A continuous culture study of the bioenergetic aspects of growth and production of exocellular protease in Bacillus licheniformis

Summary Bacillus licheniformis S 1684 is able to produce an alkaline serine protease exocellularly. In glucose-limited chemostat cultures the specific rate of protease production was maximal at a -value of 0.22. Above this growth rate protease production was repressed. Dependent on 10–20% of the glucose input was used for exocellular product formation. The degree of reduction of exocellular products was 4.1.Maximum molar growth yields were high and indicate a high efficiency of growth. The values of Y _glu ^max and YO ₂ ^max were 83.8 and 53.3, respectively. When Y _glu ^max was corrected for the amount of glucose used for product formation a value of 100.3 was obtained. These high maximum molar growth yields are most probably caused by a high Y _ATP ^max . Anaerobic batch experiments showed a Y _ATP of 14.6.Sometimes the used strain was instable in cell morphology and protease production. Non-protease producing cells most probably develop from producing cells by mutation in the rel-gene. Producing cells most probably are relaxed (rel ^-) and non-producing cells stringent (rel ⁺).Glossary specific growth rate (h^-1) - Y _sub growth yield permol substrate (g biomass/mol) - Y ^max maximum molar growth yield, corrected for maintenance requirements (g biomass/mol) - Y ^max(corr) Y ^max corrected for product formation (g biomass/mol) - m _sub maintenance requirements (mol/g biomass·h) - m _sub(corr) maintenance requirements corrected for product formation (mol/g biomass·h) - Y _c fraction of organic substrate converted in biomass - z fraction of organic substrate converted in exocellular products - d fraction of organic substrate converted in CO₂ (g mol/g atom C) - Crec% carbon recovery % - average degree of reduction of exocellular products - P/O amount of ATP produced during electron-transport of 2 electrons to oxygen     

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     

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     

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.     

Growth and energy production in Bacteroides amylophilus

The molar growth yield (Y _m) of Bacteroides amylophilus strain WP91 on maltose was 68±2 g/mol when determined from batch cultures at the peaks of maximal growth. Continued incubation led to considerable cell lysis. When calculated from batch cultures in exponential phase (specific growth rate, =0.57 h^-1) Y _m was 101 g/mol. The maximum value of Y _m in maltose-limited chemostat cultures at the maximum dilution rate (D) attainable (D==0.39 h^-1) was about 79 g/mol. Ammonia-Fmited chemostat cultures metabolized maltose with a much reduced efficiency and this was associated with a difference in morphology and chemical composition of the cells. The theoretical maximum molar growth yields (Y _m ^max ) were 55 and 114 g/mol for ammonia- and maltose-limited growth respectively. However, if account was taken of extracellular nitrogen-containing material in ammonia-limited cultures, Y _m ^max became 60. The maintenance coefficient (m _s), estimated from the lines relating the specific rate of maltose consumption (q _m) and D (where m _s=q _m at D=0), was 7.4±0.6×10^-4 mol maltose/g x h for both nutrient limitations. A difference in maintenance energy demand, independent of growth-rate, could not account, therefore, for the observed differences in Y _m between ammonia- and maltose-limited growth.     

Heterotrophic growth of Thiobacillus acidophilus in batch and chemostat cultures

Heterotrophic growth of the facultatively chemolithoautotrophic acidophile Thiobacillus acidophilus was studied in batch cultures and in carbon-limited chemostat cultures. The spectrum of carbon sources supporting heterotrophic growth in batch cultures was limited to a number of sugars and some other simple organic compounds. In addition to ammonium salts and urea, a number of amino acids could be used as nitrogen sources. Pyruvate served as a sole source of carbon and energy in chemostat cultures, but not in batch cultures. Apparently the low residual concentrations in the steady-state chemostat cultures prevented substrate inhibition that already was observed at 150 M pyruvate. Molar growth yields of T. acidophilus in heterotrophic chemostat cultures were low. The Y _max and maintenance coefficient of T. acidophilus grown under glucose limitation were 69 g biomass · mol^–1 and 0.10 mmol · g^–1 · h^–1, respectively. Neither the Y _max nor the maintenance coefficient of glucose-limited chemostat cultures changed when the culture pH was increased from 3.0 to 4.3. This indicates that in T. acidophilus the maintenance of a large pH gradient is not a major energy-requiring process. Significant activities of ribulose-1,5-bisphosphate carboxylase were retained during heterotrophic growth on a variety of carbon sources, even under conditions of substrate excess. Also thiosulphate- and tetrathionate-oxidising activities were expressed under heterotrophic growth conditions.     

