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Applied and Environmental Microbiology, September 2005, p. 5267-5274, Vol. 71, No. 9
0099-2240/05/$08.00+0 doi:10.1128/AEM.71.9.5267-5274.2005
Copyright © 2005, American Society for Microbiology. All Rights Reserved.
Environmental Science Research Center, School of Public and Environmental Affairs, Indiana University, Bloomington, Indiana 47405
Received 14 July 2004/ Accepted 13 April 2005
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3 mM NO3 reduction was observed during reduction of a variety of Fe(III) (hydr)oxides, including goethite, hematite, and an iron-bearing, natural sediment. Inhibition of oxygen and fumarate reduction was observed following treatment of cells with Fe2+ and NO2, demonstrating that utilization of other soluble electron acceptors could also be inhibited. Previous adsorption of Fe2+ onto Paracoccus denitrificans inhibited NOx reduction, showing that Fe(II) can reduce rates of soluble electron acceptor utilization by non-iron-reducing bacteria. NO2 was chemically reduced to N2O by goethite or cell-sorbed Fe2+, but not at appreciable rates by aqueous Fe2+. Transmission and scanning electron microscopy showed an electron-dense, Fe-enriched coating on cells treated with Fe2+ and NO2. The formation and effects of such coatings underscore the complexity of the biogeochemical reactions that occur in the subsurface. |
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Nitrate has both natural and anthropogenic sources, but the extensive use of NO3 as an agricultural fertilizer threatens the quality of many groundwater systems (41). The use of denitrifying microorganisms to remediate NOx-contaminated soils may be a solution for its removal in some environments (27). Since contaminant metals and NO3 may coexist in some iron-bearing sediments (12, 31), it is important to understand the complex, biogeochemical interactions that can occur during the microbial reduction of NOx and Fe(III) (hydr)oxides. Shewanella putrefaciens 200 is a facultative anaerobe capable of utilizing NO3, NO2, and Fe(III), as well as O2, Mn(IV), trimethylamine N-oxide, thiosulfate, fumarate, and a number of other compounds as terminal electron acceptors for carbon metabolism (9, 29, 30). This makes S. putrefaciens an ideal organism for studying biogeochemical interactions during redox transformations of NO3/NO2 and Fe(III)/Fe(II).
NOx reduction by microorganisms typically precedes ferric (hydr)oxide reduction in experimental or subsurface systems, in part because NOx tends to be more available to cells than the highly insoluble (at neutral pH) forms of Fe(III) (1, 9, 29, 30, 39). Recently, though, Cooper et al. reported that the reduction of NO3 and NO2 by S. putrefaciens 200 was inhibited by the presence of the solid-phase ferric (hydr)oxide goethite (
-FeOOH) (6). In addition, they observed that the presence of goethite in NOx-reducing incubations resulted in greatly enhanced production of N2O. Cooper et al. speculated that the inhibition and enhanced N2O production resulted from reaction of small amounts of biogenic Fe(II) with NO2 to form an Fe (hydr)oxide coating on the cell surface that inhibited transport of soluble electron acceptors into the cell. Although the stoichiometry and products are subject to speculation, reaction 1 shows such a reaction between surface-sorbed Fe2+ (
Fe2+) and NO2 that could lead to production of a solid Fe (hydr)oxide.
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| (1) |
-FeOOH) (40). The hypothetical mechanism suggested by Cooper et al. requires the sorption of Fe2+ to the cell surface before reacting with aqueous NO2. Dissimilatory iron-reducing bacteria are known to sorb Fe2+ to their cell surfaces, and such sorption is believed to passivate the surface and impede further Fe(III) reduction (34, 46, 47). Fe2+ is relatively soluble at neutral pH and, in anoxic, iron-reducing environments, there may also be significant sorption of Fe2+ to cell surfaces of bacteria incapable of iron reduction. NO2, whether from anthropogenic sources or produced via nitrification or denitrification, will have the opportunity to react with that sorbed Fe2+. The oxidation of surface-bound Fe2+ by NO2 and resulting formation of a Fe (hydr)oxide mineral on the surface of the cell could have a rapid, inhibitory affect on the transport of soluble electron acceptors into the cell. Although recent work has established the ability of some bacteria to catalyze Fe(II)-dependent reduction of NO3 (45, 49), little is known about how abiotic NOx reduction by cell-sorbed Fe2+ will affect microbial metabolism. Processes that limit the rate or extent of NOx reduction may have notable environmental effects. Attempts to bioremediate a NOx-contaminated site by addition of a suitable substrate, for example, would take longer and be more costly. Since NO3 must often be consumed prior to bioremediation of metals and radionuclides (5, 11), remediation of these compounds may also be negatively affected by processes that limit NOx removal. The same inhibition mechanism may also affect the reduction of other environmentally relevant electron acceptors, which has broad implications for the understanding of subsurface geochemical cycles. Since N2O, a product of the proposed reaction, is also a potent greenhouse gas also believed to be implicated in stratospheric ozone depletion (7, 10, 48), increased knowledge about possible N2O sources may improve our modeling of global climate change and other environmental stresses.
