Energetics of glucose uptake in a Salmonella typhimurium mutant containing uncoupled enzyme IIGlc

Uncoupled enzyme II^Glc of the phosphoenolpyruvate (PEP): glucose phosphotransferase system (PTS) in Salmonella typhimurium is able to catalyze glucose transport in the absence of PEP-dependent phosphorylation. We have studied the energetics of glucose uptake catalyzed by this uncoupled enzyme II^Glc. The molar growth yields on glucose of two strains cultured anaerobically in glucose-limited chemostat-and batch cultures were compared. Strain PP 799 transported and phosphorylated glucose via an intact PTS, while strain PP 952 took up glucose exclusively via uncoupled enzyme II^Glc, followed by ATP-dependent phosphorylation by glucokinase. Thus the strains were isogenic except for the mode of uptake and phosphorylation of the growth substrate. PP 799 and PP 952 exhibited similar Y _Glc values. Assuming equal Y _ATP values for both strains this result indicated that there were no energetic demands for glucose uptake via uncoupled enzyme II^Glc.Abbreviations PTS phosphoenolpyruvate: carbohydrate phosphotransferase system - HPr histidine-containing phosphocarrier protein - GalP galactose permease     

Energetic aspects of anaerobic growth of Aerobacter aerogenes in complex medium

Molar growth yields for anaerobic growth of Aerobacter aerogenes in complex medium were much higher than for growth in minimal medium. In batch cultures the molar growth yield for glucose varied from 44 to 50 and Y _ATP from 17.1 to 18.8. For glucose-limited chemostat cultures a value of 17.5 g/mole was found for Y _ATP ^max and a value of 2.3 mmoles ATP/g dry weight h for the maintenance coeficient. Growth dependent pH changes were used to control the addition of fresh medium, containing excess of glucose to a continuous culture. The specific growth rate and the population density were dependent on the pH difference between the inflowing medium and the culture. At a value of 1.44 h^-1 the molar growth yield for glucose was about 70 and Y _ATP about 28.5. An-equation is presented, which gives the relation between theoretical and experimental Y _ATP ^max values.     

Continuous and biomass recycle fermentations of Clostridium acetobutylicum

Using experimental data from continuous cultures of Clostridium acetobutylicum with and without biomass recycle, relationships between product formation, growth and energetic parameters were explored, developed and tested. For glucose-limited cultures the maintenance models for, the Y _ATP and biomass yield on glucose, and were found valid, as well as the following relationships between the butanol (Y _B/G) or butyrate (Y _BE/G) yields and the ATP ratio (R _ATP, an energetic parameter), Y _B/G =0.82-1.35 R _ATP, Y _BE/G =0.54 + 1.90 R _ATP. For non-glucose-limited cultures the following correlations were developed, Y _B/G =0.57-1.07 , Y _B/G =0.82-1.35 R _ATPATP and similar equations for the ethanol yield. All these expressions are valid with and without biomass recycle, and independently of glucose feed or residual concentrations, biomass and product concentrations. The practical significance of these expressions is also discussed.List of Symbols D h^–1 dilution rate - m _e mol g^–1 h^–1 maintenance energy coefficient - m _G mol g^–1 h^–1 maintenance energy coefficient - R biomass recycle ratio, (dimensionless) - R _ATP ATP ratio (eqs.(5), (10) and (11)), (dimensionless) - X kg/m³ biomass concentration - Y _ATP g biomass per mol ATP biomass yield on ATP - Y _ATP ^max g biomass per mol ATP maximum Y _ATP - Y _A/G mol acetate produced per mol glucose consumed molar yield of acetate - y _an/g mol acetone produced per mol glucose consumed molar yield of acetone - Y _B/G mol butanol produced per mol glucose consumed molar yield of butanol - y _be/g mol butyrate produced per mol glucose consumed molar yield of butyrate - Y _E/G mol ethanol produced per mol glucose consumed molar yield of ethanol - Y _X/G g biomass per mol glucose consumed biomass yield on glucose - Y _ATP ^max g biomass per mol maximum Y _X/G glucose consumed - h^–1 specific growth rate     

