Patent Publication Number: US-2020277211-A1

Title: Oxidant enhanced feammox activity

Description:
RELATED APPLICATION DATA 
     The present invention claims priority pursuant to 35 U.S.C. § 119(e) to U.S. Provisional Patent Application Ser. No. 62/565,480 filed Sep. 29, 2017 which is hereby incorporated by reference in its entirety. The Sequence Listing titled “Sequence Listing,” having a file size of 2,867,945 bytes, created on Sep. 29, 2017 and filed herewith is incorporated herein by reference as if fully set forth. 
    
    
     GOVERNMENT SUPPORT 
     This invention was made with government support under Grant No. DE-SC0006847 awarded by the Department of Energy and Grant No. CBET-1433101 awarded by the National Science Foundation. The government has certain rights in this invention. 
    
    
     FIELD 
     The present application relates compositions and methods for environmental remediation and, in particular, to compositions and methods employing Feammox bacteria and an oxidant. 
     BACKGROUND 
     The removal of ammonium and other contaminants from soil and water is an important environmental task. Wastewater treatment plants in the developed world and in many developing countries oxidize NH 4   +  to NO 3   −  before discharging the treated wastewater. This is done to decrease oxygen demand in the receiving waters. Additionally, nitrogen excess in near shore environments has been identified as a major environmental problem leading to eutrophication and anoxia. Legislations are being implemented requiring the conversion of NO 3   −  to N 2  in conventional waste water treatment plants. The nitrogen compounds that are present in contaminated water, such as ammonium NH 4   + , nitrite (NO 2   − ) and nitrate (NO 3   − ) will have to be converted to elemental nitrogen N 2 , which can be released in the gaseous state into an open environment. 
     Nitrogen removal via nitrification and denitrification can be performed by microrganisms. Numerous studies have focused on the aerobic oxidation of ammonia or NH 4   +  to first nitrite (NO 2 —) and then nitrate (NO 3 ). Oxidation of NH 4   +  to NO 2   −  is the first and rate limiting biological step in the nitrification, and also a required step prior to anaerobic NH 4   +  oxidation (anammox), which is the biological conversion of NH 4   +  and NO 2   −  to nitrogen gas in the absence of oxygen. Anammox is the most common anaerobic NH 4   +  oxidation pathway in soils environments known so far, using NO 2   −  as the electron acceptor. Anaerobic NH 4   +  oxidation is performed by anammox bacteria. Aerobic NH 4   +  oxidation is performed by two groups of organisms, ammonia-oxidizing bacteria (AOB), and ammonia-oxidizing archaea (AOA). 
     In the wastewater treatment plants, biological ammonium oxidation is conducted by aerobic nitrifying bacteria and requires aeration in the step with the highest energy input. An alternative is the partial nitrification (nitritation) Anammox system, which has been implemented in some treatment plants, with the goal of saving energy costs, since only half of the NH 4   +  is converted to NO 2   −  aerobically. However, these Anammox based wastewater treatment systems need to operate between 28° C. and 35° C. 
     An NH 4   +  oxidation process coupled to iron (Fe) reduction called Feammox was identified (Clement J C et al. 2005 Soil Biol Biochem 37:2323-2328; Sawayama S. 2006; J Biosci Bioeng 101:70-72; Shrestha J et al. 2009 Soil Sci 174:156-164; Yang W H et al. 2012 Nat Geosc 5: 538-541, all of which are incorporated herein by reference as if fully set forth). Feammox is a process that can be described as the oxidation of NH 4   +  in the absence of molecular oxygen, with iron oxides [Ferric iron, Fe(III)] as the electron acceptor. In this reaction Fe(III) is reduced to Ferrous iron Fe(II), while NH 4   +  is transformed to NO 2   − , nitrogen gas (N 2 ), or other nitrogen forms. Feammox may provide benefits for development of an improved system that does not require aeration or heating of the wastewater in temperate climates. 
     SUMMARY 
     In one aspect, media are described herein comprising components for removal of ammonium containing contaminants. Briefly, a medium comprises an ammonium containing contaminant, an iron component, an oxidant, and a Feammox bacterium and/or enzyme thereof capable of oxidizing ammonium with reduction of Fe(III) to Fe(II), wherein the oxidant regenerates Fe(III) via Fe(II) oxidation. In some embodiments, the medium is soil or water. Moreover, the medium can further comprise at least one additional contaminant for removal. 
