Continuous measurement of dissolved H2 in an anaerobic reactor using a new hydrogen/air fuel cell detector

A miniature fuel cell, using a hydrophobic Teflon(R) membrane, designed to continuously measure dissolved H(2) in nonbiological media, was tested for use in anaerobic digestion conditions. In water, this detector responds quickly and efficiently to variation of hydrogen concentration in the range from 80 to 770 nM The media used, and the metabolites or products found in anaerobic digestion media, i. e. inorganic carbon and phosphate buffers, formate, acetate, and dissolved methane, did not interfere with the signal of the detector cell. Dissolved hydrogen sulfide did not poison the cell but was detected. In spite of the detector's high sensitivity to hydrogen (about 21,000 times higher for hydrogen than for hydrogen sulfide), interferences can occur in media containing high sulfide levels.In a methanogenic reactor, the detector cell response to dissolved hydrogen was fast and reliable with time. The observed values ranged values ranged from 2 to 3.5muM. Dissolved hydrogen concentrations were 40 to 70 times higher than values calculated from measured hydrogen partial pressures and Henry's coefficient, suggesting a limitation of the process in the hydrogen transfer from the liquid to the gaseous phase.     

Effects of light/dark cycle, mixing pattern and partial pressure of H2 on biohydrogen production by Rhodobacter sphaeroides ZX-5

The effects of light/dark cycle, mixing pattern and partial pressure of H₂ on the growth and hydrogen production of Rhodobacter sphaeroides ZX-5 were investigated. The results from light/dark cycle culture showed that little or no hydrogen production was observed during the dark periods, and the hydrogen production immediately recovered once illumination was resumed. Also, it was found that the optimum condition of shaking velocity was 120 rpm for hydrogen photo-fermentation. Meanwhile, shaking during H₂ production phase (i.e., cell growth stationary phase) of photo-fermentation played a crucial role on effectively enhancing the phototrophic hydrogen production, rather than that during cell exponential growth phase. The other factor evaluated was hydrogen partial pressure in the culture system. The substrate conversion efficiency increased from 86.07% to 95.56% along with the decrease of the total pressure in the photobioreactor from 1.082 × 10⁵ to 0.944 × 10⁵ Pa, which indicated that reduction of H₂ partial pressure by lowering the operating pressure substantially improved H₂ production in an anaerobic, photo-fermentation process.     

Photochemical disproportionation of sulfur into sulfide and sulfate byChlorobium limicola formathiosulfatophilum

The anaerobic bacteriumChlorobium assimilates carbon dioxide in the light with various sulfur compounds as electron donors. The well-known metabolic pathway proceeds from the oxidation of sulfide via sulfur to sulfate. In the dark the reaction is partially reversed when sulfur is reduced to hydrogen sulfide. The fermenting cells thereby release an excess of reductant. We have now found a hydrogen sulfide production from sulfur, which is light-dependent. It is more than ten times faster than the dark reaction. This appears in experiments where the cell suspension is illuminated in absence of CO₂ and flushed continuously with H₂ or Ar. The H₂S is trapped with ZnCl₂ and the S^2- titrated with iodine. The total amount of H₂S evolved in the light increases proportionally with the amount of sulfur added, and about one-half of the added sulfur is converted to H₂S. Another part of the metabolized sulfur appears at the same time as sulfate, but all the sulfur oxidized to sulfate does not account for the larger amount of sulfur reduced to hydrogen sulfide. Very likely other unanalyzed oxidized sulfur compounds must also have been produced. Use of H₂ instead of Ar as the anaerobic gas phase does not increase the amount of H₂S produced, nor does the addition of thiosulfate; sulfur itself is the preferred electron donor for the sulfur reduction. Up to a light intensity of 10000 ergs cm^-2sec^-1 CO₂ does not affect H₂S production. Without CO₂, saturation of the light-dependent evolution of H₂S is reached at about 40000 ergs cm^-2sec^-1. In contrast, presence of CO₂ at this light intensity makes the sulfide production disappear completely. On application of mass spectrometry to the gas exchange upon illumination, at high light intensity a H₂S gush is found during the first 3 min. This is followed by CO₂ fixation, while simultaneously the reductant H₂S is now taken up. WithRhodospirillum rubrum, the addition of sulfur leads to a moderate evolution of H₂S. In contrast toChlorobium this reaction inR. rubrum is not light-sensitive, nor does it produce detectable amounts of sulfate. After addition of malate the rate of H₂S evolution does increase in the light, since the cells use malate as an electron donor during their photochemical metabolism.     

