Acetate formation from CO and CO2 by cell extracts of Peptostreptococcus productus (strain Marburg)

Cell extracts of Peptostreptococcus productus (strain Marburg) obtained from CO grown cells mediated the synthesis of acetate from CO plus CO₂ at rates of 50 nmol/min × mg of cell protein. ¹⁴CO was specifically incorporated into C₁ of acetate. No label exchange occurred between ¹⁴C₁ of acetyl-CoA and CO, indicating that ¹⁴CO incorporation into acetate was by net synthesis rather than by an exchange reaction. In acetate synthesis from CO plus CO₂ the latter substrate could be replaced to some extent by formate or methyl tetrahydrofolate as the methyl donor. The methyl group of methyl cobalamin was incorporated into acetate ony at very low activities. The cell extracts contained high levels of enzyme activities involved in acetate or cell carbon synthesis from CO₂. The following enzymic activities were detected: CO: methyl viologen oxidoreductase, formate dehydrogenase, formyl tetrahydrofolate synthetase, methenyl tetrahydrofolate cyclohydrolase, methylene tetrahydrofolate dehydrogenase, methylene tetrahydrofolate reductase, phosphate acetyltransferase, acetate kinase, hydrogenase, NADPH: benzyl viologen oxidoreductase, and pyruvate synthase. Some kinetic and other properties were studied.     

Growth yield increase linked to caffeate reduction in Acetobacterium woodii

Growth yields were determined with Acetobacterium woodii strain NZva 16 on hydrogen and CO₂, formate, methanol, vanillate, ferulate and fructose in mineral medium in the absence and presence of 0.05% yeast extract. Yeast extract was not essential for growth but enhanced growth yields by 25–100% depending on the substrate fermented. Comparison of yields on formate or methanol allowed calculation of an energy yield in the range of 1.5–2 mol ATP per mol acetate formed during homoacetate fermentation of A. woodii. In the presence of 6 mM caffeate, growth yields were determined with the substrates formate or methanol. Caffeate was reduced to hydrocaffeate and increased growth yields were obtained. An ATP yield of about 1 mol per mol of caffeate reduced was calculated. Cytochromes were not detectable in cell free extracts or membrane preparations.     

Sporomusa termitida sp. nov., an H2/CO2-utilizing acetogen isolated from termites

H₂-oxidizing CO₂-reducing acetogenic bacteria were isolated from gut contents of Nasutitermes nigriceps termites. Isolates were strictly anaerobic, Gram negative, endospore-forming, straight to slightly curved rods (0.5–0.8×2–8 m) that were motile by means of lateral flagella. Cells were oxidase negative, but catalase positive and possessed a b-type cytochrome(s) associated with the cell membrane. Cells grew anaerobically with H₂+CO₂ as energy source and catalyzed a total synthesis of acetate from this gas mixture. H₂ uptake by a representative isolate (strain JSN-2) displayed a K _m=6 M and V _max=380 nmol x min^-1 x mg protein^-1. Other substrates used as energy sources for growth and acetogenesis included CO, methanol, betaine, trimethoxybenzoate, and various other organic acids. Succinate was also fermented, but propionate was formed from this substrate instead of acetate. Of a variety of sugars and sugar alcohols tested, only mannitol supported growth. Cells grew optimally at 30° C and pH 7.2 and required yeast extract or a source of amino acids (e.g. Casamino acids) for good growth. During initial enrichment and isolation, cells appeared sensitive to various reducing agents commonly employed in media for anaerobes. The DNA base composition of strain JSN-2 was 48.6 mol% G+C. On the bases of cell morphology, substrate utilization spectrum, and DNA base composition, strain JSN-2 is here-with proposed as the type strain of the new species Sporomusa termitida.Journal article no. 12513 from the Michigan Agricultural Experiment Station     

Characterization of the impact of acetate and lactate on ethanolic fermentation by Thermoanaerobacter ethanolicus

