pase glucose-6-phosphatase - LG L-[1-¹⁴C]-glucose - MS-222 3-aminobenzoic acid ethyl ester methanesulphonate salt     

Crabtree-negative characteristics of recombinant xylose-utilizing Saccharomyces cerevisiae

For recombinant xylose-utilizing Saccharomyces cerevisiae, ethanol yield and productivity is substantially lower on xylose than on glucose. In contrast to glucose, xylose is a novel substrate for S. cerevisiae and it is not known how this substrate is recognized on a molecular level. Failure to activate appropriate genes during xylose-utilization has the potential to result in sub-optimal metabolism and decreased substrate uptake. Certain differences in fermentative performance between the two substrates have thus been ascribed to variations in regulatory response. In this study differences in substrate utilization of glucose and xylose was analyzed in the recombinant S. cerevisiae strain TMB3400. Continuous cultures were performed with glucose and xylose under carbon- and nitrogen-limited conditions. Whereas biomass yield and substrate uptake rate were similar during carbon-limited conditions, the metabolic profile was highly substrate dependent under nitrogen-limited conditions. While glycerol production occurred in both cases, ethanol production was only observed for glucose cultures. Addition of acetate and 2-deoxyglucose pulses to a xylose-limited culture was able to stimulate transient overflow metabolism and ethanol production. Application of glucose pulses enhanced xylose uptake rate under restricted co-substrate concentrations. Results are discussed in relation to regulation of sugar metabolism in Crabtree-positive and -negative yeast.     

Contributions of XyIR, CcpA andcre to diauxic growth ofBacillus megaterium and to xylose isomerase expression in the presence of glucose and xylose

Bacillus megaterium shows diauxic growth in minimal medium containing glucose and xylose. We have examined the influence of three elements that regulatexyl operon expression on diauxic growth and expression of axylA-lacZ fusion.xylA is 13-fold repressed during growth on glucose. Induction occurs at the onset of the lag phase after glucose is consumed. Inactivation ofxylR yields a two-fold increase in expression ofxylA on glucose. Deletion of the catabolite responsive element (cre) has a more pronounced effect, reducing glucose repression from 13-fold in the wild type to about 2.5-fold. WhenxylR andcre are inactivated together a residual two-fold repression ofxylA is found. Inactivation ofxylR affects diauxic growth by shortening the lag phase from 70 to 40 min. In-frame deletion ofccpA results in the loss of diauxic growth, an increase in doubling time and simultaneous use of both sugars. In contrast, a strain with an inactivatedcre site inxylA exhibits diauxic growth without an apparent lag phase on glucose and xylose, whereas fructose and xylose are consumed simultaneously.     

Inhibition of <Emphasis Type="Italic">Pichia stipitis</Emphasis> fermentation of hydrolysates from olive tree cuttings

The ethanolic fermentation of liquid fractions (hydrolysates) issued from dilute acid pre-treatment of olive tree biomass by Pichia stipitis is reported for the first time. On the one side, P. stipitis has been reported as the most promising naturally occurring C5 fermenting microorganism; on the other side, olive tree biomass is a renewable, low cost, and lacking of alternatives agricultural residue especially abundant in Mediterranean countries. The study was performed in two steps. First, the fermentation performance of P. stipitis was evaluated on a fermentation medium also containing the main inhibitors found in these hydrolysates (acetic acid, formic acid, and furfural), as well as glucose and xylose as carbon sources. The effect of inhibitors, individually or in a mixture, on kinetic and yield parameters was calculated. In a second step, hydrolysates obtained from 1% (w/w) sulfuric acid pre-treatment of olive tree biomass at 190°C for 10 min were used as a real fermentation medium with the same microorganism. Due to inhibition, effective fermentation required dilution of the hydrolysate and either overliming or activated charcoal treatment. Results show that ethanol yields obtained from hydrolysates, ranging from 0.35 to 0.42 g/g, are similar to those from synthetic medium, although the process proceeds at lower rates. Inhibiting compounds affect the fermentation performance in a synergistic way. Furfural is rapidly assimilated by the yeast; acetic acid and formic acid concentrations decrease slowly during the process. Activated charcoal or overliming detoxification improve the fermentability of diluted hydrolysates.     