Growth yields and growth rates of Desulfovibrio vulgaris (Marburg) growing on hydrogen plus sulfate and hydrogen plus thiosulfate as the sole energy sources

Desulfovibrio vulgaris (Marburg) was grown on H₂ plus sulfate and H₂ plus thiosulfate as the sole energy sources and acetate plus CO₂ as the sole carbon sources. Conditions are described under which the bacteria grew exponentially. Specific growth rates () and molar growth yields (Y) at different pH were determined. and Y were found to be strongly dependent on the pH. Highest growth rates and molar growth yields were observed for growth on H₂ plus sulfate at pH 6.5 (=0.15h^-1; Y _{SO 4} ^2- =8.3g·mol^-1) and for growth on H₂ plus thiosulfate at pH 6.8 (=0.21h^-1; Y _{S 2}O ₃ ² =16.9g·mol^-1).The growth yields were found to increase with increasing growth rates: plots of 1/Y versus 1/ were linear. Via extrapolation to infinite growth rates a Y _SO4 ^2- /max of 12.2g·mol^-1 and a YS₂O ₃ ^2- /max of 33.5g·mol^-1 was obtained.The growth yield data are interpred to indicate that dissimilatory sulfate reduction to sulfide is associated with a net synthesis of 1 mol of ATP and that near to 3 mol of ATP are formed during dissimilatory sulfite reduction to sulfide.     

Cell yields of Escherichia coli during anaerobic growth on fumarate and molecular hydrogen

Escherichia coli was grown anaerobically on sodium fumarate and molecular hydrogen or sodium formate in continuous culture. The maximal growth yield and the maintenance coefficient were determined. In a mineral medium a Y _fum ^max value of 6.6 g dry weight per mol fumarate was found. This value increased to 7.5 when casamino acids were present in the medium. From these data and the corresponding Y _ATP ^max values it could be calculated that per mol of fumarate reduced, 0.4 mol of ATP became available for growth. In batch culture a Y_fum value of 4.8 g dry weight per mol fumarate was determined.     

Effect of different limitations in chemostat cultures on growth and production of exocellular protease byBacillus licheniformis

Summary Maximal molar growth yields (Y _sub ^max ) and protease production ofBacillus licheniformis S 1684 during NH ₄ ⁺ -, O₂-, and NH ₄ ⁺ +O₂-limitation with either glucose or citrate as carbon and energy source and during glucose-, and citratelimitation in chemostat cultures were determined. Protease production was repressed by excess ammonia when glucose served as C/E-source. Glucose and citrate repressed protease production during NH ₄ ⁺ -limitation. A low oxygen tension enbanced protease production at low -values. It was concluded that, besides ammonia repression, catabolite flux and oxygen tension influence protease production, indicating that the energy status of the cell is important for the level of protease production.Y _sub ^max -values were high during glucose-limitation and indicate a high efficiency of growth caused by a highY _ATP ^max . During NH ₄ ⁺ -, O₂-, and NH ₄ ⁺ +O₂-limitation with glucose as C/E-values were lower than during glucose limitation. The lowerY _sub ^max -values were due to a lower efficiency of energy conservation.Y _sub ^max -values during limitations with citrate as C/E-source were lower than during limitations with glucose as C/E-source.Nomenclature specific growth rate (h^-1) - Y _sub growth yield per mol substrate (g biomass/mol) - Y ^max maximal molar growth yield corrected for maintenance requirements (g biomass/mol) - Y ^max (corr) Y ^max corrected for product formation (g biomass/mol) - m _sub maintenance requirements (mol/g biomass·h) - m _sub (corr) maintenance requirements corrected for product formation (mol/g biomass·h) - q _port ^max maximal specific rate of protease production (E₄₄₀/mg DW·h)     

A re-assessment of bacterial growth efficiency: the heat production and membrane potential of Streptococcus bovis in batch and continuous culture

