Pyruvate — a novel substrate for growth and methane formation in Methanosarcina barkeri

Methanosarcina barkeri strain Fusaro was found to grow on pyruvate as sole carbon and energy source after an incubation period of 10–12 weeks in the presence of high pyruvate concentrations (100 mM). Growth studies, cell suspension experiments and enzymatic investigations were performed with pyruvate-utilizing M. barkeri. For comparison acetate-adapted cells of M. barkeri were analyzed.

1. Pyruvate-utilizing M. barkeri grew on pyruvate (100 mM) with an initial doubling time of about 25 h (37 °C, pH 6.5) up to cell densities of about 0.8 g cell dry weight/l. The specific growth rate was linearily dependent on the pyruvate concentration up to 100 mM indicating that pyruvate was taken up by passive diffusion. Only CO₂ and CH₄ were detected as fermentation products. As calculated from fermentation balances pyruvate was converted to CH₄ and CO₂ according to following equation: Pyruvate^-+H⁺+0.5 H₂O » 1.25 CH₄+1.75 CO₂. The molar growth yield (Ych ₄) was about 14 g dry weight cells/mol CH₄. In contrast the growth yield (Ych ₄) of M. barkeri during growth on acctate (Acetate^-+H⁺ » CH₄+CO₂) was about 3 g/mol CH₄.
2. Cell suspensions of pyruvate-grown M. barkeri catalyzed the conversion of pyruvate to CH₄, CO₂ and H₂ (5–15 nmol pyruvate consumed/min x mg protein). At low cell concentrations (0.5 mg protein/ml) 1 mol pyruvate was converted to 1 mol CH₄, 2 mol CO₂ and 1 mol H₂. At higher cell concentration less H₂ and CO₂ and more CH₄ were formed due to CH₄ formation from H₂/CO₂. The rate of pyruvate conversion was linearily dependent on the pyruvate concentration up to about 30 mM. Cell suspensions of acetate-grown M. barkeri also catalyzed the conversion of 1 mol pyruvate to 1 mol CH₄, 2 mol CO₂ and 1 mol H₂ at similar rates and with similar affinity for pyruvate as pyruvate-grown cells.
3. Cell extracts of both pyruvate-grown and acetate-grown M. barkeri contained pyruvate: ferredoxin oxidoreductase. The specific activity in pyruvate-grown cells (0.8 U/mg) was 8-fold higher than in acetate-grown cells (0.1 U/mg). Coenzyme F₄₂₀ was excluded as primary electron acceptor of pyruvate oxidoreductase. Cell extracts of pyruvate-grown M. barkeri contained carbon monoxide dehydrogenase activity and hydrogenase activity catalyzing the reduction by carbon monoxide and hydrogen of both methylviologen and ferredoxin (from Clostridium).

This is the first report on growth of a methanogen on pyruvate as sole carbon and energy source, i.e. on a substrate more complex than acetate.     

Evidence for two functionally distinct hydrogenases in Anacystis nidulans

The effect of growth conditions on aerobic and anaerobic hydrogenase activities of Anacystis nidulans was studied. It was found that the two hydrogenase activities both of which were confined to the particulate fraction of cell-free extracts correlated in an opposite way with growth temperature: The algae were always grown photoautotrophically in presence of H₂ but after growth at 25° C a significant oxyhydrogen reaction contrasted with negligible photoreduction rates while the opposite was true after growth at 40°C. A similar correlation between incubation temperature and induction of the respective hydrogenase activity was also observed with resting cells.Kinetic analysis of the two different types of hydrogenase — catalysed reactions with Anacystis membranes yielded the following Michaelis-Mentenparameters: K _M=55 M H₂ and v _max=0.12 mol H₂ per min and mg protein for the oxyhydrogen reaction, and K _M=170 M H₂ and v _max=0.3 mol H₂ per min and mg protein for the photoreductions. Also the dependences of oxyhydrogen and of photoreduction activities on pH and on temperature were measured; both pH and temperature profiles were found to be markedly different for each type of H₂-supported reaction.The results are discussed as pointing to the possible occurrence of two functionally distinct hydrogenase enzymes which can be synthesized by Anacystis in response to the conditions of induction.Abbreviations BO p-benzoquinone - CAP chloramphenicol - chl chlorophyll - cytc horse heart cytochrome c - DCMU 3-(34-dichlorophenyl)-1,1-dimethylurea - DCPIP 2,6-dichlorophenolindophenol - fd ferredoxin - FeCy ferricyanide - MB methylene blue - MV methyl viologen - HEPES N-2-hydroxyethylpiperazine-N-2-ethanesulfonic acid - MES 2-(N-morpholino)-ethanesulfonic acid - PIPES piperazine-N,N-bis-(2-ethanesulfonic acid) - tricine N-tris-(hydroxymethyl)-methylglycine - Tris tris-(hydroxymethyl)-aminomethan     