Ethanolic fermentation of simple sugars is an important step in the production of bioethanol as a renewable fuel. Significant levels of organic acids, which are generally considered inhibitory to microbial metabolism, could be accumulated during ethanolic fermentation, either as a fermentation product or as a by-product generated from pre-treatment steps. To study the impact of elevated concentrations of organic acids on ethanol production, varying levels of exogenous acetate or lactate were added into cultures of Thermoanaerobacter ethanolicus strain 39E with glucose, xylose or cellobiose as the sole fermentation substrate. Our results found that lactate was in general inhibitory to ethanolic fermentation by strain 39E. However, the addition of acetate showed an unexpected stimulatory effect on ethanolic fermentation of sugars by strain 39E, enhancing ethanol production by up to 394%. Similar stimulatory effects of acetate were also evident in two other ethanologens tested, T. ethanolicus X514, and Clostridium thermocellum ATCC 27405, suggesting the potentially broad occurrence of acetate stimulation of ethanolic fermentation. Analysis of fermentation end product profiles further indicated that the uptake of exogenous acetate as a carbon source might contribute to the improved ethanol yield when 0.1% (w/v) yeast extract was added as a nutrient supplement. In contrast, when yeast extract was omitted, increases in sugar utilization appeared to be the likely cause of higher ethanol yields, suggesting that the characteristics of acetate stimulation were growth condition-dependent. Further understanding of the physiological and metabolic basis of the acetate stimulation effect is warranted for its potential application in improving bioethanol fermentation processes.     

Isolation and characterization of a carbon monoxide utilizing strain of the acetogen Peptostreptococcus productus

From sludge obtained from the sewage digester plant in Marburg-Cappel a strictly anaerobic bacterium was enriched and isolated with carbon monoxide as the sole energy source. Based on morphological and physiological characteristics the isolate was identified as a strain of Peptostreptococcus productus, which was called strain Marburg. The organism was able to grow on CO (50% at 200 kPa) as the sole energy source at a doubling time of 3 h and converted this substrate to acetate and CO₂. The type strain of P. productus was not able to grow at the expense of CO. Electron microscopic investigations of strain Marburg cells revealed a cell wall which was different from that of other Gram-positive prokaryotes. DNA:DNA hybridization studies of the DNA isolated from strain Marburg and the type strain as well as some morphological and physiological properties of both strains confirmed the low degree or relatedness between the two strains.     

Extended culture: The growth of Candida utilis at controlled acetate concentrations

Extended culture, a special type of semicontinuous culture, permits prolonged maintenance of a constant or programmed environment in a growing culture by a controlled addition of one or more substrates. Differences between extended culture and continuous culture data are a measure of differences in the properties of cell populations with different cell age distributions but identical steady-state environments. Both extended culture and continuous culture were used to study the growth kinetics of Candida utilis (ATCC 9226) under conditions of substrate inhibition at controlled concentrations of sodium acetate in a carbon-limited mineral salts medium supplemented with 0.01 g/1 yeast extract. Acetate concentrations ranged from 1.2 g/l to 10.8 g/l (expressed as acetic acid), while yeast concentrations varied from 0.3 to 7.8 (g dry cells)/1. Rate parameters such as growth yields (Y), specific growth rates (μ), and linear growth rates (K), were calculated by computer from the data and theory presented herein. Specific growth rates as high as 0.54/hr were observed, although extended culture growth was more nearly linear than exponential in these experiments. Growth yields usually varied between 0.2 and 0.4 (g dry cells)/(g acetate), although values were as high as 0.8 for a brief period during one experiment. Growth yields at a given acetate concentration were correlated by an equation of the form 1/Y = 1/Y_G + m/μ. A maintenance coefficient (m) of 0.17 (g acetate)/(g dry cell-hr) was observed at acetate concentrations of 4.5 and 10. g/1. A typical maximum growth yield (Y_G) of 0.51 (g dry cell)/(g acetate) was obtained at 4.5 g/1 acetate, but an unusually high Y_G of 1.33 was found at 10. g/1 acetate. Oxygen uptake measurements are compared with these cell yield measurements. Linear growth rates in expended culture were correlated by the equation K = 0.89–0.70 (S/S₀) where K has units of (g dry cell)/(l-hr), S is the instantaneous acetate concentration, and S₀ is the initial acetate concentration. The extended culture kinetic data are shown to be substantially different from continuous culture kinetic data. Reason for these differences are discussed in light of diffrences in the cell age distributions, as well as possible differences in experimental conditions.     

Metabolism of H2-CO2, methanol, and glucose by Butyribacterium methylotrophicum.