     In another aspect, systems for environmental remediation are provided. A system, for example, comprises a reactor including a medium comprising an ammonium containing contaminant, an iron component, an oxidant, and a Feammox bacterium and/or enzyme thereof capable of oxidizing ammonium with reduction of Fe(III) to Fe(II), wherein the oxidant regenerates Fe(III) via Fe(II) oxidation. In some embodiments, the reactor comprises an inlet and outlet for the medium, such as water and/or soil. The reactor, for example, can be operated continuously or in a batch mode. The medium, in some embodiments, can further comprise at least one additional contaminant for removal. 
     In another aspect, methods of environmental remediation are described herein. A method comprises providing a medium including one or more ammonium containing contaminants and disposing a Feammox bacterium and/or enzyme thereof in the medium. The Feammox bacterium and/or enzyme thereof participates in the oxidation of ammonium coupled with reduction of Fe(III) to Fe(II). An oxidant in the medium subsequently regenerates Fe(III) via Fe(II) oxidation. In some embodiments, oxidation of Fe(II) by the oxidant generates hydrogen ions that are consumed in the ammonium oxidation. Additionally, in some embodiments, the oxidant forms a compound with Fe(II) in the medium. 
     In another aspect, various compositions are described herein. In some embodiments, a composition comprises an Acidimicrobiaceae Feammox bacterium A6 having Accession Deposit Number PTA-122488, at least one of soil, wastewater, and a carrier, and elemental sulfur. The bacterium is capable of oxidizing ammonium coupled with reduction of Fe(III) to Fe(II). In other embodiments, a composition comprises at least one enzyme capable of oxidizing ammonium into nitrite, at least one of soil, wastewater, and a carrier, and elemental sulfur. The soil or wastewater comprises an ammonium containing contaminant, and the at least one enzyme comprises a sequence with at least 70% identity to the sequence selected from the group consisting of SEQ ID NOS: 29-49. 
     In another aspect, systems employing the various compositions are provided. In some embodiments, a system comprises a reactor and a composition that includes an Acidimicrobiaceae Feammox bacterium A6 having Accession Deposit Number PTA-122488, at least one of soil, wastewater and a carrier, and elemental sulfur. The bacterium is capable of oxidizing ammonium coupled with reduction of Fe(III) to Fe(II). 
     In another aspect, processes for reducing a nitrogen contaminant in soil and/or water are described herein. A process, in some embodiments, comprises mixing the wastewater with an Acidimicrobiaceae Feammox bacterium A6 having Accession Deposit Number PTA-122488 to form a mixture. The process also comprises adding elemental sulfur to the mixture. In some embodiments, the water can be wastewater or water from the ground water system. 
     In a further aspect, various hosts are provided including nucleic acids comprising a sequence with at least 70% identity to a reference sequence selected from the group consisting of SEQ ID NOS: 8-28. Additionally, compositions comprising such hosts are also contemplated. A composition, for example, can comprise one or more hosts, at least one or soil, wastewater, and a carrier and elemental sulfur. The soil or wastewater can comprise an ammonium containing contaminant. 
     These and other embodiments are described in further detail in the following detailed description. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIGS. 1A-1B  illustrate concentration of Fe(II) ( FIG. 1A ) and NH 4   +  ( FIG. 1B ) in incubation with three different Fe(III) sources: ferrihydrite (open circle), ferric chloride (closed square), and ferric citrate (closed triangle). 
         FIGS. 2A-2B  illustrate concentration of Fe(II) ( FIG. 2A ) and NH 4   +  ( FIG. 2B ) in 25-day incubation with NH 4 Cl and ferrihydrite (open circle), NH 4 Cl and goethite (closed circle). 
         FIGS. 3A-3B  illustrate concentration of Fe(II) ( FIG. 3A ) and NH 4   +  ( FIG. 3B ) during the 180 day incubation. 
         FIGS. 4A-4B  illustrate concentration of Fe(II) ( FIG. 4A ) and NH 4   +  ( FIG. 4B ) in 25-day incubations in samples with NH 4 Cl (open square), ferrihydrite (open circle), sterilized soil with NH 4 Cl and ferrihydrite (closed triangle). 
         FIGS. 5A-5B  illustrate concentration of NO 3   −  (open circle) and NO 2   −  (closed square) ( FIG. 5A ) and DOC (open triangle) and TN (open square) ( FIG. 5B ) during the 180 day incubation. 