Hydrogen sulfide releasing enmein-type diterpenoid derivatives as apoptosis inducers through mitochondria-related pathways

In this study, we combined two enemin-type diterpenoid derivatives with two well-established hydrogen sulfide moieties via ester or different anhydride linkers, to search apoptosis inducing drug candidate capable of hydrogen sulfide generating. Therefore, a series of hybrids were synthesized and superior antiproliferative efficacy accompanied with enhanced selectivity was observed under extensive pharmacological evaluations. A standard methylene blue (MB⁺) method was applied to measure the capacity for the hydrogen sulfide generation of all the target derivatives. One particular molecule A1, which contained α-thioctic acid moiety for hydrogen sulfide donating, manifested more potent antiproliferative activity. It exerted inhibitory effects against Bel-7402, SGC-7901 and A549 cell lines with IC₅₀ values of 2.16, 5.07 and 6.98 μM respectively. While it exacted relatively low effects over human normal cell lines L-02 and PBMC with IC₅₀ values of 15.81 μM for the prior and 14.15 μM for the latter, and displayed better selectivity index (SI) than parent diterpenoids. A high dosage of H₂S release was also recorded. Hence, A1 was most suitable for mechanistic exploration on account of both safety and efficacy. The ensuing biological assays revealed central role of apoptosis in A1’s mode of action for antiproliferative efficacy, which led to further confirmation of G1 phase cell cycle arrest, mitochondria membrane potential collapse and apoptotic activation in Bel-7402 cells. Further western blot assay on intrinsic mitochondria pathway unlocked intricate interplay among a series of apoptotic related proteins in which Bax, caspase-3 and cytochrome c went through up-regulation, while Bcl-2, Bcl-xL and procaspase-3 undergone down-regulation. In a nutshell, a hydrogen sulfide releasing hybrid A1 was synthesized and antiproliferative evaluation identified it to be a worthy drug candidate for future in depth study.     

Biohydrogen production in alkalithermophilic conditions: Thermobrachium celere as a case study

In the present work the hydrogenesis in the anaerobic alkalithermophilic bacterium Thermobrachium celere was studied. The impact of several factors on hydrogen production during glucose fermentation was investigated in batch conditions. The optimal hydrogen production occurred at pH_67 °C 8.2 with phosphate buffer concentration of 50 mM. Hydrogen yield reached the highest value of 3.36 mol H₂/mol glucose when the partial pressure in the gas headspace was reduced. Supplementation of nitrogen sources and iron affected hydrogen production. Under optimized conditions, the maximum H₂ accumulation and H₂ production rate were estimated to be respectively 124.3 mmol H₂/l culture and 20.7 mmol H₂/l/h. Considering the efficient and rapid hydrogen evolution, and the ability to grow in extreme environments, T. celere might be a good candidate for biohydrogen production in open (non-sterile) bioprocess system.     

Control of Carbon and Electron Flow in Clostridium acetobutylicum Fermentations: Utilization of Carbon Monoxide to Inhibit Hydrogen Production and to Enhance Butanol Yields