One carbon metabolism in methanogenic bacteria

Two strains of Methanosarcina (M. Barkeri strain MS, isolated from sewage sludge, and strain UBS, isolated from lake sediments) were found to have similar cellular properties and to have DNA base compositions of 44 mol percent guanosine plus cytosine. Strain MS was selected for further studies of its one-carbon metabolism. M. barkeri grew autotrophically via H₂ oxidation/CO₂ reduction. The optimum temperature for growth and methanogenesis was 37°C. H₂ oxidation proceeded via an F₄₂₀-dependent NADP⁺-linked hydrogenase. A maximum specific activity of hydrogenase in cell-free extracts, using methyl viologen as electron acceptor, was 6.0 mol min · mg protein at 37°C and the optimum pH (9.0). M. barkeri also fermented methanol andmethylamine as sole energy sources for growth. Cell yields during growth on H₂/CO₂ and on methanol were 6.4 and 7.2 mg cell dry weight per mmol CH₄ formed, respectively. During mixotrophic growth on H₂/CO₂ plus methanol, most methane was derived from methanol rather than from CO₂. Similar activities of hydrogenase were observed in cell-free extracts from H₂/CO₂-grown and methanol-grown cells. Methanol oxidation apparently proceeded via carrierbound intermediates, as no methylotrophy-type of methanol dehydrogenase activity was observed in cell-free extracts. During growth on methanol/CO₂, up to 48% of the cell carbon was derived from methanol indicating that equivalent amounts of cell carbon were derived from CO₂ and from an organic intermediate more reduced than CO₂. Cell-free extracts lacked activity for key cell carbon synthesis enzymes of the Calvin cycle, serine path, or hexulose path.Abbreviations CAPS cycloaminopropane sulfonic acid - CH₃-SCoM methyl coenzyme M - DCPIP 2,6-dichlorophenolindophenol - DEAE diethylaminoethyl - dimethyl POPOP 1,4-bis-2-(4-mothyl-5-phenyloxazolyl)-benzene - DNA deoxyribonucleic acid - dpm dismtegrations per min - DTT dithiothreitol - EDTA ethylenediamine tetraacetic acid - F₄₂₀ factor 420 - G+C guanosine plus cytosine - NAD⁺ nicotinamide adenine dinucleotide - NADP⁺ nicotinamide adenine dinucleotide phosphate - PBBW phosphate buffered basal Weimer - PMS phenazine methosulfate - PPO 2,5-diphenyloxazole - rRNA ribosomal ribonucleic acid - RuBP ribulose-1,5-bisphosphate - Tris tris-hydroxymethyl-aminomethane - max maximum specific growth rate     

Growth yields of Desulfotomaculum orientis with hydrogen in chemostat culture

Desulfotomaculum orientis (strain Singapore 1) was grown autotrophically with H₂+CO₂ and sulfate, thiosulfate or sulfite as electron acceptor in sulfide- and pH-controlled continuous culture. Under sulfate-limiting conditions real growth yields of up to 9.7 g cell dry mass per mol sulfate were obtained. Electron acceptor limitation resulted in the excretion of up to 14.5 mmol acetate per liter, formed by reduction of CO₂ with H₂. Acetate production was not coupled to an increase of growth yields: under hydrogen-limiting conditions only 1.6 mmol acetate per liter was produced, and even higher growth yields of up to 12,4 g cell dry mass per mol sulfate were obtained. With thiosulfate or sulfite as electron acceptor growth yields increased up to 17.9 g cell dry mass per mol electron acceptor. Growth yields were not simply correlated with the growth rate, and did not allow the determination of maintenance coefficients and the extrapolation to maximal yields at infinite growth rate (Y ^max). The maximal growth rates (_max) with sulfate and thiosulfate were 0.090 and 0.109 h^-1, respectively, if cells were grown continuously in sulfidostat culture under nonlimiting conditions.The net energy yield of sulfate reduction and the energy requirement for the activation of sulfate by Desulfotomaculum orientis are discussed.     