         FIG. 6  illustrates comparison of DGGE analysis profiles of soil communities during anaerobic incubations. 
         FIG. 7  illustrates abundance of total bacteria (closed rhombus) during 180 days of anaerobic incubation, 16S rRNA gene (black bars) and RNA copy numbers (gray bars) of Acidimicrobiaceae bacterium A6 in soil samples with 1.20 mmol L −1  NaHCO 3  addition, 16S rRNA gene (white bars) and RNA copy numbers (dotted bars) of bacterium A6 with 0.20 mmol L −1  NaHCO 3  addition. 
         FIGS. 8A-8D  illustrate concentration of NH 4   +  ( FIG. 8A ), NO 2   −  ( FIG. 8B ), NO 3   −  ( FIG. 8C ), and N 2 O ( FIG. 8D ) in the samples incubated with (open circle) or without (closed square) C 2 H 2 . 
         FIG. 9  illustrates stoichiometry between the Fe(II) production and NH 4   +  consumption during 180 day incubation. 
         FIG. 10  illustrates a graph of ΔG vs. pH. 
         FIG. 11  illustrates a schematic representation of a membrane reactor for NH 4   +  oxidation via Feammox. 
         FIGS. 12A-12B  illustrate ordination plots of the canonical correspondence analysis (CCA) for the first two dimensions of CCA of the relationship between the environmental factors and Feammox bacteria vs. environment factor of soil analysis and relation of Feammox to other bacterial communities affecting the nitrogen cycle. 
         FIG. 12A  illustrates the total variance in the bacterial abundance and the cumulative variance of the bacteria-environment relationship.  FIG. 12B  illustrates the total variance in the microbial composition and the cumulative variance of the bacteria-sampling location relationship. 
         FIG. 13  illustrates NH 4   +  oxidized over 6 days by Acidimicrobiaceae bacteria A6. 
         FIG. 14  illustrates uranium U(VI) removed from solution over 6 days. 
         FIG. 15  illustrates reduction of Fe in nontronite over 12 days. 
         FIG. 16  illustrates total U and U(VI) concentrations over 11 days. 
         FIGS. 17A-17B  illustrate oxidation of NH 4   +  ( FIG. 17A ) and bioreduction of Cu(II) ( FIG. 17B ) by Feammox. Filled bars are for results with A6, and open bars are controls. 
         FIGS. 18A-18D  illustrate an effect of biodegradation of trichloroethylene (TCE) ( FIG. 18A ), tetrachloroethylene (PCE) ( FIG. 18B ), benzene ( FIG. 18C ) and phenanthrene ( FIG. 18D ) by Feammox. Filled bars are for results without FMO inhibitor, open bars are for results with FMO inhibitor and crosshatched bars are no NH 4   +  controls. 
         FIGS. 19A-19D  illustrate A6 bacterial cultures and cells.  FIG. 19A  illustrates growth of the A6 bacterium in the liquid medium.  FIG. 19B  illustrates A6 growth on the solid inorganic NH 4   + -ferric iron medium.  FIGS. 19C-19D  show rod-shaped A6 cells. 
         FIG. 20  illustrates anaerobic oxidation of ammonium by the A6 isolate. Filled bars are for results with NH 4   +  and stripped bars are results with NO 2   − . 
         FIG. 21  illustrates an effect of NH 4   +  concentration on its consumption by A6. 10 mM NH 4   +  results are reported in the left filled bar of each of days 0, 5, 10 and 20 panels. 5 mM NH 4   +  are reported in the middle dotted bar of each of days 0, 5, 10 and 20 panels. 1 mM NH 4   +  is reported in the right open bar of each of days 0, 5, 10 and 20 panels. 
         FIG. 22  illustrates iron reduction rates. Fe(II) results are reported in the left bar of each of the day 0, 10, and 20 panels. Fe(III) results are reported in the right bar of each of the days 0, 10, and 20 panels. 
         FIG. 23  illustrates an effect of iron concentration on Feammox. 20 mM NH 4   +  results are reported in the left filled bar of each of days 0, 5, 10 and 20 panels. 10 mM NH 4   +  results are reported in the middle dotted bar of each of days 0, 5, 10 and 20 panels. 2 mM NH 4   +  results are reported in the right open bar of each of days 0, 5, 10 and 20 panels. 