Glucose as an energy donor in acetate growing Acinetobacter calcoaceticus

Since glucose can be oxidized but not assimilated by Acinetobacter calcoaceticus 69-V the question arose whether energy generated by glucose oxidation can help incorporate carbon from heterotrophic substrates and, if so, what the efficiency of ATP production is like. For this reason this species was grown in the chemostat on acetate. After having reached steady state conditions an increasing concentration of glucose was added. This led to an increase in the biomass level from about 0.4 g/g for growth on acetate alone to 0.6–0.65 g/g in the presence of glucose, independently of either the growth rate or the steepness of the glucose gradient used. This upper value approximates about the limit of the carbon conversion efficiency calculated for non-glycolytic substrates. Glucose was almost exclusively oxidized to gluconic acid, 2- and 5-ketogluconates, and pentose 5-phosphates were found only in traces. These results demonstrate that glucose functions as an additional energy source in Acinetobacter calcoaceticus 69-V. From the transient behaviour of biomass increase and the mixing proportion at which the maximum growth yield on acetate in the presence of glucose was obtained it followed that two mol of ATP must have been generated per mol of glucose oxidized. This property is discussed in terms of coupling glucose dehydrogenase with the respiratory chain.Abbreviations G _ox glucose oxidized to gluconic acid - G _t amount of glucose necessary for complete substitution of S _d - S _o inlet concentration of the limiting carbon substrate - S _a and S _d assimilated and dissimilated part respectively of the carbon substrate - PQQ pyrrolo-quinoline-quinone - V _ATP ^Ac ATP gain from complete oxidation to CO₂ of acetate (P/O=2) - V _ATP ^Glc ATP gain from oxidation of glucose to gluconic acid     

Growth and fermentation responses of Selenomonas ruminantium to limiting and non-limiting concentrations of ammonium chloride

 The objective of this study was to assess fermentation product, growth rate and growth yield responses of Selenomonas ruminantium HD₄ to limiting and non-limiting ammonia concentrations. The ammonia half-inhibition constant for S. ruminantium in batch culture was 296 mM. Cells were grown in continuous culture with a defined ascorbate-reduced basal medium containing either 0.5, 5, 25, 50, 100 or 200 mM NH₄Cl and dilution rates were 0.07, 0.14, 0.24 or 0.40 h^-1. Ammonia was the growth-limiting nutrient when 0.5 mM NH₄Cl was provided and the half-saturation constant was 72 μM. Specific rates of glucose utilization and fermentation acid carbon formation were highest for 0.5 mM NH₄Cl. Lactate production (moles per mole of glucose disappearing) increased at the fastest dilution rate (0.40 h^-1) for 5.0 mM NH₄Cl while acetate and propionate decreased when compared to slower dilutions (0.07 and 0.14 h^-1). Lactate production remained low while acetate and propionate remained high for all dilution rates when NH₄Cl concentrations were 25 mM or greater. Yield (Y _Glc and Y _ATP) were nearly doubled when NH₄Cl was increased from 0.5 mM (25.1 g cells/mol glucose used and 13.9 g cells/mol ATP produced respectively) to the higher concentrations. Y _Glc was highest at 25 mM and 50 mM NH₄Cl (48.2 cells/mol and 43.1 cells/mol respectively) as was Y _ATP (23.2 cells/mol and 20.8 cells/mol respectively). Y _NH3 was highest at the lowest NH₄Cl concentration. The maximal fermentation product formation rate occurred at a growth-limiting ammonia concentration, while maximal glucose and ATP bacterial yields occurred at non-growth-limiting ammonia concentrations. Given the growth response of this ruminal bacterium, it is possible that maximization of ruminal bacterial yield may necessitate sacrificing the substrate degradation rate and vice versa. Received: 5 December 1995/Received revision: 2 April 1996/Accepted: 22 April 1996     

A theoretical study on the amount of ATP required for synthesis of microbial cell material