N 5-Methyltetrahydromethanopterin: coenzyme M methyltransferase in methanogenic archaebacteria is a membrane protein

An assay is described that allows the direct measurement of the enzyme activity catalyzing the transfer of the methyl group from N ⁵-methyltetrahydromethanopterin (CH₃–H₄MPT) to coenzyme M (H–S–CoM) in methanogenic archaebacteria. With this method the topology, the partial purification, and the catalytic properties of the methyltransferase in methanol- and acetate-grown Methanosarcina barkeri and in H₂/CO₂-grown Methanobacterium thermoautotrophicum were studied. The enzyme activity was found to be associated almost completely with the membrane fraction and to require detergents for solubilization. The transferase activity in methanol-grown M. barkeri was studied in detail. The membrane fraction exhibited a specific activity of CH₃–S–CoM formation from CH₃–H₄MPT (apparent K _m=50 M) and H–S–CoM (apparent K _m=250 M) of approximately 0.6 mol·min^-1·mg protein^-1. For activity the presence of Ti(III) citrate (apparent K _m=15 M) and of ATP (apparent K _m=30 M) were required in catalytic amounts. Ti(III) could be substituted by reduced ferredoxin. ATP could not be substituted by AMP, CTP, GTP, S-adenosylmethionine, or by ATP analogues. The membrane fraction was methylated by CH₃–H₄MPT in the absence of H–S–CoM. This methylation was dependent on Ti(III) and ATP. The methylated membrane fraction catalyzed the methyltransfer from CH₃–H₄MPT to H–S–CoM in the absence of ATP and Ti(III). Demethylation in the presence of H–S–CoM also did not require Ti(III) or ATP. Based on these findings a mechanism for the methyltransfer reaction and for the activation of the enzyme is proposed.Abbreviations H₄MPT tetrahydromethanopterin - CH₃–H₄MPT N ⁵-methyl-H₄MPT - H–S–CoM 2-mercaptoethanesulfonate or coenzyme M - CH₃–S–CoM 2(methylthio)ethanesulfonate or methylcoenzyme M - SDS-PAGE sodium dodecylsulfate polyacrylamide gel electrophoresis - DTT dithiothreitol - MOPS morpholinopropanesulfonate - CHAPS 3-[(3-cholamidopropyl)-dimethylammonio]-1-propane-sulfonate - 1 U = 1 mol/min     

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)     

Two N 5, N 10-methylenetetrahydromethanopterin dehydrogenases in the extreme thermophile Methanopyrus kandleri: characterization of the coenzyme F420-dependent enzyme