Glucose-limited, continuous cultures (dilution rate 0.1 h^-1) of Streptococcus bovis JB1 fermented glucose at a rate of 3.9 mol mg protein^-1 h^-1 and produced acctate, formate and ethanol. Based on a maximum ATP yield of 32 cells/mol ATP (Stouthamer 1973) and 3 ATP/glucose, the theoretical glucose consumption for growth would have been 2.1 mol mg protein^-1 h^-1. Because the maintenance energy requirement was 1.7 mol/mg protein/h (Russell and Baldwin 1979), virtually all of the glucose consumption could be explained by growth and maintenance and the Y_ATP was 30. Glucose-limited, continuous cultures produced heat at a rate of 0.29 mW/mg protein, and this value was similar to the enthalpy change of the fermentation (0.32 mW/mg protein). Batch cultures (specific growth rate 2.0 h^-1) fermented glucose at a rate of 81 mol mg protein^-1 h^-1, and produced only lactate. The heat production was in close agreement with the theoretical enthalpy change (1.72 versus 1.70 mW/mg protein), but only 80% of the glucose consumption could be accounted by growth and maintenance. The Y_ATP of the batch cultures was 25. Nitrogen-limited, glucose-excess, non-growing cultures fermented glucose at a rate of 6.9 mol mg protein^-1 h^-1, and virtually all of the enthalpy for this homolactic fermentation could be accounted as heat (0.17 mW/mg protein). The nitrogenlimited cultures had a membrane potential of 150 mV, and nearly all of the heat production could be explained by a futile cycle of protons through the cell membrane (watts = amperes x voltage where H⁺/ATP was 3). The membrane voltage of the nitrogen-limited cells was higher than the glucose-limited continuous cultures (150 versus 80 mV), and this difference in voltage explained why nitrogen-limited cultures consumed glucose faster than the maintenance rate. Batch cultures had a membrane potential of 100 mV, and this voltage could not account for increased glucose consumption (more than growth plus maintenance). It appears that another mechanism causes the increased heat production and lower growth efficiency of batch cultures.     

Oxidative phosphorylation in Micrococcus denitrificans

P/O ratios were measured in membrane particles obtained from cells of Micrococcus denitrificans, while growing on different carbon sources. The membrane particles obtained from cells growing actively on glucose, succinate, ethanol and propanol as the carbon and energy sources catalyzed oxidative phosphorylation and yielded respective P/O ratios of 1.4, 1.2, 0.8, and 0.5 with NADH, and 0.8, 0.6, 0.6, and 0.5 with succinate as the electron donors. Not such a difference in P/O ratio is observed in intact resting cells grown with different carbon sources. It is concluded that the influence of the carbon source is probably directed towards the efficiency of oxidative phosphorylation in membrane particles and not in the growing cells.For the aerobic carbon source-limited chemostat cultures the following maximum growth yields were determined: 40.2 and 34.2 for succinate and oxgen, 41.7 and 36.5 for malate and oxygen, 81.4 and 39.4 for mannitol and oxygen, and 77.8 and 43.4 for gluconate and oxygen respectively. With a mathematical model (de K waadsteniet et al., in press) the P/O ratio was valued at 1.4–1.7. Y _ATP at =0.2 was valued at 8.7–10.9; Y _ATP ^max at 9.6–13.2 and m _e at 0.6–4.5 for the most precise experiment (gluconate-limited). The calculation of these growth parameters has been discussed.     

Growth yield and energy generation in anaerobically-grown Campylobacter spec.

An anaerobic continuous culture study was made with Campylobacter spec. to determine growth yields under various growth conditions. The growth media contained 0.1% (w/v) yeast extract as carbon source. When grown in an aspartate-limited culture Y _asp ^max was 4.6. Inclusion of formate in the culture medium hardly affected the true growth yield. The number of ATP equivalents generated in the fumaratereductase system was 0.66 and the Y _ATP ^max was 7.0. In the nitrate reduction with formate 1.7 ATP equivalents were generated, and a YNO _3- ^max of 12.2 was observed. The true growth yield obtained with a mixture of lactate and aspartate was lower than that found with aspartate alone.     