The inhibitory mechanism proposed by Cooper et al. was supported primarily by nitrogen stable isotope experiments that showed that the increased N2O production was primarily of chemical origin, i.e., produced by the abiotic reduction of NO2 by surface-bound Fe2+ produced during microbial reduction of synthetic goethite. Their proposed mechanism, however, was largely speculative, direct evidence of such Fe-rich cell coatings was not provided, and the potential environmental significance of the reaction was not apparent. In the current work, we demonstrate that NOx reduction is inhibited during reduction of other Fe(III) minerals, that the utilization of soluble electron acceptors other than NOx are similarly inhibited, and that NOx reduction by microorganisms incapable of dissimilatory iron reduction can also be inhibited by sorption of aqueous Fe2+. In addition, we provide direct evidence of an Fe-rich, electron-dense coating formed on bacteria in the presence of NO2 and Fe2+.
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, 600 nm) of approximately 1.2 in low-ionic-strength, artificial groundwater (AGW) medium. The full composition of AGW medium is described elsewhere (5). This medium contains 15 mM lactate as an electron donor, and primary buffering capacity is provided by 10 mM HEPES buffer. Phosphate (0.044 mM) and bicarbonate (0.50 mM) concentrations are relatively low to minimize the potential for precipitation of vivianite or siderite.
Fe(III) and NOx reduction experiments.
Although the general methodology employed in the Fe(III) and NO3 reduction experiments has been previously described (6), a summary of the procedure is presented here. All experiments were conducted in 150-ml serum bottles, crimp sealed with butyl rubber stoppers under a 95% N2-5% H2 headspace. Except where noted, slurries were established that contained 75 ml AGW medium and the appropriate solid phase. Three solid phases were used in separate experiments as sources of ferric iron: goethite (
-FeOOH,) hematite (Fe2O3), and an iron-containing natural sediment. Goethite was prepared as described by Schwertmann and Cornell (36), hematite was purchased from J.T. Baker/Mallinckrodt Baker Inc., and the natural sediment (MNC-71) was collected from iron-bearing, clayey sediments at Marshall, N.C. (J. Zachara, PNNL, personal communication). The amount of each sediment required for the 50 mM Fe3+ (by citrate dithionate extraction) used in these experiments was approximately 0.34 g goethite, 0.6 g hematite, and 4.9 g MNC-71 in 75 ml of medium. When required, NO3 or NO2 was added to serum bottles from sterile stock solutions of NaNO3 and NaNO2. In experiments requiring a chelator to reduce Fe2+ adsorption to cell surfaces, 1.0 ml sterile anaerobic nitrilotriacetic acid (NTA) stock solution was added to the AGW medium for a final concentration of 5.0 mM.
Experiments were initiated by inoculating slurries with 1 ml of washed S. putrefaciens suspension under anoxic conditions (ca. 2 x106 cells ml1). Serum bottle reactors were wrapped in foil and incubated horizontally on a shaker table at room temperature. Initial samples were taken prior to inoculation, and subsequent samples were taken at regular intervals thereafter. During sampling, bottles were transferred to the anaerobic chamber, shaken vigorously, and immediately sampled with a 3-ml syringe (23-gauge needle). A 1.5-ml aliquot of slurry was transferred to a microcentrifuge tube, and solids were separated by centrifugation. The supernatant was immediately sampled for pH, NO3, and NO2. To determine if the observed inhibition of NOx reduction was due to unknown goethite toxicity, a different bacterium (Paracoccus denitrificans) was substituted for S. putrefaciens. P. denitrificans is able to utilize NO3 as a terminal electron acceptor but is unable to reduce Fe(III). The same growth and experimental procedures described above for goethite and NO3 reduction were followed, using P. denitrificans in place of S. putrefaciens.