Extracts prepared from non-solvent-producing cells of Clostridium acetobutylicum contained methyl viologen-linked hydrogenase activity (20 U/mg of protein at 37°C) but did not display carbon monoxide dehydrogenase activity. CO addition readily inhibited the hydrogenase activity of cell extracts or of viable metabolizing cells. Increasing the partial pressure of CO (2 to 10%) in unshaken anaerobic culture tube headspaces significantly inhibited (90% inhibition at 10% CO) both growth and hydrogen production by C. acetobutylicum. Growth was not sensitive to low partial pressures of CO (i.e., up to 15%) in pH-controlled fermentors (pH 4.5) that were continuously gassed and mixed. CO addition dramatically altered the glucose fermentation balance of C. acetobutylicum by diverting carbon and electrons away from H₂, CO₂, acetate, and butyrate production and towards production of ethanol and butanol. The butanol concentration was increased from 65 to 106 mM and the butanol productivity (i.e., the ratio of butanol produced/total acids and solvents produced) was increased by 31% when glucose fermentations maintained at pH 4.5 were continuously gassed with 85% N₂-15% CO versus N₂ alone. The results are discussed in terms of metabolic regulation of C. acetobutylicum saccharide fermentations to achieve maximal butanol or solvent yield.     

Mass spectrometric control of the thermophilic anaerobic digestion process based on levels of dissolved hydrogen

Summary The continuous and simultaneous monitoring of dissolved CH₄ and H₂ in samples from a laboratory scale thermophilic anaerobic digester contents by use of a silicone rubber-covered probe has enabled control of methanogenesis: regulation of the hydrogen signal in a closed feedback loop was by controlled addition of the carbon source. Dissolved hydrogen became apparent in this system at a lower loading rate than was obtained for a mesophilic anaerobic digestion system (Whitmoreet al., 1986). Controlling the supply of glucose (25 mM) at a dilution rate of 0.02 h^–1 and at progressively lower preset hydrogen levels allowed methanogenesis to be significantly prolonged before inhibition of the process occurred.     

Control of Oxidative Sulfur Metabolism of Chlorobium limicola forma thiosulfatophilum

A metered blend of anaerobic-grade N₂, CO₂, and H₂S gases was introduced into an illuminated, 800-ml liquid volume, continuously stirred tank reactor. The system, described as an anaerobic gas-to-liquid phase fed-batch reactor, was used to investigate the effects of H₂S flow rate and light energy on the accumulation of oxidized sulfur compounds formed by the photoautotroph Chlorobium limicola forma thiosulfatophilum during growth. Elemental sulfur was formed and accumulated in stoichiometric quantities when light energy and H₂S molar flow rate levels were optimally adjusted in the presence of nonlimiting CO₂. Deviation from the optimal H₂S and light energy levels resulted in either oxidation of sulfur or complete inhibition of sulfide oxidation. Based on these observations, a model of sulfide and sulfur oxidases electrochemically coupled to the photosynthetic reaction center of Chlorobium spp. is presented. The dynamic deregulation of oxidative pathways may be a mechanism for supplying the photosynthetic reaction center with a continuous source of electrons during periods of varying light and substrate availability, as in pond ecosystems where Chlorobium spp. are found. Possible applications for a sulfide gas removal process are discussed.     

Simulation of constituent processes of anaerobic degradation of organic matter by the 〈methane〉 model

The model of anaerobic digestion described earlier by the authors was used for analysis of the different phases of the process. It was shown that at the glucose conversion a coexistence of hydrogen-producing acidogenic bacteria and hydrogen-utilizing non-methanogenic bacteria causes a hydrogen partial pressure decrease at an increase of solids retention time (i), the intensity of the negative feed-back effect in sulfate-reduction through hydrogen sulfide formation is regulated by the pH level during an oscillation dynamics in acetate/sulfate system (ii), under the toxicity influence the processes of methanogenesis and acetogenesis together with hydrolysis may be rate-limiting steps in the anaerobic system with particulate substrate degradation (iii).Abbreviations B1, B2 two groups of acidogens - DS total dissolved sulfide concentration - HRT hydraulic retention time - MPB methane-producing bacteria - SRB sulfate-reducing bacteria - SRT solids retention time - VFA's volatile fatty acids     

Control of Interspecies Electron Flow during Anaerobic Digestion: Role of Floc Formation in Syntrophic Methanogenesis