Metabolism of Acetivibrio cellulolyticus during optimized growth on glucose,cellobiose and cellulose

Summary The growth of Acetivibrio cellulolyticus in 2.5 l batch cultures was optimized by controlling the growth pH at 6.7, the dissolved inorganic sulphide concentration at 0.4–0.6 mM, and by constant removal of hydrogen from the cultures by sparging with N₂/CO₂ or N₂ gas. An initial ethanol concentration of 0.15% (w/v) in cellobiose media resulted in specific growth rates which were reduced by about 75% compared to growth rates of 0.17 h^–1 in control cultures. Acetivibrio cellulolyticus had to be adapted for growth on glucose and ¹⁴C-radiotracer studies indicated that glucose was metabolized by the Embden-Meyerhof pathway. The specific growth rate (=0.03h^–1) and molar growth yield (Y_glucose=21.5) were considerably lower than those obtained (=0.17 h^–1, Y_cellobiose=68.9) in cellobiose media. A Y_ATP of 12.8 was obtained during growth on cellobiose. The mol product formed per mol Avicel cellulose fermented (on anhydroglucose equivalent basis) were 3.70 H₂, 2.64 CO₂, 0.73 acetate, 0.39 ethanol and 0.03 total soluble sugars on glucose basis. Maximum cellulase activity was observed in cellulose-grown cultures.National Research council of Canada No. 20826     

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.     

Hydrogen oxidation and efficiency of nitrogen fixation in succinate-limited chemostat cultures ofRhizobium ORS 571

Rhizobium ORS 571, isolated from stem nodules of the tropical legumeSesbania rostrata is able to grow in the chemostat with molecular nitrogen as sole nitrogen source at a specific growth rate of 0.1 h^-1. Samples from nitrogenfixing cultures showed high acetylene reduction activities: 1,500 nmol ethylene formed per milligram dry weight per hour. Under nitrogen-fixing conditions an uptake hydrogenase is induced. Ammonia-assimilating cultures, without additional hydrogen, did not induce hydrogenase. The addition of hydrogen to succinate-limited nitrogen-fixing cultures resulted in an increase in the molar growth yield on succinate (Y _succinate) from 27 to 35 and a slight decrease in the molar growth yield on oxygen ( ), showing that hydrogen oxidation is less energy-yielding than the oxidation of endogenous substrates. Respiration-driven proton translocation measured with starved cells indicated the functioning of site 1 and 2 of oxidative phosphorylation. Cytochrome spectra showed that cytochromea ₆₀₀, present at high dissolved oxygen tension (d.o.t.) almost completely disappeared at low d.o.t. In flash-photolysis spectra only thea-type cytochrome could be detected as an oxidase in cells both grown at high and low d.o.t. Growth yields in ammonia-assimilating cultures were higher than those measured in nitrogen-fixing cultures. Assuming two sites of oxidative phosphorylation, a molar growth yield on ATP (Y _ATP) of about 3 and 6 was calculated for respecticely nitrogen-fixing and ammonia-assimilating cultures. TheY _ATP under nitrogen-fixing conditions is dependent on the amount of H₂ formed per mol N₂ fixed (H₂/N₂ ratio). A method has been described to calculate the total amount of ATP use by nitrogenase during the fixation of 1 mol N₂ (ATP/N₂ ratio) and H₂/N₂ ratios in aerobic nitrogen fixing organisms. This calculation yielded that nitrogen fixation inRhizobium ORS 571 is a high ATP-consuming process. The calculated ATP/N₂ and H₂/N₂ ratios were respectively 42 and 7.5.Abbreviations d.o.t. dissolved oxygen tension A preliminary account of this work was presented at the 5th International Symposium on Nitrogen Fixation, September 1983, Noordwijkerhout, The Netherlands     

Cell yields of Vibrio succinogenes growing with formate and fumarate as sole carbon and energy sources in chemostat culture

Vibrio succinogenes which gains all the ATP by anaerobic electron transport phosphorylation, was grown in continuous culture on a defined medium with formate and fumarate as sole energy sources. The growth yield at infinite dilution rate (Y ^max) was obtained by extrapolation from the growth yields measured at various dilution rates. With formate as the growth limiting substrate, Y ^max was found as 14 g dry cells/mol formate. Under these conditions growth was limited by the rate of energy supply, because formate is used only as a catabolic substrate (Bronder et al. 1982). The Y _ATP ^max calculated from the ATP requirement for cell synthesis was 18 g dry cells/mol ATP. This gives an ATP/2e ratio of 0.8. The ATP/2e ratio in vitro had been measured as 1 (Kröger and Winkler 1981). It is concluded that growing V. succinogenes gain at least 80% the stoichiometrically possible amount of ATP, when growth is limited by energy supply.     

