| Literature DB >> 21837252 |
Johannes Zedelius, Ralf Rabus, Olav Grundmann, Insa Werner, Danny Brodkorb, Frank Schreiber, Petra Ehrenreich, Astrid Behrends, Heinz Wilkes, Michael Kube, Richard Reinhardt, Friedrich Widdel.
Abstract
Microorganisms can degradeEntities:
Year: 2011 PMID: 21837252 PMCID: PMC3151549 DOI: 10.1111/j.1758-2229.2010.00198.x
Source DB: PubMed Journal: Environ Microbiol Rep ISSN: 1758-2229 Impact factor: 3.541
Fig. 1Phylogenetic (16S rRNA-based) affiliation of strain HdN1 with selected Beta- and Gammaproteobacteria including other strains able to degrade aromatic or saturated petroleum hydrocarbons with nitrate (*). Strains able to degrade n-alkanes anaerobically are highlighted in bold; occurrence of (1-methylalkyl)succinate formation for alkane activation is also indicated (M). Bootstrap values (%; only > 60% shown) were obtained after 1000 resamplings. Scale bar, 10% estimated sequence divergence.
Fig. 2Microscopic images of strain HdN1.
A. Highly variable cell forms of strain HdN1 grown anaerobically with hexadecane and nitrate. Phase-contrast micrographs of viable cells. Bar, 5 µm.
B. Cells from a pure culture of strain HdN1 hybridized with a specific 16S rRNA-targeted oligonucleotide probe and stained with DAPI. The image represents an overlay of the probe and the DAPI signal. Bar, 5 µm.
C. Mixed cells of strains HdN1 and OcN1 hybridized, stained and visualized as in (B). Bar, 5 µm.
Fig. 3Time-courses of the formation of N2O (A and B), N2 (C and D) and CO2 (E and F) in anaerobic cultures of strain HdN1 with n-hexadecane (A, C and E) or palmitate (B, D and F). The electron acceptors were added in stoichiometrically limiting amounts (100 µmol of NO3−; c. 250 µmol of N2O) relative to the electron donor (171 µmol of hexadecane, advantage of large excess explained in text; 10 µmol of palmitate). Results show that alkane oxidation to CO2 was not possible with N2O, but readily occurred with NO3−. The functionalized compound, palmitate, was oxidized with N2O. Duplicates yielded the same results (not shown). Culture volumes of 10 ml (phosphate-buffered medium, pH ≈ 7.1, without addition of NaHCO3; Appendix S1) were incubated in 165 ml serum bottles under an argon headspace. N2O was injected as pure O2-free gas. Cultures were very gently shaken for a few minutes per day. Vigorous shaking had to be avoided because it impeded growth. Samples from the headspace were analysed with a gas chromatograph employing argon as carrier gas and a thermal conductivity detector. The calculated dissolved amounts of gases were added so as to obtain the total amounts in the bottles. Calculation was based on literature data (Wilhelm ; Stumm and Morgan, 1995), assuming equilibrium (which may not have been fully reached due to limited agitation) and considering pH in the case of CO2.
Fig. 4N2 formed in anaerobic cultures of strains HdN1, HxN1 and OcN1 with alkanes (black bars) or fatty acids (striated bars) and either NO3− (100 µmol) or N2O (250 µmol). A control experiment with strain HdN1 for excluding N2O toxicity received both, NO3− and N2O. Here, more N2 was formed than with NO3− alone. This indicated that not only NO3− but also N2O was used in the anaerobic respiratory chain if alkane degradation was enabled by NO3−. Data show that strain HdN1 could not use N2O alone for alkane degradation, in contrast to the other strains. Culture volumes of 10 ml were incubated in 20 ml butyl-rubber sealed tubes. Strain HdN1 received 171 µmol of pure n-hexadecane, or 10 µmol of palmitate. Strain HxN1 received 38 µmol of n-hexane (in 100 µl of heptamethylnonane as carrier), or 30 µmol of caproate. Strain OcN1 received 31 µmol of n-octane (in 100 µl of heptamethylnonane), or 30 µmol of caproate. Tubes were incubated nearly horizontally while contact of the hydrocarbon phase with the stopper was avoided (Widdel, 2009) as far as possible. Gas samples were withdrawn 11 days after inoculation and analysed (triplicates) as indicated in Fig. 3.