The flora of an anaerobic whey-processing chemostat was separated by anaerobic sedimentation techniques into a free-living bacterial fraction and a bacterial floc fraction. The floc fraction constituted a major part (i.e., 57% total protein) of the total microbial population in the digestor, and it accounted for 87% of the total CO₂-dependent methanogenic activity and 76% of the total ethanol-consuming acetogenic activity. Lactose was degraded by both cellular fractions, but in the free flora fraction it was associated with higher intermediary levels of H₂, ethanol, butyrate, and propionate production. Electron microscopic analysis of flocs showed bacterial diversity and juxtapositioning of tentative Desulfovibrio and Methanobacterium species without significant microcolony formation. Ethanol, an intermediary product of lactose-hydrolyzing bacteria, was converted to acetate and methane within the flocs by interspecies electron transfer. Ethanol-dependent methane formation was compartmentalized and closely coupled kinetically within the flocs but without significant formation of H₂ gas. Physical disruption of flocs into fragments of 10- to 20-μm diameter initially increased the H₂ partial pressure but did not change the carbon transformation kinetic patterns of ethanol metabolism or demonstrate a significant role for H₂ in CO₂ reduction to methane. The data demonstrate that floc formation in a whey-processing anaerobic digestor functions in juxtapositioning cells for interspecies electron transfer during syntrophic ethanol conversion into acetate and methane but by a mechanism which was independent of the available dissolved H₂ gas pool in the ecosystem.     

Characterizing and modeling hydrogen sulfide production in anaerobic digestion of livestock manure,agro-industrial wastes,and wastewater sludge

Hydrogen sulfide (H₂S) is the most undesirable inorganic gas in biogas from anaerobic digestion (AD). However, H₂S production in AD is complex and understanding of its processes is still limited. This study performed six controlled batch anaerobic co-digestion experiments to investigate H₂S production. Materials were obtained from four field anaerobic digester systems and co-digestion feedstocks from agroindustry. An additional precipitation experiment was conducted to further examine H₂S production dynamics. Digesters containing highly soluble, carbohydrate-based wastes had a high H₂S final specific production (FSP) value. Additionally, the FSP values were negatively correlated with the initial Fe(II):S ratios in the digester liquid of the batch tests. The precipitation experiment indicated that iron sulfide precipitation was preferred in the presence of an anaerobic community. The H₂S production as a time series was successfully modeled using a generalized additive model (R² > 0.82). This study revealed that sulfate, phosphorus, and iron concentrations are important predictors and potential inhibitors of H₂S production in AD. Further examination of real-time H₂S modeling in AD is warranted.     

Properties of the hydrogenase system in Rhizobium japonicum bacteroids

The hydrogenase system which catalyzes the oxyhydrogen reaction in soybean nodules produced by strains of $\text{Rhizobium japonicum}$ is located in the bacteroids. The hydrogenase complex in intact bacteroids has an apparent K_m for H₂ of 2.8 μM and an apparent K_m for O₂ of 1.3 μM. The addition of hydrogen to bacteroids increases oxygen uptake but decreases respiratory CO₂ production, indicating a conservation of endogenous substrates. After correction for the effect of hydrogen on endogenous respiration a ratio of 1.9 ± 0.1 for H₂ to O₂ uptake was determined. Bacteroids from greenhouse or field-grown soybeans that evolved hydrogen showed no measurable oxyhydrogen reaction activity whereas consistent activity was demonstrated by bacteroids from soybean nodules that evolved little or no H₂.     

Anaerobic versus Aerobic Degradation of Dimethyl Sulfide and Methanethiol in Anoxic Freshwater Sediments