It was recently reported that the extreme thermophile Methanopyrus kandleri contains only a H₂-forming N ⁵, N ¹⁰-methylenetetrahydromethanopterin dehydrogenase which uses protons as electron acceptor. We describe here the presence in this Archaeon of a second N ⁵,N ¹⁰-methylenetetrahydromethanopterin dehydrogenase which is coenzyme F₄₂₀-dependent. This enzyme was purified and characterized. The enzyme was colourless, had an apparent molecular mass of 300 kDa, an isoelectric point of 3.7±0.2 and was composed of only one type of subunit of apparent molecular mass of 36 kDa. The enzyme activity increased to an optimum with increasing salt concentrations. Optimal salt concentrations were e.g. 2 M (NH₄)₂SO₄, 2 M Na₂HPO₄, 1.5 M K₂HPO₄, and 2 M NaCl. In the absence of salts the enzyme exhibited almost no activity. The salts affected mainly the V _max rather than the K _m of the enzyme. The catalytic mechanism of the dehydrogenase was determined to be of the ternary complex type, in agreement with the finding that the enzyme lacked a chromophoric prosthetic group. In the presence of M (NH₄)₂SO₄ the V _max was 4000 U/mg (k _cat=2400 s^-1) and the K _m for N ⁵,N ¹⁰-methylenetetrahydromethanopterin and for coenzyme F₄₂₀ were 80 M and 20 M, respectively. The enzyme was relatively heat-stable and lost no activity when incubated anaerobically in 50 mM K₂HPO₄ at 90°C for one hour. The N-terminal amino acid sequence was found to be similar to that of the F₄₂₀-dependent N ⁵, N ¹⁰-methylenetetrahydromethanopterin dehydrogenase from Methanobacterium thermoautotrophicum, Methanosarcina barkeri, and Archaeoglobus fulgidus.Abbreviations H₄MPT tetrahydromethanopterin - F₄₂₀ coenzyme F₄₂₀ - CH₂=H₄MPT N ⁵,N ¹⁰-methylenetrahydromethanopterin - CHH₄MPT⁺ N ⁵,N ¹⁰-methenyltetrahydromethanopterin - methylene-H₄MPT dehydrogenase N ⁵,N ¹⁰-methylenetetrahydromethanopterin dehydrogenase - Mops N-morpholinopropane sulfonic acid - Tricine N-[Tris(hydroxymethyl)-methyl]glycine - 1 U = 1 mol/min     

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.     

N 5,N 10-Methylenetetrahydromethanopterin reductase (coenzyme F420-dependent) and formylmethanofuran dehydrogenase from the hyperthermophile Archaeoglobus fulgidus

Methylene-H₄MPT reductase was found to be present in Archaeoglobus fulgidus in a specific activity of 1 U/mg. The reductase was purified 410-fold. The native enzyme showed an apparent molecular mass of approximately 200 kDa. Sodium dodecylsulfate/polyacrylamide gel electrophoresis revealed the presence of only 1 polypeptide of apparent molecular mass 35 kDa. The ultraviolet/visible spectrum of the reductase was almost identical to that of albumin indicating the absence of a chromophoric prosthetic group. The reductase was dependent on reduced coenzyme F₄₂₀ as electron donor. Neither NADH, NADPH, nor reduced viologen dyes could substitute for the reduced deazaflavin. From reciprocal plots, which showed an intersecting patter, a K _m for methylene-H₄MPT of 16 M, a K _m for F₄₂₀H₂ of 4 M, and a V _max of 450 U/mg (K_cat=265 s^-1) were obtained. The enzyme was found to be rapidly inactivated when incubated at 80°C in 100 mM Tris/HCl pH 7. The rate of inactivation, however, decreased to essentially zero in the presence of either F₄₂₀ (0.2 mM), methylene-H₄MPT (0.2 mM), albumin (1 mg/ml), or KCl (0.5 M). The N-terminal amino acid sequence was determined and found to be similar to that of methylene-H₄MPT reductase (F₄₂₀-dependent) from the methanogens Methanobacterium thermoautotrophicum, Methanosarcina barkeri, and Methanopyrus kandleri. The purification and some properties of formylmethanofuran dehydrogenase from A. fulgidus are also described.Abbreviations H₄MPT tetrahydromethanopterin - CH₂=H₄MPT N ⁵,N ¹⁰-methylene-H₄MPT - CH₃–H₄MPT N ⁵-methyl-H₄MPT - CHH₄MPT methenyl-H₄MPT - F₄₂₀ coenzyme F₄₂₀ - MFR methanofuran - CHO-MFR formyl-MFR - 1 U 1 mol/min     

Growth yields and saturation constant of Desulfovibrio vulgaris in chemostat culture

Desulfovibrio vulgaris (strain Marburg) was grown on H₂ and sulfate as sole energy source in a chemostat limited by the sulfate supply. The biomass concentration and the sulfate concentration in the culture were determined as a function of the dilution rate. From the data a K _S (saturation constant) for sulfate of 10 M, a _max of 0.23 h^–1, and a of 13 g/mol were calculated. The organism was also grown in chemostat culture on H₂ and sulfite, H₂ and thiosulfate, and pyruvate (without sulfate). was found to be 35 g/mol, 36 g/mol, and Y _pyr ^max 10 g/mol. The growth yields are discussed with respect to ATP gains in dissimilatory sulfate reduction.     