The amount of ATP required for the formation of microbial cells growing under various conditions was calculated. It was assumed that the chemical composition of the cell was the same under all these conditions. The analysis of the chemical composition of microbial cells of Morowitz (1968) was taken as a base. It was assumed that 4 moles of ATP are required for the incorporation of one mole of amino acid into protein. The amount of ATP required on account of the instability and frequent regeneration of messenger RNA was calculated from data in the literature pertaining to the relative rates of synthesis of the various classes of RNA molecules in the cell. An estimate is given of the amount of ATP required for transport processes. For this purpose it was assumed that 0.5 mole of ATP is necessary for the uptake of 1 g-ion of potassium or ammonium, and 1 mole of ATP for the uptake of 1 mole of phosphate, amino acid, acetate, malate etc. The results of the calculations show that from preformed monomers (glucose, amino acids and nucleic acid bases) 31.9 g cells can be formed per g-mole of ATP when acetyl-CoA is formed from glucose. When acetyl-CoA cannot be formed from glucose and must be formed from acetate, Y _ATP ^MAX is only 26.4. For growth with glucose and inorganic salts a Y _ATP ^MAX value of 28.8 was found. Addition of amino acids was without effect on Y _ATP ^MAX but addition of nucleic acid bases increased the Y _ATP ^MAX value to that for cells growing with preformed monomers. Under these conditions 15–20% of the total ATP required for cell formation is used for transport processes. Much lower Y _ATP ^MAX values are found for growth with malate, lactate or acetate and inorganic salts. During growth on these substrates a greater part of the ATP required for cell formation is used for transport processes. The calculated figures are very close to the experimental values found. The interrelations between Y _ATP ^MAX and Y_ATP, the specific growth rate (μ), the maintenance coefficient (m_e) and the P/O rate are given. From a review of the literature evidence is presented that these parameters may vary under different growth conditions. It is concluded that in previous studies on the relation between ATP production and formation of cell material these effects have unjustly been neglected.     

Metabolic and energetic aspects of the growth of Clostridium butyricum on glucose in chemostat culture

The influence of a number of environmental parameters on the fermentation of glucose, and on the energetics of growth of Clostridium butyricum in chemostat culture, have been studied. With cultures that were continuously sparged with nitrogen gas, glucose was fermented primarily to acetate and butyrate with a fixed stoichiometry. Thus, irrespective of the growth rate, input glucose concentration specific nutrient limitation and, within limits, the culture pH value, the acetate/butyrate molar ratio in the culture extracellular fluids was uniformly 0.74±0.07. Thus, the efficiency with which ATP was generated from glucose catabolism also was constant at 3.27±0.02 mol ATP/mol glucose fermented. However, the rate of glucose fermentation at a fixed growth rate, and hence the rate of ATP generation, varied markedly under some conditions leading to changes in the Y _glucose and Y _ATP values. In general, glucose-sufficient cultures expressed lower yield values than a correponding glucose-limited culture, and this was particularly marked with a potassium-limited culture. However, with a glucose-limited culture increasing the input glucose concentration above 40g glucose·l^-1 also led to a significant decrease in the yield values that could be partially reversed by increasing the sparging rate of the nitrogen gas. Finally glucose-limited cultures immediately expressed an increased rate of glucose fermentation when relieved of their growth limitation. Since the rate of cell synthesis did not increase instantaneously, again the yield values with respect to glucose consumed and ATP generated transiently decreased.Two conditions were found to effect a change in the fermentation pattern with a lowering of the acetate/butyrate molar ratio. First, a significant decrease in this ratio was observed when a glucose-limited culture was not sparged with nitrogen gas; and second, a substantial (and progressive) decrease was observed to follow addition of increasing amounts of mannitol to a glucose-limited culture. In both cases, however, there was no apparent change in the Y _ATP value.These results are discussed with respect to two imponder-ables, namely the mechanism(s) by which C. butyricum might partially or totally dissociate catabolism from anabolism, and how it might dispose of the excess reductant [as NAD(P)H] that attends both the formation of acetate from glucose and the fermentation of mannitol. With regards to the latter, evidence is presented that supports the conclusion that the ferredoxin-mediated oxidation of NAD(P)H, generating H₂, is neither coupled to, nor driven by, an energy-yielding reaction.     