Biokinetic parameters and behavior of <Emphasis Type="Italic">Aeromonas hydrophila</Emphasis> during anaerobic growth

The biokinetics of glucose metabolism were evaluated in Aeromonas hydrophila during growth in an anaerobic biosystem. After approx 34 h growth, A. hydrophila metabolized 5,000 mg glucose l⁻¹ into the end-products ethanol, acetate, succinate and formate. The maximum growth rate, μ _m, half saturation coefficients, K _s, microbial yield coefficient, Y, cell mass decay rate coefficient, k _d, and substrate inhibition coefficient, K _si were 0.25 ± 0.03 h⁻¹, 118 ± 31 mg glucose l⁻¹, 0.12 μg DNA mg glucose⁻¹, 0.01 h⁻¹, and 3,108 ± 1,152 mg glucose l⁻¹, respectively. These data were used to predict the performance of a continuous growth system with an influent glucose concentration of 5,000 mg l⁻¹. Results of the analysis suggest that A. hydrophila will metabolize glucose at greater than 95% efficiency when hydraulic retention times (HRTs) exceed 7 h, whereas the culture is at risk of washing out at an HRT of 6.7 h.     

Methanol metabolism in yeasts: Regulation of the synthesis of catabolic enzymes

The regulation of the synthesis of four dissimilatory enzymes involved in methanol metabolism, namely alcohol oxidase, formaldehyde dehydrogenase, formate dehydrogenase and catalase was investigated in the yeasts Hansenula polymorpha and Kloeckera sp. 2201. Enzyme profiles in cell-free extracts of the two organisms grown under glucose limitation at various dilution rates, suggested that the synthesis of these enzymes is controlled by derepression — represion rather than by induction — repression. Except for alcohol oxidase, the extent to which catabolite repression of the catabolic enzymes was relieved at low dilution rates was similar in both organisms. In Hansenula polymorpha the level of alcohol oxidase in the cells gradually increased with decreasing dilution rate, whilst in Kloeckera sp. 2201 derepression of alcohol oxidase synthesis was only observed at dilution rates below 0.10 h^–1 and occurred to a much smaller extent than in Hansenula polymorpha.Derepression of alcohol oxidase and catalase in cells of Hansenula polymorpha was accompanied by synthesis of peroxisomes. Moreover, peroxisomes were degraded with a concurrent loss of alcohol oxidase and catalase activities when excess glucose was introduced into the culture. This process of catabolite inactivation of peroxisomal enzymes did not affect cytoplasmic formaldehyde dehydrogenase.     

Energy requirements for microbial exopolysaccharide synthesis

Calculations indicate that at the high specific rates of exopolysaccharide synthesis obtained in continuous cultures of Xanthomonas campestris and mucoid Pseudomonas aeruginosa strains the ATP demand for this synthesis is a significant proportion of total cellular ATP demand. However, depending upon the proportion of polymer substituents more oxidised than the carbohydrate substrate, some, and in certain cases all of this energy can be provided via NAD(P)H₂ produced during exopolysaccharide synthesis. For xanthan production by X. campestris a P/O ratio of 2.2 to 2.6, depending on the content of pyruvyl substituents, would be necessary for energy generation as a direct result of xanthan synthesis to support the ATP demand for this synthesis. In sulphur-limited cultures of X. campestris, however, energy metabolism is shown to be inefficient, the organism exhibiting either a low P/O ratio or low Y _ATP. In such cultures the yield of exopolysaccharide from glucose was 0.62/g glucose compared with maximum theoretical yields of 0.81 to 0.87/g glucose for P/O ratio of 1 to 3.