The fermentative metabolism of Butyribacterium methylotrophicum grown on either H2-CO2, methanol, glucose, or CO is described. The following reaction stoichiometries were obtained: 1.00 H2 + 0.52 CO2 leads to 0.22 acetate + 0.06 cell C; 1 methanol + 0.18 CO2 + 0.01 acetate leads to 0.24 butyrate + 0.29 cell C; and 1.00 glucose leads to 0.31 CO2 + 1.59 acetate + 0.21 butyrate + 0.13 H2 + 1.58 cell C. Cell yields of 1.7 g (dry weight) per mol of H2, 8.2 g (dry weight) per mol of methanol, 42.7 g (dry weight) per mol of glucose, and 3.0 g (dry weight) per mol of CO were obtained from linear plots of cell synthesis and substrate consumption. Doubling times of 9.0, 9.0, and 3 to 4 h were observed during batch growth on H2-CO2, methanol, and glucose, respectively. Indicative of a growth factor limitation, glucose fermentation in defined medium displayed a lower cell synthesis efficiency than when yeast extract (0.05%) was present. B. methylotrophicum fermentation displayed atypically high substrate/cell carbon synthesis conversion ratios for an anaerobe, as greater than 24% of the carbon was assimilated into cells during growth on methanol or glucose. The data indicate that B. methylotrophicum conserves carbon-bound electrons during growth on single-carbon or multicarbon substrates.     

Purification and characterization of ferredoxin from Peptostreptococcus productus (strain Marburg)

Ferredoxin was purified to apparent homogeneity from cell extracts of the homoacetogen Peptostreptococcus productus (strain Marburg). The yield was 70 g ferredoxin per g wet cells of P. productus. The UV-vis spectrum exhibited characteristics of a typical clostridial ferredoxin spectrum with a molar extinction coefficient ₃₈₅ of 30000 M^-1 cm^-1 and an A₃₈₅/A₂₈₀ ratio of 0.76. The molecular weight M_r was near 5700 as calculated from the amino acid composition. The protein contained per mol 9.9 mol iron, 8.2 mol acid-labile sulfide, and near 7 mol cysteine indicating the presence of two 4 Fe/4 S clusters. The redox potential was determined to be-410 mV. The purified ferredoxin was reduced with carbon monoxide by the carbon monoxide dehydrogenase from crude extracts and by the partially enriched enzyme of P. productus.     

Bioconversion of synthesis gas to hydrogen using a light-dependent photosynthetic bacterium,Rhodospirillum rubrum

Biological hydrogen production from synthesis gas was carried out in batch culture. The phototrophic anaerobic bacterium, Rhodospirillum rubrum was used to oxidize CO and water to CO₂ and hydrogen. The bacteria were grown under anaerobic conditions in liquid medium; also acetate was used as carbon source in presence of synthesis gas. Biological hydrogen production was catalysed by R. rubrum via the water–gas shift reaction. A light-dependent cell growth modelled with a desired rate of hydrogen production and CO uptake was determined. The effect of light intensity on microbial cell growth was also studied at 500, 1,000 and 1,500 m.cd. A complete conversion of CO to hydrogen and maximum light efficiency were obtained with an acetate concentration of 1 g/l and light intensity of 500 m.cd. Utilization of the carbon monoxide from the gas phase was often considered as a mass transfer limited process, which needed to diffuse through the gas–liquid interface and then further diffuse into liquid medium prior to reaction. The results from this study showed that maximum cell propagation and hydrogen production were achieved with a limited light intensity of 1,000 m.cd. It was also found that high-light intensity may interfere with cell metabolism. In low-light intensity and substrate concentration, no inhibition was observed, however at extreme conditions, non-competitive inhibition was identified. The adverse effect of high-light intensity was shown at 5,000 m.cd, where the CO conversion drastically dropped to as low as 21%. Maximum CO conversion of 98% and maximum yield of 86% with an acetate concentration of 1.5 g/l and a light intensity of 1,000 m.cd were achieved.     

Elevated atmospheric CO2 increases microbial growth rates in soil: results of three CO2 enrichment experiments