A continuous culture study of an ATPase-negative mutant of Escherichia coli

For anaerobic glucose-limited chemostat cultures of Escherichia coli a value of 8.5 was found for Y _ATP ^max . For anaerobic glucose- or ammoniumlimited chemostat cultures of the ATPase-negative mutant M2-6 of E. coli Y _ATP ^max values of 17.6 and 20.0 were found, respectively. From these data it can be concluded that in the wild type during anaerobic growth 51–58% of the total ATP production is used for energetization of the membrane. Using the Y _ATP values obtained in the anaerobic experiments a P/O ratio of 1.46 could be calculated for aerobic experiments with the wild type. It is concluded that from the energy obtained by respiration in wild type E. coli about 60% is used for membrane energetization and only about 40% for the actual formation of ATP. No dramatic difference in the maintenance requirement for ATP or glucose has been observed between glucose- and ammonium-limited chemostat cultures of the mutant. The large difference in maintenance requirement observed for such cultures of the wild type is therefore supposed to be made possible by ATP hydrolysis by the ATPase.     

The growth of Saccharomyces cerevisiae CBS 426 on mixtures of glucose and ethanol: a model

Saccharomyces cerevisiae CBS 426 was grown in continuous culture in a defined medium with a mixture of glucose and ethanol as carbon source. Growth on ethanol as the sole carbon source was only possible after the addition of a small amount of glutamic acid. The flows of glucose, ethanol, oxygen, carbon dioxide and biomass to and from the system were measured and a model for the growth of the yeast on the carbon sources constructed. The model is shown to allow independent estimation of Y_ATP and P/O. Y_ATP is not independent of the substrate used, but the amount of ATP used in the production of biomass from the monomers is approximately the same for growth on ethanol and on glucose.Nomenclature C chemical state vector - C_i component of the chemical state vector (C-mol) - C_x biomass present in the system (C-mol biomass) - H₂ reduction equivalents (NAD(P)H + H⁺ and FADH₂) - k the amount of ATP required in the production of 1 C-mol of biomass from the monomers (mol ATP/C-mol biomass) - m_ATP maintenance requirement for ATP (mol ATP/C-mol biomass·h) - P/O (=), efficiency of the oxidative phosphorylation (mol ATP/atom O) - r vector of reaction rates - r_i component of the vector of reaction rates (C-mol/h) - r_ATP rate of ATP production (mol ATP/h) - r_x rate of biomass production (C-mol biomass/h) - Y_ATP Y_ATP growth yield on ATP (C-mol biomass/mol ATP) - (Y_ATP)_max maximum growth yield on ATP - stoichiometry matrix - P/O - vector of the flows to the system - _s flow of glucose to the system (C-mol glucose/h) - _o flow of oxygen to the system (mol O₂/h) - _c flow of carbon dioxide to the system (mol CO₂/h) - _x flow of biomass to the system (C-mol biomass/h) - _e flow of ethanol to the system (C-mol ethanol/h) - _w flow of water produced during metabolism (mol H₂O/h)     

Estimation of the energetic biomass yield and efficiency of oxidative phosphorylation in cell-recycle cultures of Schizosaccharomyces pombe

The energetics of growth of the fission yeast Schizosaccharomyces pombe was studied in continuous high-cell concentration cultures using a cell-recycle fermentor. Under non-O₂-limited conditions, steady-states were obtained at various specific growth rates (partial cell-recycle) with purely oxidative (glucose limitation) or respiro-fermentative (glucose excess) metabolic behaviour. The stoichiometry of biomass synthesis was established from the elemental composition of the cells and measurements of all the specific metabolic rates, i.e. consumption of glucose and O₂ and production of CO₂, ethanol and other products. The theoretical yield factor for biomass on glucose was Y_G,X = 0.85 C-mol·C-mol^–1 and maintenance requirements were negligible. Assuming a constant coupling between energy generation and biomass formation for both respirative and respiro-fermentative breakdown of glucose, the biomass yield from ATP (Y_ATP) and the efficiency of oxidative phosphorylation (P/O ratio) could be determined as 9.8 g biomass·mol ATP and 1.28 mol ATP·atom of O₂, respectively. Correspondence to: A. Pareilleux     

Growth characteristics of Saccharomyces cerevisiae S288C in changing environmental conditions: auxo-accelerostat study