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     

Growth parameters (K s, μmax,Y s) of Methanobacterium thermoautotrophicum

Methanobacterium thermoautotrophicum was grown on a mineral salts medium in a fermenter gassed with H₂ and CO₂, which were the sole carbon and energy sources. Under the conditions used the bacterium grew exponentially. The dependence of the growth rate () on the concentration of H₂ and CO₂ in the incoming gas and the dependence of the growth yield ( ) on the growth rate were determined at pH 7 (the pH optimum) and 65° C (the temperature optimum).The curves relating growth rate to the H₂ and CO₂ concentration were hyperbolic. From reciprocal plots apparent K _s values for H₂ and CO₂ and _max were obtained: app. = 20%; app. = 11%; = 0.69 h^-1; t (max)=1 h. was 1.6 g mol^-1 and almost independent of the growth rate, when the rate of methane formation was not limited by the supply of either H₂ or CO₂. The yield increased to near 3 g mol^-1 when H₂ or CO₂ were limiting. These findings indicate that methane formation and growth are less tightly coupled at high concentrations of H₂ or CO₂ in the medium than at low concentrations. The physiological significance of these findings is discussed. K _s: H₂ and CO₂ concentration supporting 0.5 _max; _max: specific growth rate at infinite substrate concentration; Y _s:growth yield (g dry weight/mol substrate); t : doubling time     

Non-aceticlastic methanogenesis from acetate: acetate oxidation by a thermophilic syntrophic coculture

Methanogenesis from acetate by a rod-shaped enrichment culture grown at 60° C was found to require the presence of two organisms rather than a single aceticlastic methanogen. A thermophilic Methanobacterium which grew on H₂/CO₂ or formate was isolated from the enrichment. Lawns of this methanogen were used to co-isolate an acetate oxidizer in roll tubes containing acetate agar. The rod-shaped acetate oxidizer was morphologically distinct from the methanogen and did not show F₄₂₀ autofluorescence. The coculture completely degraded 40 mol/ml acetate, and produced nearly equal quantities of methane, and methanogenesis was coupled with growth. The doubling time for the coculture at 60°C was 30–40 h and the yield was 2.7±0.3 g dry wt/mol CH₄. Studies with ¹⁴C-labelled substrates showed that the methyl group and the carboxyl group of acetate were both converted primarily to CO₂ by the coculture and that CO₂ was concurrently reduced to CH₄. During growth, there was significant isotopic exchange between CO₂ and acetate, especially with thecarboxyl position of acetate. These results support a mechanism for methanogenesis from acetate by the coculture in which acetate was oxidized to CO₂ and H₂ by one organism, while H₂ was subsequently used by a second organism to reduce CO₂ to CH₄. Since the H₂ partial pressure must be maintained below 10^-4 atm by the methanogen for acetate oxidation to be thermodynamically feasible, this is an example of obligate interspecies hydrogen transfer. This mechanism was originally proposed for a single organism by Barker in 1936.     

Mixotrophy in the termite gut acetogen,Sporomusa termitida

Cell suspensions of H₂/CO₂-grown Sporomusa termitida catalyzed an H₂-supported synthesis of acetate from CO₂ at rates of about 1 mol acetate x h^-1 x mg protein^-1. Cells pre-grown on methanol, mannitol, lactate, or glycine also displayed H₂-supported acetogenesis from CO₂, although at rates 5–85% that of H₂/CO₂-grown cells. With methanol-grown cell suspensions: the presence of methanol greatly stimulated the rate of H₂-supported conversion of ¹⁴CO₂ to ¹⁴C-acetate (which became labeled mainly in the COOH-group); and like-wise the presence of H₂ stimulated the conversion of ¹⁴CH₃OH+CO₂ to ¹⁴C-acetate (which became labeled mainlyan the CH₃-group). Analogous stimulatory effects were observed for cell suspensions pre-grown on methanol + CO₂+H₂. Furthermore, when H₂ (+CO₂) was included as a growth substrate with either methanol or lactate: both substrates were used simultaneously; there was no diauxie in the growth of cells or in acetate production; and the molar growth yield of S. termitida was close to that predicted from summation of the yields observed when grown with each substrate alone. These data indicated that S. termitida can grow by mixotrophy, i.e. by the simultaneous use of H₂/CO₂ and organic compounds for energy. Results are discussed in light of the ability of H₂/CO₂ acetogens to outprocess methanogens in H₂ consumption in the hindgut fermentation of wood-feeding termites.     