Degradation of dimethyl sulfide and methanethiol in slurries prepared from sediments of minerotrophic peatland ditches were studied under various conditions. Maximal aerobic dimethyl sulfide-degrading capacities (4.95 nmol per ml of sediment slurry · h⁻¹), measured in bottles shaken under an air atmosphere, were 10-fold higher than the maximal anaerobic degrading capacities determined from bottles shaken under N₂ or H₂ atmosphere (0.37 and 0.32 nmol per ml of sediment slurry · h⁻¹, respectively). Incubations under experimental conditions which mimic the in situ conditions (i.e., not shaken and with an air headspace), however, revealed that aerobic degradation of dimethyl sulfide and methanethiol in freshwater sediments is low due to oxygen limitation. Inhibition studies with bromoethanesulfonic acid and sodium tungstate demonstrated that the degradation of dimethyl sulfide and methanethiol in these incubations originated mainly from methanogenic activity. Prolonged incubation under a H₂ atmosphere resulted in lower dimethyl sulfide degradation rates. Kinetic analysis of the data resulted in apparent K_m values (6 to 8 μM) for aerobic dimethyl sulfide degradation which are comparable to those reported for Thiobacillus spp., Hyphomicrobium spp., and other methylotrophs. Apparent K_m values determined for anaerobic degradation of dimethyl sulfide (3 to 8 μM) were of the same order of magnitude. The low apparent K_m values obtained explain the low dimethyl sulfide and methanethiol concentrations in freshwater sediments that we reported previously. Our observations point to methanogenesis as the major mechanism of dimethyl sulfide and methanethiol consumption in freshwater sediments.     

Co-digestion of manure and whey for in situ biogas upgrading by the addition of H2: process performance and microbial insights

In situ biogas upgrading was conducted by introducing H₂ directly to the anaerobic reactor. As H₂ addition is associated with consumption of the CO₂ in the biogas reactor, pH increased to higher than 8.0 when manure alone was used as substrate. By co-digestion of manure with acidic whey, the pH in the anaerobic reactor with the addition of hydrogen could be maintained below 8.0, which did not have inhibition to the anaerobic process. The H₂ distribution systems (diffusers with different pore sizes) and liquid mixing intensities were demonstrated to affect the gas-liquid mass transfer of H₂ and the biogas composition. The best biogas composition (75:6.6:18.4) was obtained at stirring speed 150 rpm and using ceramic diffuser, while the biogas in the control reactor consisted of CH₄ and CO₂ at a ratio of 55:45. The consumed hydrogen was almost completely converted to CH₄, and there was no significant accumulation of VFA in the effluent. The study showed that addition of hydrogen had positive effect on the methanogenesis, but had no obvious effect on the acetogenesis. Both hydrogenotrophic methanogenic activity and the concentration of coenzyme F₄₂₀ involved in methanogenesis were increased. The archaeal community was also altered with the addition of hydrogen, and a Methanothermobacter thermautotrophicus related band appeared in a denaturing gradient gel electrophoresis gel from the sample of the reactor with hydrogen addition. Though the addition of hydrogen increased the dissolved hydrogen concentration, the degradation of propionate was still thermodynamically feasible at the reactor conditions.     

Hydrogen Partial Pressures in a Thermophilic Acetate-Oxidizing Methanogenic Coculture

Hydrogen partial pressures were measured in a thermophilic coculture comprised of a eubacterial rod which oxidized acetate to H₂ and CO₂ and a hydrogenotrophic methanogen, Methanobacterium sp. strain THF. Zinder and Koch (S. H. Zinder and M. Koch, Arch. Microbiol. 138:263-272, 1984) originally predicted, on the basis of calculations of Gibbs free energies of reactions, that the H₂ partial pressure near the midpoint of growth of the coculture should be near 4 Pa (ca. 4 × 10⁻⁵ atm; ca. 0.024 μM dissolved H₂) for both organisms to be able to conserve energy for growth. H₂ partial pressures in the coculture were measured to be between 20 and 50 Pa (0.12 to 0.30 μM) during acetate utilization, approximately one order of magnitude higher than originally predicted. However, when ΔG_f (free energy of formation) values were corrected for 60°C by using the relationship ΔG_f = ΔH_f − TΔS (ΔH_f is the enthalpy or heat of formation, ΔS is the entropy value, and T is the temperature in kelvins), the predicted value was near 15 Pa, in closer agreement with the experimentally determined values. The coculture also oxidized ethanol to acetate, a more thermodynamically favorable reaction than oxidation of acetate to CO₂. During ethanol oxidation, the H₂ partial pressure reached values as high as 200 Pa. Acetate was not used until after the ethanol was consumed and the H₂ partial pressure decreased to 40 to 50 Pa. After acetate utilization, H₂ partial pressures fell to approximately 10 Pa and remained there, indicating a threshold for H₂ utilization by the methanogen. Axenic cultures of the acetate-oxidizing organism were combined with pure cultures of either Methanobacterium sp. strain THF or Methanobacterium thermoautotrophicum ΔH to form reconstituted acetate-oxidizing cocultures. The H₂ partial pressures measured in both of these reconstituted cocultures were similar to those measured in the original acetate-oxidizing rod coculture. Since M. thermoautotrophicum ΔH did not use formate as a substrate, formate is not necessarily involved in interspecies electron transfer in this coculture.     