The effect of individual environmental conditions (pH, pO₂, temperature, salinity, concentration of ethanol, propanol, tryptone and yeast extract) on the specific growth rate as well as ethanol and glycerol production rate of Saccharomyces cerevisiae S288C was mapped during the fermentative growth in aerobic auxo-accelerostat cultures. The obtained steady-state values of the glycerol to ethanol formation ratio (0.1 mol mol⁻¹) corresponding to those predicted from the stoichiometric model of fermentative yeast growth showed that the complete repression of respiration was obtained in auxostat culture and that the model is suitable for calculation of Y _ATP and Q _ATP values for the aerobic fermentative growth. Smooth decrease in the culture pH and dissolved oxygen concentration (pO₂) down to the critical values of 2.3 and 0.8%, respectively, resulted in decrease in growth yield (Y _ATP) and specific growth rate, however the specific ATP production rate (Q _ATP) stayed almost constant. Increase in the concentration of biomass (>0.8 g dwt l⁻¹), propanol (>2 g l⁻¹) or NaCl (>15 g l⁻¹) lead at first to the decrease in the specific growth rate and Q _ATP, while Y _ATP was affected only at higher concentrations. The observed decrease in Q _ATP was caused by indirect rather than direct inhibition of glycolysis. The increase in tryptone concentration resulted in an increase in the specific growth rate from 0.44 to 0.62 h⁻¹ and Y _ATP from 12.5 to 18.5 mol ATP g dwt⁻¹. This study demonstrates that the auxo-accelerostat method, besides being an efficient tool for obtaining the culture characteristics, provides also decent conditions for the experiments elucidating the control mechanisms of cell growth.     

Expression of Galactose Permease and Pyruvate Carboxylase in Escherichia coli ptsG Mutant Increases the Growth Rate and Succinate Yield under Anaerobic Conditions

In Escherichia coli, disruption of ptsG, which encodes the glucose-specific permease of the phosphotransferase transport system (PTS) protein EIICB^Glc, is crucial for high succinate production. This mutation can, however, cause very slow growth and low glucose consumption rates. The ptsG mutant (TUQ2), from wild type E. coli W1485, and E. coli galP (encoding galactose permease) and glk (encoding glucose kinase) gene expression plasmids were constructed. TUQ2 increased the generation time to approximately 4 h and gave a higher final cell density of 0.5 g/l by expression of galP. However, glk expression had no effect on the mutant. After expression of pyruvate carboxylase (PYC) and galactose permease, the ptsG mutant showed higher succinate yield (1.2 mol/mol glucose) and the specific rate of glucose consumption from 0.33 to 0.6 g/1 h. Received 31 August 2005; Revisions requested 27 September 2005; Revisions received 1 November 2005; Accepted 2 November 2005 An erratum to this article is available at .     

Uncoupler-Resistant Glucose Uptake by the Thermophilic Glycolytic Anaerobe Thermoanaerobacter thermosulfuricus (Clostridium thermohydrosulfuricum)

The transport of glucose across the bacterial cell membrane of Thermoanaerobacter thermosulfuricus (Clostridium thermohydrosulfuricum) Rt8.B1 was governed by a permease which did not catalyze concomitant substrate transport and phosphorylation and thus was not a phosphoenolpyruvate-dependent phosphotransferase. Glucose uptake was carrier mediated, could not be driven by an artificial membrane potential (Δψ) in the presence or absence of sodium, and was not sensitive to inhibitors which dissipate the proton motive force (Δp; tetrachlorosalicylanilide, N,N-dicyclohexylcarboiimide, and 2,4-dinitrophenol), and no uptake of the nonmetabolizable analog 2-deoxyglucose could be demonstrated. The glucokinase apparent K_m for glucose (0.21 mM) was similar to the K_t (affinity constant) for glucose uptake (0.15 mM), suggesting that glucokinase controls the rate of glucose uptake. Inhibitors of ATP synthesis (iodoacetate and sodium fluoride) also inhibited glucose uptake, and this effect was due to a reduction in the level of ATP available to glucokinase for glucose phosphorylation. These results indicated that T. thermosulfuricus Rt8.B1 lacks a concentrative uptake system for glucose and that uptake is via facilitated diffusion, followed by ATP-dependent phosphorylation by glucokinase. In T. thermosulfuricus Rt8.B1, glucose is metabolized by the Embden-Meyerhof-Parnas pathway, which yields 2 mol of ATP (G. M. Cook, unpublished data). Since only 1 mol of ATP is used to transport 1 mol of glucose, the energetics of this system are therefore similar to those found in bacteria which possess a phosphotransferase.     