Enzymes and coenzymes of the carbon monoxide dehydrogenase pathway for autotrophic CO2 fixation in Archaeoglobus lithotrophicus and the lack of carbon monoxide dehydrogenase in the heterotrophic A. profundus

Archaeoglobus lithotrophicus is a hyperthermophilic Archaeon that grows on H₂ and sulfate as energy sources and CO₂ as sole carbon source. The autotrophic sulfate reducer was shown to contain all the enzyme activities and coenzymes of the reductive carbon monoxide dehydrogenase pathway for autotrophic CO₂ fixation as operative in methanogenic Archaea. With the exception of carbon monoxide dehydrogenase these enzymes and coenzymes were also found in A. profundus. This organism grows lithotrophically on H₂ and sulfate, but differs from A. lithotrophicus in that it cannot grow autotrophically: A. profundus requires acetate and CO₂ for biosynthesis. The absence of carbon monoxide dehydrogenase in A. profundus is substantiated by the observation that this organism, in contrast to A. lithotrophicus, is not mini-methanogenic and contains only relatively low concentrations of corrinoids.Abbreviations F ₄₂₀ coenzyme F₄₂₀ - MFR methanofuran - CHO-MFR formylmethanofuran - H ₄MPT 5,6,7,8-tetrahydromethanopterin - CHO–H ₄MPT N⁵ formyl-H₄MPT - CHH₄MPT⁺N⁵ methenyl-H₄MPT - CH ₂=H₄MPT N⁵, N¹⁰ methylene-H₄MPT - CH ₃–H₄MPT N⁵ methyl-H₄MPT - H ₄F tetrahydrofolate - I U 1 mol/min - t _d doubling time     

Energy conservation in the extreme thermophile Thermus thermophilus HB8

Whole cells of the extreme thermophile Thermus thermophilus HB8 contained a membrane-bound respiratory chain (comprised of nicotinamide nucleotide transhydrogenase, NADH dehydrogenase, menaquinone, and cytochromes b, c, aa₃, o), which exhibited a maximumH⁺/O quotient of approximately 8 g-ion H⁺·g-atom O^-1 for the oxidation of endogenous substrates. Whole cell respiration at 70° at the expense of endogenous substrates or ascorbate-TMPD generated a transmembrane protonmotive force (p) of up to 197 mV and an intracellular phosphorylation poteintial (Gp), measured under similar conditions, of approximately 43.9 kJ·mol^-1.The measured Gp/p ratio thus indicated anH⁺/ATP quotient of approximately 2.3 g-ion H⁺·mole ATP^-1. Glucose-limited continuous cultures of T. thermophilus at 60°, 70° and 78.5° exhibited extremely low moler growth yields (Y _O2 ^max 27.6 g cells·mol O ₂ ^-1 ; Y _glucose ^max 64.4 g cells ·mol glucose^-1) compared with mesophilic bacteria of similar respiratory chain composition and proton translocation efficiency. These low yields are probably at least partly explained by the extremely high permeability of the cytoplasmic membrane to H⁺, which thus causes the cells to respire rapidly in order to maintain the protonmotive force at a level commensurate with cell growth.Abbreviations TPMP⁺ triphenylmethylphosphonium cation - FCCP carbonylcyanide p-trifluoromethoxy phenythydrazone - TMPD N,N,N,N-tetramethyl-p-phenylene diamine     

Competition between sulfate-reducing and methanogenic bacteria for H2 under resting and growing conditions