Increasing the belowground translocation of assimilated carbon by plants grown under elevated CO₂ can cause a shift in the structure and activity of the microbial community responsible for the turnover of organic matter in soil. We investigated the long‐term effect of elevated CO₂ in the atmosphere on microbial biomass and specific growth rates in root‐free and rhizosphere soil. The experiments were conducted under two free air carbon dioxide enrichment (FACE) systems: in Hohenheim and Braunschweig, as well as in the intensively managed forest mesocosm of the Biosphere 2 Laboratory (B2L) in Oracle, AZ. Specific microbial growth rates (μ) were determined using the substrate‐induced respiration response after glucose and/or yeast extract addition to the soil. For B2L and both FACE systems, up to 58% higher μ were observed under elevated vs. ambient CO₂, depending on site, plant species and N fertilization. The μ‐values increased linearly with atmospheric CO₂ concentration at all three sites. The effect of elevated CO₂ on rhizosphere microorganisms was plant dependent and increased for: Brassica napus=Triticum aestivum<Beta vulgaris<Populus deltoides. N deficiency affected microbial growth rates directly (N limitation) and indirectly (changing the quantity of fine roots). So, 50% decrease in N fertilization caused the overall increase or decrease of microbial growth rates depending on plant species. The μ‐value increase was lower for microorganisms growing on yeast extract then for those growing on glucose, i.e. the effect of elevated CO₂ was smoothed on rich vs. simple substrate. So, the r/K strategies ratio can be better revealed by studying growth on simple (glucose) than on rich substrate mixtures (yeast extract). Our results clearly showed that the functional characteristics of the soil microbial community (i.e. specific growth rates) rather than total microbial biomass amount are sensitive to increased atmospheric CO₂. We conclude that the more abundant available organics released by roots at elevated CO₂ altered the ecological strategy of the soil microbial community specifically a shift to a higher contribution of fast‐growing r‐selected species was observed. These changes in functional structure of the soil microbial community may counterbalance higher C input into the soil under elevated atmospheric CO₂ concentration.     

Capacity of chromatiaceae for chemotrophic growth. Specific respiration rates of Thiocystis violacea and Chromatium vinosum

The capacity for chemoautotrophic, mixotrophic and organotrophic growth in the dark was tested with 45 strains of 17 species (11 genera) of the Chromatiaceae. The auxanographic deep agar shake culture method was used; the gas phase contained 5% O₂ and 1% CO₂ in N₂. All strains tested of Chromatium vinosum, C. minus, C. violascens, C. gracile, Thiocystis violacea, Amoebobacter roseus, Thiocapsa roseopersicina gave positive growth responses under chemoautotrophic and mixotrophic conditions (extra carbon source acetate); one strain of Thiocapsa roseopersicina grew also organotrophically on acetate alone. No growth was obtained with the remaining 17 strains of ten species. None of the five type species (three genera) of the Chlorobiaceae grew under chemotrophic conditions. With Thiocystis violacea 2311 a growth yield of 11.3g dry weight per mol thiosulfate consumed was obtained under chemoautotrophic conditions; under mixotrophic conditions with acetate the yield increased to 69g dry weight per mol thiosulfate consumed. With Thiocystis violacea 2311 maximal specific respiration rates were obtained with thiosulfate as electron donor irrespective of the presence or absence of sulfur globules in the cells; organic substrates served as carbon sources only and did not support respiration. With Chromatium vinosum D utilization of thiosulfate was not constitutive; maximal respiration rates on thiosulfate were obtained only with thiosulfate grown cells containing sulfur globules. Respiration rates were further increased by malate, fumarate or propionate; these substrates also served as sole electron donors for respiration. Acetate and pyruvate were used as carbon sources only. The ecological significance of the chemotrophic metabolism is discussed.     

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     

Ethanol production from xylose by Thermoanaerobacter ethanolicus in batch and continuous culture

The fermentation of xylose by Thermoanaerobacter ethanolicus ATCC 31938 was studied in pH-controlled batch and continuous cultures. In batch culture, a dependency of growth rate, product yield, and product distribution upon xylose concentration was observed. With 27 mM xylose media, an ethanol yield of 1.3 mol ethanol/mol xylose (78% of maximum theoretical yield) was typically obtained. With the same media, xylose-limited growth in continuous culture could be achieved with a volumetric productivity of 0.50 g ethanol/liter h and a yield of 0.42 g ethanol/g xylose (1.37 mol ethanol/mol xylose). With extended operation of the chemostat, variation in xylose uptake and a decline in ethanol yield was seen. Instability with respect to fermentation performance was attributed to a selection for mutant populations with different metabolic characteristics. Ethanol production in these T. ethanolicus systems was compared with xylose-to-ethanol conversions of other organisms. Relative to the other systems, T. ethanolicus offers the advantages of a high ethanol yield at low xylose concentrations in batch culture and of a rapid growth rate. Its disadvantages include a lower ethanol yield at higher xylose concentrations in batch culture and an instability of fermentation characteristics in continuous culture.     