Reaction of NO2 with sorbed Fe2+.
Experiments were done to measure N2O production from the abiotic reduction of NO2 by aqueous Fe2+ or Fe2+ sorbed to a goethite surface. Previously deoxygenated AGW medium lacking vitamins and lactate was dispensed into replicate (n = 3) sets of serum bottle batch reactors in an anaerobic chamber (Coy Laboratory Products, Grass Lake, MI). The first set contained 3 mM Fe2+ added from a stock solution of FeCl2 that had been prepared anoxically, adjusted to pH 7, and filtered (0.45 µm) to remove fine particulates. This filtration step was required to ensure that only aqueous Fe2+ was utilized and Fe(III) oxides present as contaminants on the FeCl2 crystals or formed in trace amounts during stock solution preparation were not inadvertently added. The second and third sets of replicates contained 50 mM goethite and 50 mM goethite plus 3 mM Fe2+, respectively. After 24 h, all systems received an amendment of NO2 as NaNO2 to a final concentration of 3 mM. N2O production was measured in all three systems over time as described below.
Fe2+ was sorbed to the surface of S. putrefaciens and P. denitrificans (4, 38) to compare the inhibition of NOx reduction by bacteria able and unable to reduce Fe(III). S. putrefaciens and P. denitrificans were grown and harvested as described above and then resuspended in anaerobic AGW medium containing 50 mM FeCl2 (pH,
7) in the anaerobic chamber. The resuspension was gently mixed for 15 min to allow adsorption of Fe2+ onto the cell surfaces. The cells were then centrifuged again in tightly sealed centrifuge tubes to prevent Fe2+ oxidation and washed with anaerobic, Fe-free AGW before being used to inoculate replicate reactors containing 3 mM NO3 or NO2. Control reactors were set up identically except they were initially resuspended in Fe-free AGW medium.
Additional experiments were similarly done (only with S. putrefaciens) to determine if sorption of Fe2+ and subsequent exposure to NO2 would impede the utilization of soluble electron acceptors other than NO3 or NO2. In these experiments, Fe2+ was sorbed to cells and suspensions were harvested and washed as described above. The washed cells were then incubated in anaerobic AGW medium containing 5 mM NO2 which was allowed to react for 1 h with the Fe2+ sorbed to cells. Cells were washed and subsequently incubated in AGW amended either with 5 mM fumarate or
8.6 mg liter1 O2. Consumption of the electron acceptor over time was compared with identical suspensions that had not undergone the Fe2+ sorption step. Where reported, initial and final cell numbers were determined by acridine orange direct counting (15).
Electron microscopy and electron dispersion spectroscopy.
Cells of S. putrefaciens for examination using transmission and scanning electron microscopy (TEM and SEM) were prepared by sequential incubation with Fe2+ and NO2 as described above to abiotically simulate the formation of the Fe(III) (hydr)oxide coating believed to form in NOx- reducing incubations containing goethite. Control cells were incubated solely with either Fe2+ or NO2 for comparison. All preparation of samples for TEM and SEM analyses was performed in an anaerobic chamber to prevent oxidation of Fe2+. For TEM analysis, prepared cells were placed on parlodian support films on 300 mesh copper grids and allowed to dry in the anaerobic chamber. Dried grids with cells were placed in an anaerobic container (BBL GasPak system) for transport to the TEM facility and were exposed to the air for less than 1 minute while being transferred to the TEM vacuum chamber. Treated and control cells were observed at 100 kV on a JEOL JEM-1010 transmission electron microscope, and images were taken at a magnification of x12,000. For SEM analysis, prepared cells were filtered onto a 0.45-µm membrane filter, dehydrated using graded alcohol-water washes, and critical point dried in hexamethyldisilazane. Following gold coating, treated and control cells were observed at 20.0 kV on a FEI Quanta 400F scanning electron microscope at a magnifications between x23,000 and x78,000. Surface point elemental analysis was performed while the samples were being viewed in the SEM using a Princeton Gamma-Tech energy-dispersive spectrometer.
Analytical methods.
Samples for NO3 and NO2 analyses were diluted twofold in Milli-Q water, frozen, and stored for later analysis by ion chromatography as previously described (6). NH4+ was quantified in some experiments using the colorimetric phenate method (15). N2O production was quantified by removing 25.0 µl of headspace gas from the batch reactors using a gas-tight syringe and analyzed via gas chromatography as previously described (6).