Dependency of growth yield,maintenance and K s-values on the dissolved oxygen concentration in continuous cultures of Azotobacter vinelandii

Azotobacter vinelandii was grown diazotrophically in sucrose-limited chemostat cultures at either 12, 48, 108, 144 or 192 M dissolved oxygen. Steady state protein levels and growth yield coefficients (Y) on sucrose increased with increasing dilution rate (D). Specific rate of sucrose consumption (q) increased in direct proportion to D. Maintenance coefficients (m) extrapolated from plots of q versus D, as well as from plots of 1/Y versus 1/D exhibited a nonlinear relationship to the dissolved oxygen concentration. Constant maximal theoretical growth yield coefficients (Y ^G) of 77.7 g cells per mol of sucrose consumed were extrapolated irrespective of differences in ambient oxygen concentration. For comparison, glucose-, as well as acetate-limited cultures were grown at 108 M oxygen. Fairly identical m- and Y ^G-values, when based on mol of substrate-carbon with glucose and sucrose grown cells, indicated that both substrates were used with the same efficiency. However, acetate-limited cultures showed significantly lower m- and, at comparable, D, higher Y-values than cultures limited by either sucrose or glucose. Substrate concentrations (K _s) required for half-maximal growth rates on sucrose were not constant, they increased when the ambient oxygen concentration was raised and, at a given oxygen concentration, when D was decreased. Since biomass levels varied in linear proportion to K _s these results are interpreted in terms of variable substrate uptake activity of the culture.Abbreviations D dilution rate - K _s substrate concentration required for half maximal growth rate - m maintenance coefficient - q specific rate of substrate consumption - Y growth yield coefficient - Y ^G maximum theoretical growth yield coefficient     

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     

The influence of different carbon sources and medium osmolarity on the potassium requirements of Candida utilis NCYC 321, growing in continuous culture

In order to study the influence of different carbon sources on the K⁺-requirements of Candida utilis NCYC 321, this yeast was grown at several different dilution rates in potassium-limited continuous cultures with either glucose, glycerol, ethanol, citrate or lactate serving as the carbon and energy source.It was found that the nature of the carbon source profoundly influenced the cellular potassium content, especially at low dilution rates, but that these differences could not be correlated with any differences in relative growth rate (i.e., / _max. And although small amounts of potassium seemingly were needed to serve in osmoregulation and in the cotransport of some acidic carbon sources (lactate and citrate), these requirements were negligible.Independent of carbon source, a strong correlation existed between the intracellular potassium concentration and the yield value on oxygen (Y _O), and between cellular potassium concentration and growth rate. From these two correlations it was concluded that potassium probably was involved mainly in processes associated with ATP synthesis in this yeast.Finally the effect of the addition of NaCl to the medium was tested with glucose-containing cultures that were either carbon- or potassium-limited. Up to a concentration of 20 g/l, NaCl was without influence on Y _O, Y _glucose and q _{O 2}, but effected a slight increase in the cellular potassium content of the potassium-limited cells and a decrease in that of the glucose-limited cells.     

Energy conservation during nitrate respiration in Paracoccus denitrificans

P/2e ratios were calculated from anaerobic chemostat cultures of Paracoccus denitrificans with nitrogenous oxides as electron acceptor. P/2e ratios were calculated, using the Y _ATP ^max values determined for aerobic cultures. When succinate was the carbon and energy source the average P/2e values of the sulphate-and succinate-limited cultures with nitrate as electron acceptor were 0.5 and 0.7, respectively, and of the nitrite-limited culture 0.9. With gluconate as carbon and energy source the average P/2e values of the gluconate-limited with nitrate as electron acceptor and nitrate limited cultures were 0.9 and 1.1, respectively.H⁺/O ratios measured in cells obtained from sulphate-, succinate, nitrite-, gluconate-and nitratelimited cultures yielded respective average values of 3.4, 4.5, 3.5, 4.8 and 6.2 for endogenous substrates. From our data we conclude that sulphate-and nitritelimitation causes the loss of site I phosphorylation. Nitrite has no influence on the maximum growth yield on ATP. We propose that metabolism in heterotrophically grown cells of Paracoccus dentrificans is regulated on the level of phosphorylation in the site I region of the electron transport chain.