Fig. 5Hypothetical involvement of denitrification intermediates in alkane activation. The scheme offers an explanation for the inability of strain HdN1 to utilize n-alkanes with N2O alone (see Figs 3 and 4). It is assumed that a small proportion of NO2− or NO is deviated from the respiratory chain for alkane activation. They may be used for activation indirectly (by yielding O2 that is used by alkane monooxygenase; or by giving rise to another reactive factor or enzyme centre) or directly (as co-reactants introducing a polar group). The alkyl residue R′ may or may not be identical with the original residue R (depending on the activation mechanism and alkane C-atom being attacked). FA, fatty acid; TCA, tricarboxylic acid cycle.
Fig. 6Some energetic aspects of N–O (and N–H) species. Graphs are for the following activities or fugacities: {NO3−}, {NO2−}, {NH3 (g)}, {NH4+} = 10−2; {N2 (g)} = 10−0.1 (78% in air); {O2 (g)} = 10−0.7 (21% in air); {H2} = 1; {NO (g)}, {N2O (g)} = 10−4.3 (approximately corresponding to dissolved concentrations monitored under natural conditions; Schreiber ).A. E–pH (stability, Pourbaix) diagram of the system H–N–O. Only N2 and the lowest and highest oxidation states, NH4+, NH3 and NO3−, are thermodynamically stable. Other metabolically formed inorganic N-compounds are metastable (endergonic; e.g. Eqs 1 and 2) and can, in principle, spontaneously decompose (dismutate) into the species (including O2) depicted in the diagram. Endergonic N-compounds can be metabolically formed because they appear as co-products besides H2O (from reductive O elimination).B. Electrochemical half-reactions (including hypothetical ones) of N–O species and O2. If an endergonic N-compound does not react via dismutation (e.g. Eqs 1 and 2) but in an electrochemical half-reaction (yielding the same product as dismutation), this half-reaction has a higher redox potential than that of O2/2H2O (E°′ = +0.815 V). Again, this does not contradict the fact that NO3− and NO2− originate from a microbial oxidation process with O2 (see under A; also, the reaction sequence in nitrification is different: NH4+/NH3→ NH2OH → NO2−). Generally, the redox potentials (E) of subsequent reduction steps (i = 1, 2, …, m) of an overall reduction with free intermediates are linked to an average redox potential (Eav) according to (n1E1 + n2E2 + … + n)/ntot = Eav; n is the number of electrons involved in an individual step and ntot the total number of electrons. Eav is connected to the total free energy change, ΔGtot, of the overall reduction with an electron-donating reaction of the redox potential Edon according to Eav = −ΔGtot/(ntotF) + Edon, with F = 96 485 C mol−1 (explanation in Appendix S2). Eav of 2NO3−/N2 marks the borderline between the stability regions of NO3− and N2 in the E–pH diagram (A). In a real metabolic process, a strong oxidant formed in a reduction sequence can only appear as free intermediate if its further reduction is enzymatically controlled and if unspecific reactions with reductants are slower or do not take place. Also, overall irreversibility is required, but this is naturally given (in an equilibrium system, redox pairs with different redox potential, e.g. NO3−/ NO2− and NO2−/NO, cannot coexist).Calculations are based on standard free energy data (Garrels and Christ, 1965; Thauer ). Derived standard redox potentials at pH = 7 (E°′/V): NO3−/NO2−, +0.431; 2NO3−/N2, +0.747 (av); NO2−/NO, +0.347; 2NO2−/N2, +0.958; 2NO/N2O, +1.172; 2NO/N2, +1.264; N2O/N2; +1.355.