         FIG. 24  illustrates the relative ammonium removal rate constants (k) by Acidimicrobiaceae-bacteria A6 at 15° C. (top line), 20° C. (middle line) and 35° C. (lower line). 
         FIGS. 25A-25B  illustrate determination of the effect of pH on NH 4   +  consumption ( FIG. 25A ) and bacterial growth ( FIG. 25B ). pH=2 results are reported in the far left bar of each of days 0, 5, 10, 15 and 20 panels. pH=4.5 results are reported in the left middle bar of each of days 0, 5, 10, 15 and 20 panels. pH=6.5 results are reported in the right middle bar of each of days 0, 5, 10, 15 and 20 panels. pH=8 results are reported in the far right bar of each of days 0, 5, 10, 15 and 20 panels. 
         FIG. 26  illustrates a schematic representation of the genome of the Acidimicrobiaceae Feammox bacterium A6. 
         FIG. 27  illustrates the FMO activity. 
         FIG. 28  illustrates oxidation of NH 4   +  by Acidimicrobiaceae bacterium A6 when the FMO activity in the presence (left bars for each of 0, 12, 22, 30 and 37 day panels) and absence (right bars for each of 0, 12, 22, 30 and 37 day panels) of a broad enzyme inhibitor (NaS). 
         FIG. 29  illustrates a scheme of the electrogenic microbial reactor. 
         FIG. 30  illustrates the concentration of NH 4   +  after 20 days of incubation with Acidimicrobiaceae Feammox bacterium A6 in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 31  illustrates concentration of Fe(III) after 20 days of incubation with Acidimicrobiaceae Feammox bacterium A6 in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 32  illustrates the concentration of NH 4   +  after 20 days of incubation with an enrichment culture of Acidimicrobiaceae Feammox bacterium A6 in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 33  illustrates the concentration of Fe(III) after 20 days of incubation with an enrichment culture of Acidimicrobiaceae Feammox bacterium A6 in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 34  illustrates the concentration of NH 4   +  after 20 days of incubation with an enrichment culture of Acidimicrobiaceae Feammox bacterium A6 in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 35  illustrates the concentration of Fe(III) after 20 days of incubation with an enrichment culture of Acidimicrobiaceae Feammox bacterium A6 in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 36  illustrates copy number of 16S rRNA gene of Acidimicrobiaceae Feammox bacterium A6 during 20 days of incubation in the presence of elemental sulfur and different controls according to some embodiments. 
         FIG. 37  illustrates the effects of elemental sulfur additions in a continuous flow membrane Feammox reactor according to some embodiments. 
     
    
    
     DETAILED DESCRIPTION 
     Certain terminology is used in the following description for convenience only and is not limiting. The words “right,” “left,” “top,” and “bottom” designate directions in the drawings to which reference is made. The words “a” and “one,” as used in the claims and in the corresponding portions of the specification, are defined as including one or more of the referenced item unless specifically stated otherwise. This terminology includes the words above specifically mentioned, derivatives thereof, and words of similar import. The phrase “at least one” followed by a list of two or more items, such as “A, B, or C,” means any individual one of A, B or C as well as any combination thereof. 
     “Synthetic nucleic acid sequence,” “synthetic polynucleotide,” “synthetic oligonucleotide,” “synthetic DNA,” or “synthetic RNA” as used herein refers to a nucleic acid, polynucleotide, oligonucleotide, DNA, or RNA that differs from one found in nature by having a different sequence than one found in nature or a chemical modification not found in nature. The definition of synthetic nucleic acid includes but is not limited to a DNA sequence created using biotechnology tools. Such tools include but are not limited to recombinant DNA technology, chemical synthesis, or directed use of nucleases (so called “genome editing” or “gene optimizing” technologies). 
     Embodiments described herein can be understood more readily by reference to the following detailed description and examples and their previous and following descriptions. Elements and apparatus described herein, however, are not limited to the specific embodiments presented in the detailed description. It should be recognized that these embodiments are merely illustrative of the principles of the present invention. Numerous modifications and adaptations will be readily apparent to those of skill in the art without departing from the spirit and scope of the invention. 
     In one aspect, media are described herein comprising components for removal of ammonium containing contaminants. A medium comprises an ammonium containing contaminant, an iron component, an oxidant, and a Feammox bacterium and/or enzyme thereof capable of oxidizing ammonium with reduction of Fe(III) to Fe(II), wherein the oxidant regenerates Fe(III) via Fe(II) oxidation. In some embodiments, the medium is soil or water. The medium, for example, is a ground water system or wastewater. Moreover, the medium can further comprise at least one additional contaminant for removal. 