The basis for the outcome of competition between sulfidogens and methanogens for H₂ was examined by comparing the kinetic parameters of representatives of each group separately and in co-culture. Michaelis-Menten parameters (V _max and K _m) for four methanogens and five sulfate-reducing bacteria were determined from H₂-depletion data. Further, Monod growth parameters (_max, K _s, Y _H2) for Desulfovibrio sp. G11 and Methanospirillum hungatei JF-1 were similarly estimated. H₂ K _m values for the methanogenic bacteria ranged from 2.5 M (Methanospirillum PM1) to 13 M for Methanosarcina barkeri MS; Methanospirillum hungatei JF-1 and Methanobacterium PM2 had intermediate H₂ K _m estimates of 5 M. Average H₂ K _m estimates for the five sulfidogens was 1.2 M. No consistent difference among the V _max estimates for the above sulfidogens (mean=100 nmol H₂ min^-1 mg^-1 protein) and methanogens (mean=110 nmol H₂ min^-1 mg^-1 protein) was found. A two-term Michaelis-Menten equation accurately predicted the apparent H₂ K _m values and the fate of H₂ by resting co-cultures of sulfate-reducers and methanogens. Half-saturation coefficients (K _s) for H₂-limited growth of Desulfovibrio sp. G11 (2–4 M) and Methanospirillum JF-1 (6–7 M) were comparable to H₂ K _m estimates obtained for these organisms. Maximum specific growth rates for Desulfovibrio sp. G11 (0.05 h^-1) were similar to those of Methanospirillum JF-1 (0.05–0.06 h^-1); whereas G11 had an average yield coefficient 4 x that of JF-1. Calculated _max and V _max/K _m values for the methanogens and sulfidogens studied predict that the latter bacterial group will process more H₂ whether these organisms are in a growing or resting state, when the H₂ concentration is in the first-order region.     

Methane and hydrogen production in a termite-symbiont system

Methane and hydrogen emission rates and the ¹³C of CH₄ were observed for various termites in Australia, Thailand and Japan. Combined with the already reported emission rates of CH₄ in the literature, the phylogenetic trend was examined. Emission rates of the observed termites were categorized into five groups: group I with high CH₄ and low H₂ emission rates with a CH₄/H₂ ratio of typically 10/1; group II with high CH₄ and high H₂ emissions with a CH₄/H₂ ratio of 4/1–1/2; group III with low emission rates of CH₄ and H₂; group IV with high H₂ and insignificant CH₄ emissions; and group V with insignificant emissions for both CH₄ and H₂. In lower termites, there are both colonies infected and uninfected with methanogens even in the same species, and no specific trend in CH₄ and H₂ emissions was observed within a genus. Whether protozoa in the hindgut of termites are infected with methanogens or not and the differences in species compositions of protozoa are possibly responsible for the inter-colonial variations. The proportions of infected colonies were possibly small for the family Kalotermitidae (dry wood feeders), and relatively large for families of wet or damp wood feeders. The hydrogen emission rate possibly depends on the locality of methanogens: namely, whether they are intracellular symbionts of protozoa or whether they are attached to the hindgut wall. Emission rates of higher termites were classified into groups according to genera and the diet. Most species of soil or wood/soil interface feeders classified into group I, while the soil feeders Dicuspiditermes in Thailand and Amitermes in Australia were classified into groups with high H₂ emission rates. Typical wood-feeding termites and fungus-growing termites were classified into group III. The results indicate that higher termites tend to increase the CH₄ emission rate during dietary evolution from wood- to soil-feeding, and two types of the system with different efficiencies of interspecies transfer of H₂ have been formed. The ¹³C of CH₄ was discernible with a difference in the decomposition process in the termite–symbiont system among lower termites, fungus-growing termites and other higher termites.     