When applicable, aqueous and cell-bound Fe2+ was analyzed via a modification of the ferrozine method (35, 42). Surface areas of the various iron oxides used were determined by multipoint Brunauer-Emmett-Teller (BET) N2 adsorption on a NOVA 1000 surface area analyzer. Oxygen utilization rate was determined using a YSI biological oxygen monitor. Fumarate concentrations were quantified on a Waters high-performance liquid chromatography apparatus using an absorbance detector at a wavelength of 238 nm.
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9 m2 g1) is much less than that of the goethite (
72 m2 g1) used in previous experiments where inhibition of NO3 reduction occurred almost immediately (6). The microbially accessible surface area of an iron oxide has a significant effect on the rate and extent of iron oxide reduction (34, 35). Less Fe(III) reduced to Fe2+ would in turn affect the rate of the hypothesized surface reaction between Fe2+ and NO2.
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FIG. 1. NO3 reduction by S. putrefaciens in the presence of 50 mmol liter1 hematite ( ) and without hematite ( ) and NO2 production/reduction in the presence of 50 mmol liter1 hematite () and without hematite ( ). Error bars indicate the standard deviations of the means (n = 3).
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FIG. 2. NO3 reduction by S. putrefaciens in the presence of the natural sediment MNC-71 ( ) and without MNC-71 ( ) and NO2 production/reduction in the presence of MNC-71 () and without MNC-71 ( ). Error bars indicate the standard deviations of the means (n = 3).
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In order to test whether the reaction between NO2 and Fe2+ was indeed surface catalyzed, the chelator NTA was used to complex with Fe2+ produced during the reduction of goethite. The formation of an NTA-Fe2+ complex would reduce Fe2+ sorption and, if the reaction with NO2 was indeed surface catalyzed, we expected that this would minimize the formation of the hypothetical Fe (hydr)oxide coating on the cell and allow NO3 reduction to proceed normally. Previous studies under similar conditions have reported no detectible Fe(III)aq in NTA-amended (5 mM) systems containing 50 mM goethite and inoculated with Shewanella alga (47). The NTA amendments were therefore not expected to significantly contribute to the dissolution of Fe(III) from goethite. Figure 3 summarizes the results, which support the surface reaction hypothesis. Without NTA, NO3 reduction was inhibited by up to 200 h in systems containing both goethite and NO3. When NTA was present at 5 mM in goethite-containing systems, NO3 reduction was complete within 50 h. In goethite-free controls (with and without NTA), NO3 reduction was complete by 30 h. The temporary inhibition seen in the system containing goethite and NTA may be due to Fe2+ sorbing to the cell surface before having a chance to complex with NTA. The rate and extent of Fe(III) mineral reduction is increased in the presence of NTA (2, 47), and it is reasonable to postulate that a portion of the Fe2+ formed at the mineral-microbe interface may be temporarily sorbed to the cell before removal by the chelators.
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FIG. 3. NO3 reduction by S. putrefaciens with 5 mmol liter1 NTA ( ), without NTA ( ), with 50 mmol liter1 goethite ( ), and with 5 mmol liter1 NTA plus 50 mmol liter1 goethite (). Error bars are not shown for cultures lacking goethite, for the sake of clarity.
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Sorption of Fe2+ and reaction with NO2.
In the absence of an iron (hydr)oxide, S. putrefaciens 200 primarily reduces NO3 and NO2 to ammonia and typically produces only trace amounts of N2O (6), presumably as an enzymatic side reaction during dissimilatory reduction of nitrate to ammonia (3, 43). In systems containing small amounts of biogenic Fe2+, goethite, and S. putrefaciens, though, Cooper et al. found N2O production in amounts 10-fold greater than when goethite was absent (6). Additional experiments were done to clearly determine if the enhanced N2O production observed in microbial systems containing NOx and goethite could be explained solely by the abiotic reduction by surface-bound Fe2+. The first set of abiotic, replicate batch reactors contained 3 mM aqueous Fe2+ and 3 mM NO2; the second set contained 50 mM of goethite and 3 mM NO2; the third contained all three components, Fe2+, NO2, and goethite. As can be seen in Fig. 4, bottles containing only aqueous Fe2+ and NO2 generated only 30 µM N2O after 125 h. In contrast, bottles containing Fe2+, NO2, and goethite had generated 225 µM N2O after 30 h and, eventually, 260 µM after 125 h. Controls containing only NO2 and goethite amendments did not produce any N2O over the course of the experiment. These results are in agreement with studies by Sørensen et al., in which very little N2O was produced by reaction of aqueous Fe2+ and NOx in systems lacking a surface catalyst (40). The results also confirm that, under our experimental conditions, Fe2+ will sorb to a surface such as goethite and abiotically reduce NO2 to N2O. Although the mechanistic details of the surface reaction remain unknown, it is possible that surface sorption of Fe2+ increases the local electron density over that in aqueous solution, thereby increasing the possibility of reduction reactions involving multiple electrons. It is possible that a similar reaction could occur on cell surfaces which have adsorbed Fe2+.