Anaerobic acetate oxidation to CO2 by Desulfotomaculum acetoxidans

Desulfotomaculum acetoxidans oxidizes acetate to CO₂ with sulfate. This organism metabolizes acetate via a pathway in which C₁ units rather than tri- and dicarboxylic acids are intermediates. We report here that cell extracts of D. acetoxidans catalyzed an exchange between CO₂ and the carboxyl group of acetate at a rate of 90 nmol · min^-1 · mg^-1 protein which is sufficient to account for the in vivo acetate oxidation rate of 250 nmol · min^-1 · mg^-1 protein. The reaction was strictly dependent on both ATP and coenzyme A. The extracts contain high activities of acetate kinase (6.3 U · mg^-1 protein) and phosphotransacetylase (60 U · mg^-1 protein). These findings indicate that acetyl-CoA rather than acetyl-phosphate or acetate is the substrate of the carbon-carbon cleavage activity. Exchange was only observed in the presence of strong reducing agents such as Ti³⁺. Interestingly, the cell extracts also catalyzed the reduction of CO₂ to CO with Ti³⁺ as electron donor (120 nmol · min^-1 · mg^-1 protein). Carbon monoxide dehydrogenase and other oxidoreductases involved in acetate oxidation were found to be partially associated with the membrane fraction suggesting a membrane localization of these enzymes.Abbreviations MOPS Morpholinopropane sulfonic acid - Tricine N-tris(hydroxymethyl)-methylglycine - DTT d,l-1,4-Dithiothreitol - DMN 2,3-Dimethyl-1,4-naphthoquinone - MV_OX Methyl viologen, oxidized - APS Adenosinephosphosulfate - SRB Sulfate reducing bacteria - U mol product formed per min     

Determination of the maximum product yield from glucoamylase-producing Aspergillus niger grown in the recycling fermentor

Aspergillus niger has been grown in glucose- and maltose-limited recycling cultures to determine the maximum growth yield, the maximum product yield for glucoamylase production, and the maintenance requirements at very slow specific growth rates. Using the linear equation for substrate utilization, and using the experimental data from both recycling experiments, both the maximum growth yield, Y_xsm, and the maximum product yield, Y_psm, could be determined. The values estimated were 157 g biomass per mol maltose for Y_xsm and 100 g protein per mol maltose for Y_psm. Expressed on a C₁-basis these values are 0.52 and 0.36 C-mole per C-mol for respectively Y_xsm and Y_psm. The found value for Y_psm is half the value found for alkaline serine protease production in Bacillus lichoniformis, and it can be concluded that formation of extracellular protein is more energy consuming in filamentous fungi than in prokaryotic organisms. Maintenance requirements are no significant factor during growth of Aspergillus niger, and reported maintenance requirements are most probably due to differentiation.     

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     

Glucose fermentation to acetate,CO2 and H2 in the anaerobic hyperthermophilic eubacterium Thermotoga maritima: involvement of the Embden-Meyerhof pathway

The hyperthermophilic anaerobic eubacterium Thermotoga maritima was grown on glucose as carbon and energy source. During growth 1 mol glucose was fermented to 2 mol acetate, 2 mol CO₂ and 4 mol H₂. The molar growth yicld on glucose (Y_glucose) was about 45 g cell dry mass/mol glucose. In the presence of elemental sulfur growing cultures of T. maritima converted 1 mol glucose to 2 mol acetate, 2 mol CO₂ about 0.5 mol H₂ and about 3.5 mol H₂S. Y_glucose was about 45 g/mol. Cell extracts contained all enzymes of the Embden-Meyerhof pathway: hexokinase (0.29 U/mg, 50°C), glucose-6-phosphate isomerase (0.56 U/mg, 50°C), phosphofructokinase (0.19 U/mg, 50° C), fructose-1,6-bisphosphate aldolase (0.033 U/mg, 50°C), triosephosphate isomerase (6.3 U/mg, 50°C), glyceraldehyde-3-phosphate dehydrogenase (NAD⁺ reducing: 0.63 U/mg, 50°C), phosphoglycerate kinase (3.7 U/mg, 50°C), phosphoglycerate mutase (0.4 U/mg, 50°C); enolase (4 U/mg, 80°C), pyruvate kinase (0.05 U/mg, 50°C). Furthermore, cell extracts contained pyruvate: ferredoxin oxidoreductasee (0.43 U/mg, 60°C); NADH: ferredoxin oxidoreductase (benzylviologen reduction: 0.46 U/mg, 80°C); hydrogenase (benzylviologen reduction: 15 U/mg, 80°C), phosphate acetyltransferase (0.13 U/mg, 80°C), acetate kinase (1.2 U/mg, 55°C), lactate dehydrogenase (0.16 U/mg, 80°C) and pyruvate carboxylase (0.02 U/mg, 50°C). The findings indicate that the hyperthermophilic eubacterium T. maritima ferments sugars (glucose) to acetate, CO₂ and H₂ involving the Embden-Meyerhof pathway, phosphate acetyltransferase and acetate kinase. Thus, the organism differs from the hyperthermophilic archaeon Pyrococcus furiosus which ferments sugars to acetate, CO₂ and H₂ involving a modified non-phosphorylated Entner-Doudoroff pathway and acetyl-CoA synthetase (ADP forming).     