Energetics of syntrophic ethanol oxidation in defined chemostat cocultures

The ethanol-oxidizing, proton-reducing Pelobacter acetylenicus was grown in chemostat cocultures with either Acetobacterium woodii, Methanobacterium bryantii, or Desulfovibrio desulfuricans. Stable steady state conditions with tightly coupled growth were reached at various dilution rates between 0.02 and 0.14 h^-1. Both ethanol and H₂ steady state concentrations increased with growth rate and were lower in cocultures with the sulfate reducer < methanogen < homoacetogen. Due to the higher affinity for H₂, D. desulfuricans outcompeted M. bryantii, and this one A. woodii when inoculated in cocultures with P. acetylenicus. Cocultures with A. woodii had lower H₂ steady state concentrations when bicarbonate reduction was replaced by the energetically more favourable caffeate reduction. Similarly, cocultures with D. desulfuricans had lower H₂ concentrations with nitrate than with sulfate as electron acceptor. The Gibbs free energy (G) available to the H₂-producing P. acetylenicus was independent of growth rate and the H₂-utilizing partner, whereas the G available to the latter increased with growth rate and the energy yielding potential of the H₂ oxidation reaction. The critical Gibbs free energy (G_c), i.e. the minimum energy required for H₂ production and H₂ oxidation, was-5.5 to-8.0 kJ mol^-1 H₂ for P. acetylenicus,-5.1 to-6.3 kJ mol^-1 H₂ for A. woodii,-7.5 to-9.1 kJ mol^-1 H₂ for M. bryantii, and-10.3 to-12.3 kJ mol^-1 H₂ for D. desulfuricans. Obviously, the potentially available energy was used more efficiently by homoacetogens > methanogens > sulfate reducers.     

Purification and properties of N 5 ,N 10 -methylenetetrahydromethanopterin reductase (coenzyme F420-dependent) from the extreme thermophile Methanopyrus kandleri

Methanopyrus kandleri belongs to a novel group of abyssal methanogenic archaebacteria that can grow at 110°C on H₂ and CO₂ and that shows no close phylogenetic relationship to any methanogens known so far. N ⁵ N ¹⁰ -Methylenetetrahydromethanopterin reductase, an enzyme involved in methanogenesis from CO₂, was purified from this hyperthermophile. The apparent molecular mass of the native enzyme was found to be 300 kDa. Sodium dodecylsulfate/polyacrylamide gel electrophoresis revealed the presence of only one polypeptide of apparent molecular mass 38 kDa. The ultraviolet/visible spectrum of the enzyme was almost identical to that of albumin indicating the absence of a chromophoric prosthetic group. The reductase was specific for reduced coenzyme F₄₂₀ as electron donor; NADH, NADPH or reduced dyes could not substitute for the 5-deazaflavin. The catalytic mechanism was found to be of the ternary complex type as deduced from initial velocity plots. V _max at 65°C and pH 6.8 was 435 U/mg (k_cat=275 s^-1) and the K _m for methylenetetrahydro-methanopterin and for reduced F₄₂₀ were 6 M and 4 M, respectively. From Arrhenius plots an activation energy of 34 kJ/mol was determined. The Q ₁₀ between 40°C and 90°C was 1.5.The reductase activity was found to be stimulated over 100-fold by sulfate and by phosphate. Maximal stimulation (100-fold) was observed at a sulfate concentration of 2.2 M and at a phosphate concentration of 2.5 M. Sodium-, potassium-, and ammonium salts of these anions were equally effective. Chloride, however, could not substitute for sulfate or phosphate in stimulating the enzyme activity.The thermostability of the reductase was found to be very low in the absence of salts. In their presence, however, the reductase was highly thermostable. Salt concentrations between 0.1 M and 1.5 M were required for maximal stability. Potassium salts proved more effective than ammonium salts, and the latter more effective than sodium salts in stabilizing the enzyme activity. The anion was of less importance.The N-terminal amino acid sequence of the reductase from M. kandleri was determined and compared with that of the enzyme from Methanobacterium thermoautotrophicum and Methanosarcina barkeri. Significant similarity was found.Abbreviations H₄MPT tetrahydromethanopterin - CH₂=H₄MPT N ⁵ ,N ¹⁰ -methylene-H₄MPT - CH₃-H₄MPT N ⁵-methyl-H₄MPT - CHH₄MPT⁺ N ⁵ ,N ¹⁰ -methenyl-H₄MPT - F₄₂₀ coenzyme F₄₂₀; 1 U=1 mol/min