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.     

Energetics of growth of Microbacterium thermosphactum at low temperatures

Microbacterium thermosphactum was grown at 5°C and 9°C in glucose-limited continuous cultures. The end products of glucose metabolism were L-lactate and ethanol, and these compounds accounted for 86–92% of the glucose utilized. With input glucose concentrations less than 3 mM Y _glu ^Max was found to be 40–43, Y _ATP ^Max 20–21 and m _s 0.1–0.2. These values are almost identical to those found previously for cultures at 25°C and show that this psychrotroph grows with a very high energetic efficiency over a wide range of temperatures. With a higher (but still limiting) input glucose concentration of 5.6 mM at 9°C, cellular efficiency declined as there was a marked reduction in Y _glu. This decrease was accounted for in mathematical terms by an increase in m _s to 0.7, whilst Y _glu ^Max and Y _ATP ^Max remained high at 38 and 19 respectively.     

Carbon monoxide gasing leads to alcohol production and butyrate uptake without acetone formation in continuous cultures ofClostridium acetobutylicum

Summary When continuous, steady-state, glucose-limited cultures ofClostridium acetobutylicum were sparged with CO, the completely or almost completely acidogenic fermentations became solventogenic. Alcohol (butanol and ethanol) and lactate production at very high specific production rates were initiated and sustained without acetone, and little or no acetate and butyrate formation. In one fermentation, strong butyrate uptake without acetone formation was observed. Growth could be sustained even with 100% inhibition of H₂ formation. Although CO gasing inhibited growth up to 50%, and H₂ formation up to 100%, it enhanced the rate of glucose uptake up to 300%. TheY _ATP was strongly affected and mostly reduced with respect to its steady-state value. The results support the hypothesis that solvent formation is triggered by an altered electron flow.     

Energy production and growth of Pseudomonas oxalaticus OX1 on oxalate and formate

The efficiency of oxidative phosphorylation in Pseudomonas oxalaticus during growth on oxalate and formate was estimated by two methods. In the first method the amount of ATP required to synthesize cell material of standard composition was calculated during growth of the organism on either of the two substrates. The [Y _ATP ^max ] theor. values thus obtained were 12.5 and 6.5 for oxalate and formate respectively, if the assumption were made that no energy is required for transport of oxalate or carbon dioxide. When active transport of oxalate requiring an energy input equivalent to 1 mole of ATP per mole of oxalate was taken into account, [Y _ATP ^max ]theor. for oxalate was 9.4. True Y _ATP ^max values were derived from these data on the assumption that the energy produced in the catabolism of Pseudomonas oxalaticus is used with approximately the same efficiency as in a range of other chemoorganotrophs. P/O ratios were calculated using the equation P/O=Y _O/Y _ATP. The data for Y _O and m _e required for these calculations were obtained from cultures of Pseudomonas oxalaticus growing on oxalate or formate in carbon-limited continuous cultures. The P/O ratios calculated by this method were, for oxalate, 1.3 (or 1.0 if active transport were ignored), and for formate, 1.7.In the second method the stoicheiometries of the respiration-linked proton translocations with oxalate and formate were measured in washed suspensions of cells grown on the two substrates. The H⁺/O ratios obtained were 4.3 with oxalate and 3.9 with formate. These data indicate the presence of two functional phosphorylation sites in the electron transport chain of Pseudomonas oxalaticus during growth on both substrates. A comparison of the P/O ratio on oxalate obtained with the two methods indicated that the energy requirement for active transport of oxalate has a major effect on the energy budget of the cell; about 50% of the potentially available energy in oxalate is required for its active transport across the cell membrane. Translocation of formate requires approximately 25% of the energy potentially available in the substrate. These results offer an explanation for the fact that molar growth yields of Pseudomonas oxalaticus on oxalate and formate are not very different.Abbreviations PMS phenazinemethosulphate - DCPIP 2,6-dichlorophenolindophenol - TMPD N,N,N,N-tetramethyl-1,4-phenylene-diamine dihydrochloride - SD standard deviation - PEP Phosphoenol-pyruvate     