Growth and butyric acid production by Clostridium populeti

The growth of Clostridium populeti in 2% (w/v) glucose medium containing 0.2% (w/v) yeast extract was optimal with 10 mM NH₄Cl as the nitrogen source. Although the maximum specific growth rate (=0.32 h^-1) with 5 mM NH₄Cl was similar, the biomass yield was about 30% lower than that at the optimum. Either sodium sulphide or cysteine-HCl at an optimum concentration of 0.33 mM and 5.0 mM respectively, could serve as the sole sulphur source for growth. The growth rate was unaffected by initial glucose concentrations of up to 10% (w/v), but in the presence of 15% glucose it declined by about 35%. The molar yield of butyric acid (mol/mol glucose) declined from 0.70 in 1% (w/v) initial glucose medium to 0.39 in 10% glucose medium. In 5.7% initial glucose medium, butyric acid levels of 6.3 g/l were obtained (0.56 mol butyrate/mol glucose) after 72 h of incubation in 2.5 l batch cultures. A decrease of about 50% in the maximum specific growth rate of C. populeti was observed in the presence of an initial concentration of either 1.2 g/l of butyric acid or 18.9 g/l of acetic acid.This paper is issued as NRCC No. 29032     

Aerobic denitrification: a controversy revived

During studies on the denitrifying mixotroph, Thiosphaera pantotropha, it has been found that this organism is capable of simultaneously utilizing nitrate and oxygen as terminal electron acceptors in respiration. This phenomenon, termed aerobic denitrification, has been found in cultures maintained at dissolved oxygen concentrations up to 90% of air saturation.The evidence for aerobic denitrification was obtained from a number of independant experiments. Denitrifying enzymes were present even in organisms growing aerobically without nitrate. Aerobic yields on acetate were higher (8.1 g protein/mol) without than with (6.0 g protein/mol) nitrate, while the anaerobic yield with nitrate was even lower (4 g protein/mol). The maximum specific growth rate of Tsa. pantotropha was higher (0.34 h^-1) in the presence of both oxygen (>80% air saturation) and nitrate than in similar cultures not supplied with nitrate (0.27 h^-1), indicating that the rate of electron transport to oxygen was limiting. This was confirmed by oxygen uptake experiments which showed that although the rate of respiration on acetate was not affected by nitrate, the total oxygen uptake was reduced in its presence. The original oxygen uptake could be restored by the addition of denitrification inhibitors.Dedicated to Professor Dr. H.-G. Schlegel on the occasion of his 60th birthday     

Propionate acts as carboxylic group acceptor in aspartate fermentation by Propionibacterium freudenreichii

Cells of Propionibacterium freudenreichii ssp. shermanii and ssp. freudenreichii did not show significant growth or product formation in a mineral medium with 10 mM aspartate or 10 mM fumarate, vitamins, and a small amount (0.05% w/v) of yeast extract. In the presence of added propionate, growth with aspartate or fumarate was possible, and depended strictly on the amount of propionate provided, according to the equation: 3 aspartate + propionate 3 succinate + acetate + CO₂+3 NH₃. Cocultures of P. freudenreichii with the succinate-decarboxylating strain Ft2 converted 3 aspartate stoichiometrically to acetate and 2 propionate. High activity of methylmalonyl-CoA: pyruvate transcarboxylase, and lack of methylmalonyl-CoA decarboxylase and oxaloacetate decarboxylase activity in cell-free extracts of aspartate-grown cells indicated that failure to use aspartate as sole substrate was due to the inability of these strains to catalyze a net decarboxylation of C₄-dicarboxylic acids.Dedicated to Prof. Dr. Norbert Pfennig on occasion of his 65th birthday