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FIG. 4. N2O production in systems containing aqueous Fe2+ (2 mmol liter1) and NO2 (3 mmol liter1) ( ), aqueous Fe2+, NO2, and 50 mmol liter1 goethite ( ), and NO2 and 50 mmol liter1 goethite (). Error bars indicate the standard deviations of the means (n = 3).
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FIG. 5. (a) NO3 reduction by S. putrefaciens treated with Fe2+ ( ) and without treatment ( ). (b) NO2 reduction by S. putrefaciens treated with Fe2+ and NO2 () and without treatment ( ). Error bars indicate the standard deviations of the means (n = 3).
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FIG. 6. (a) NO3 reduction by P. denitrificans treated with Fe2+ and NO2 ( ) and without treatment ( ). (b) NO2 reduction by P. denitrificans treated with Fe2+ and NO2 () and without treatment ( ). Error bars indicate the standard deviations of the means (n = 3).
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Fumarate reduction by cells treated with Fe2+ and NO2 was also severely inhibited compared to cells exposed to just NO2 (Fig. 7). After 12 h, about 3.5 times more fumarate remained in systems containing cells exposed to both Fe2+ and NO2 than in those systems containing cells previously exposed to NO2 alone. Fumarate reduction in treated systems was still not complete after 48 h. Both the O2 and fumarate reduction results suggest that the inhibitory effect of the Fe (hydr)oxide coating on the reduction of soluble electron acceptors is not restricted to NO3 and NO2 but may have broad environmental implications concerning the utilization of environmentally significant electron acceptors.
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FIG. 7. Fumarate reduction by S. putrefaciens treated with Fe2+ and NO2 ( ) and without treatment ( ). Error bars indicate the standard deviations of the means (n = 3).
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FIG. 8. Transmission and scanning electron micrographs of S. putrefaciens under three treatments. (A and D) Cells treated with NO2; (B and E) cells treated with Fe2+; (C and F) cells treated with both Fe2+ and NO2. The electron-dense coating on the cells in panel C and the rough surface on the cells in panel F represent an Fe (oxy)hydroxide coating formed from the reaction between surface-bound Fe2+ and NO2. The inset on each SEM image is an EDS point scan that corresponds to the cells in the image.
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Conclusions.
Support for the proposed inhibition mechanism involving the reaction of NO2 and surface-bound Fe2+ is evident in the results demonstrating that the presence of Fe2+ on the surface of cells leads to the production of N2O and an inhibition of NOx reduction even at small concentrations of Fe2+. This reaction occurs using a variety of Fe oxides, including an iron-bearing natural sediment, can occur with bacterial species incapable of Fe(III) reduction if they are in environments containing aqueous Fe2+, and affects several soluble terminal electron acceptors. The exact composition of the Fe (hydr)oxide coating is not yet known. The extent and significance of N2O formation via this reaction in the environment is not known but could be significant in iron-bearing soils during microbial remediation of NOx contamination. The potential increase of both Fe2+ and NO2 production during bioremediation efforts could significantly increase the formation of N2O as a by-product, and the implications of this reaction for metal bioremediation efforts, geochemical cycling, and greenhouse gas production make it an important subject for further investigation.
We also thank Craig Cooper for valuable discussions and mentorship, Barry Stein for guidance using the TEM, Juergen Schieber for patience and persistence with the SEM/EDS analyses, and Ai Nguyen for assistance in the some of the experiments.
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-FeOOH) suspensions by a dissimilatory metal-reducing bacterium. Geochim. Cosmochim. Acta 64:3085-3098.[CrossRef]
-FeOOH) of Fe(II)-dependent nitrite reduction. Geochim. Cosmochim. Acta 55:1289-1294.
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