Hydrogen sulfide in regulation of frog myocardium contractility

Hydrogen sulfide (H₂S) is an endogenously synthesized gaseous molecule which, along with nitric oxide and carbon monoxide, induces a number of effects in cardiovascular system under normal and pathological conditions. In the present work, the effects and underlying mechanisms of the H₂S donor sodium hydrosulfide (NaHS) on the isometric force of frog myocardium contraction have been studied. NaHS at the concentration of 100 μM induced negative inotropic effect and reduced the maximum velocity of the contraction and relaxation of the isolated ventricle strips. The substrate of H₂S synthesis, L-cysteine (200 μM and 1 mM), induced the same effect, while the inhibitors of cystathionin-γ-lyase, the H₂S-producing enzyme in heart, β-cyanoalanine (500 μM) and propargylglycine (500 μM), increased the amplitude of contraction. Inhibition of cystathionin-γ-lyase by β-cyanoalanine prevented the negative inotropic effect of L-cysteine. After the inhibition of adenylate cyclase by MDL-12,330A (3 μM) or phosphodiesterases by IBMX (200 μM), the effect of NaHS was less than that in the control. In the presence of membrane-penetrating analogous of cAMP, 8Br-cAMP (100 μM) and pCPT-cAMP (100 μM), the negative inotropic effect of NaHS was completely retained. The effect of NaHS significantly decreased after preliminary application of the NO donor, SNAP (10 μM), and did not change after the inhibition of NO synthases by L-NAME (100 μM). The results suggest the possibility of endogenous synthesis of H₂S in frog myocardium and regulation of its contractility by the activation of phosphodiesterases hydrolyzing cAMP, which leads to a decrease in the activation of cAMP-dependent protein kinases and phosphorylation of voltage-dependent L-type Ca channels. As a result, the reduction of calcium entry into cardiomyocytes decreases the contractility of frog myocardium.     

Coupling of Methanothermobacter thermautotrophicus Methane Formation and Growth in Fed-Batch and Continuous Cultures under Different H2 Gassing Regimens

In nature, H₂- and CO₂-utilizing methanogenic archaea have to couple the processes of methanogenesis and autotrophic growth under highly variable conditions with respect to the supply and concentration of their energy source, hydrogen. To study the hydrogen-dependent coupling between methanogenesis and growth, Methanothermobacter thermautotrophicus was cultured in a fed-batch fermentor and in a chemostat under different 80% H₂-20% CO₂ gassing regimens while we continuously monitored the dissolved hydrogen partial pressures (p_H2). In the fed-batch system, in which the conditions continuously changed the uptake rates by the growing biomass, the organism displayed a complex and yet defined growth behavior, comprising the consecutive lag, exponential, and linear growth phases. It was found that the in situ hydrogen concentration affected the coupling between methanogenesis and growth in at least two respects. (i) The microorganism could adopt two distinct theoretical maximal growth yields (Y_{CH4 max}), notably approximately 3 and 7 g (dry weight) of methane formed mol⁻¹, for growth under low (p_H2 < 12 kPa)- and high-hydrogen conditions, respectively. The distinct values can be understood from a theoretical analysis of the process of methanogenesis presented in the supplemental material associated with this study. (ii) The in situ hydrogen concentration affected the “specific maintenance” requirements or, more likely, the degree of proton leakage and proton slippage processes. At low p_H2 values, the “specific maintenance” diminished and the specific growth yields approached Y_{CH4 max}, indicating that growth and methanogenesis became fully coupled.     