Hydrogen formation by an arsenate-reducing Pseudomonas putida, isolated from arsenic-contaminated groundwater in West Bengal, India

Anaerobic growth of a newly isolated Pseudomonas putida strain WB from an arsenic-contaminated soil in West Bengal, India on glucose, l-lactate, and acetate required the presence of arsenate, which was reduced to arsenite. During aerobic growth in the presence of arsenite arsenate was formed. Anaerobic growth of P. putida WB on glucose was made possible presumably by the non-energy-conserving arsenate reductase ArsC with energy derived only from substrate level phosphorylation. Two moles of acetate were generated intermediarily and the reducing equivalents of glycolysis and pyruvate decarboxylation served for arsenate reduction or were released as H₂. Anaerobic growth on acetate and lactate was apparently made possible by arsenate reductase ArrA coupled to respiratory electron chain energy conservation. In the presence of arsenate, both substrates were totally oxidized to CO₂ and H₂ with part of the H₂ serving for respiratory arsenate reduction to deliver energy for growth. The growth yield for anaerobic glucose degradation to acetate was Y _Glucose = 20 g/mol, leading to an energy coefficient of Y _ATP = 10 g/mol adenosine-5'-triphosphate (ATP), if the Emden–Meyerhof–Parnas pathway with generation of 2 mol ATP/mol glucose was used. During growth on lactate and acetate no substrate chain phosphorylation was possible. The energy gain by reduction of arsenate was Y _Arsenate = 6.9 g/mol, which would be little less than one ATP/mol of arsenate.     

Studies on substrate utilisation in l-valine-producing Corynebacterium glutamicum strains deficient in pyruvate dehydrogenase complex

The pyruvate dehydrogenase complex was deleted to increase precursor availability in Corynebacterium glutamicum strains overproducing l-valine. The resulting auxotrophy is treated by adding acetate in addition glucose for growth, resulting in the puzzling fact of gluconeogenic growth with strongly reduced glucose uptake in the presence of acetate in the medium. This result was proven by intracellular metabolite analysis and labelling experiments. To increase productivity, the SugR protein involved in negative regulation of the phosphotransferase system, was inactivated, resulting in enhanced consumption of glucose. However, the surplus in substrate uptake was not converted to l-valine; instead, the formation of up to 289 μM xylulose was observed for the first time in C. glutamicum. As an alternative to the genetic engineering solution, a straightforward process engineering approach is proposed. Acetate limitation resulted in a more efficient use of acetate as cosubstrate, shown by an increased biomass yield Y _X/Ac and improved l-valine formation.     

Glucose Fermentation by <Emphasis Type="Italic">Propionibacterium microaerophilum</Emphasis>: Effect of pH on Metabolism and Bioenergetic

pH affected significantly the growth and the glucose fermentation pattern of Propionibacterium microaerophilum. In neutral conditions (pH 6.5–7.5), growth and glucose fermentation rate (qs) were optimum producing propionate, acetate, CO₂, and formate [which together represented 90% (wt/wt) of the end products], and lactate representing only 10% (wt/wt) of the end products. In acidic conditions, propionate, acetate, and CO₂ represented nearly 100% (wt/wt) of the fermentation end products, whereas in alkaline conditions, a shift of glucose catabolism toward formate and lactate was observed, lactate representing 50% (wt/wt) of the fermentation end products. The energy cellular yields (Y _X/ATP), calculated (i) by taking into account extra ATP synthesized through the reduction of fumarate into succinate, was 6.1–7.2 g mol⁻¹. When this extra ATP was omitted, it was 11.9–13.1 g mol⁻¹. The comparison of these values with those of Y _X/ATP in P. acidipropionici and other anaerobic bacteria suggested that P. microaerophilum could not synthesize ATP through the reduction of fumarate into succinate and therefore differed metabolically from P. acidipropionici. Received: 8 April 2002 / Accepted: 8 May 2002