Thioacetamide as a source of hydrogen sulfide for colony growth of purple sulfur bacteria

Thioacetamide (TAA), CH₃CSNH₂, is an unstable sulfur compound which upon addition of acid decomposes into acetic acid, ammonia, and hydrogen sulfide (H₂S). This characteristic may be taken advantage of when doing plate counts or isolation streaks of phototrophic purple sulfur bacteria. We have performed plate counts and isolation streaks of these bacteria in Gas-Pak anaerobic jars (BBL) supplemented with a test tube containing 0.05 g or 0.10 g TAA dissolved in 1.0 ml of 0.2 N or 0.5 N HCl. It may be demonstrated in a Warburg respirometer that the gas is released over a period of at least 1 week. Colony growth may be observed in 5–10 days. One advantage of this technique is that sodium sulfide (Na₂S·9H₂O) need not be added to the agar medium, which, therefore, may be prepared and stored for future use. This technique has been used successfully for the isolation ofAmoebobacter, Chromatium, Ectothiorhodospira, Lamprocystis, Thiocapsa, andThiocystis.     

Mass-spectrometric kinetic studies of the nitrogenase and hydrogenase activities in in-vivo cultures of Azospirillum brasilense Sp. 7

Acetylene reduction, deuterium uptake and hydrogen evolution were followed in in-vivo cultures of Azospirillum brasilense, strain Sp 7, by a direct mass-spectrometric kinetic method. Although oxygen was needed for nitrogenase functioning, the enzyme was inactivated by a fairly low oxygen concentration in the culture and an equilibrium had to be found between the rate of oxygen diffusion and bacterial respiration. A nitrogenase-mediated hydrogen evolution was observed only in the presence of carbon monoxide inhibiting the uptake hydrogenase activity which normally recycles all the hydrogen produced. However, under anaerobic conditions and in the presence of deuterium, a bidirectional hydrogenase activity was observed, consisting in D₂ uptake and in H₂ and HD evolution. In contrast to the nitrogenase-mediated H₂ production, this anaerobic H₂ and HD evolution was insensitive to the presence of acetylene and was partly inhibited by carbon monoxide. It was moreover relatively unaffected by the deuterium partial pressure. These results suggest that the anaerobic H₂ and HD evolution can be ascribed to a reverse hydrogenase activity under conditions where D₂ is saturating the uptake process and scavenging the electron acceptors. Although the activities of both nitrogenase and hydrogenase were thus clearly differentiated, a close relationship was found between their respective functioning conditions.     

Studies on a gram-positive hydrogen bacterium,Nocardia opaca 1 b

Nocardia opaca strain 1 b has a NAD-dependent hydrogenase (hydrogen dehydrogenase). The enzyme has been purified from autotrophically grown cells and tested for optimal assay conditions and stability. The purification procedure involved protamine sulfate treatment, ammonium sulfate precipitation, and separation by DEAE-cellulose and Sephadex G-200 chromatography and resulted in a 63-fold increase of specific activity at a 11.7% enzyme recovery. The final specific activity was 103 μmoles H₂/min·mg protein. The purified enzyme was dependent on nickel and magnesium ions at 0.5 and 5.0 mM concentrations, respectively, as well as flavin mononucleotide at a 5–10 μM concentration. Straight enzyme kinetics were achieved by preincubating the enzyme in the presence of NADH₂. A high stability of the enzyme was observed in 0.1 M potassium phosphate buffer, pH 6.5, in the presence of 0.5 mM nickel and 5 mM magnesium ions under hydrogen atmosphere. Even under air the enzyme was remarkably stable, although less than under hydrogen. From double reciprocal plots of substrate saturation curves the Michaelis-Menten constants were calculated: For saturating NAD-concentration the K _m was 0.063 mM H₂ and for saturating hydrogen concentration the K _m was 0.123 mM NAD.