     Turning now to specific components, the medium comprises one or more ammonium containing contaminants. An ammonium containing contaminant may be, but is not limited to, an industrial, agricultural or human municipal waste. Ammonium containing contaminants, for example, can comprise fertilizers, domestic sewage, or industrial effluents. The ammonium containing contaminant may comprise ammonium chloride and/or any other ammonium salt. The ammonium containing contaminant may also be a nitrogen containing organic compound, wherein nitrogen may be hydrolyzed to ammonium. 
     The medium also comprises a Feammox bacterium and/or enzyme thereof capable of oxidizing ammonium with reduction of Fe(III) to Fe(II). The Feammox bacterium may be an Acidimicrobiaceae bacterium or a bacterium with a similar genetic composition. The Feammox bacterium may be a bacterial strain that was isolated from wetland soils collected in New Jersey after a series of enrichment incubations. The soil samples were collected at the location identified as 40° 15′ N-74° 30′ W or within 100 m of the identified location. The Feammox bacterium may be the bacterial strain designated the Acidimicrobiaceae Feammox bacterium A6 and described herein. The Acidimicrobiaceae Feammox bacterium A6 was submitted for deposit with the American Type Culture Collection (ATCC; 10801 University Blvd. Manassas, Va. 20110-2209, USA) on Apr. 27, 2015, the submission was supplemented on May 7, 2015, and was assigned Accession Deposit Number PTA-122488 on Sep. 17, 2015. The Acidimicrobiaceae Feammox bacterium may have a genome comprising, consisting essentially of, or consisting of a nucleic acid sequence with at least 70, 72, 75, 80, 85, 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, or 100% identity to SEQ ID NO: 1. The Feammox bacterium may have the genome size of 3.3 mega base pairs (Mb) and guanine-cytosine content 52%. The bacterial genome may further include a gene encoding a Feammox Ammonium Monooxygenase. As used herein, the term “Feammox Ammonium Monooxygenase” (FMO) refers to an enzyme that plays a key role in oxidizing ammonium coupled with ferric iron reduction. The FMO also refers to genes encoding clones or different variants of the Feammox Ammonium Monooxygenase. The gene may include a nucleic acid comprising, consisting essentially of, or consisting of a nucleic acid sequence with at least 70, 72, 75, 80, 85, 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, or 100% identity to a sequence selected from the group consisting of: SEQ ID NOS: 8-28. The Feammox Ammonium Monooxygenase may include an amino acid comprising, consisting essentially of, or consisting of a nucleic acid sequence with at least 70, 72, 75, 80, 85, 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, or 100% identity to a sequence selected from the group consisting of: SEQ ID NOS: 29-49. The Feammox bacterium may be live or lyophilized. 
     Determining percent identity of two nucleic acid sequences may include aligning and comparing the nucleotides at corresponding positions in the two sequences. If all positions in two sequences are occupied by identical nucleotides then the sequences are said to be 100% identical. Percent identity may be measured by the Smith Waterman algorithm (Smith T F, Waterman M S 1981 “Identification of Common Molecular Subsequences,” J Mol Biol 147: 195-197, which is incorporated herein by reference as if fully set forth). 
     As described herein, the medium may comprise one or more enzymes, such as FMO, in addition to the Feammox bacterium for the oxidation of ammonium coupled with reduction of Fe(III) to Fe(II). Alternatively, one or more enzymes, such as FMO, can be present in the medium in the absence of the Feammox bacterium. In such embodiments, the one or more enzymes can be responsible for the ammonium oxidation and/or reduction of Fe(III) to Fe(II). In some embodiments, for example, FMO is isolated from Feammox bacterium and employed in the media. In other embodiments, the one or more enzymes may be fabricated via synthetic chemical techniques. 
     The medium also comprises an iron component. In some embodiments, the iron component is a natural component of the medium. The iron component can naturally occur in soil, for example. In other embodiments, the iron component is added to the medium. The iron component can be the source of ferric ion, Fe(III), reduced to Fe(II) in conjunction with ammonium oxidation. Any iron component or source consistent with the environmental objectives of the present invention can be employed in the medium. In some embodiments, the iron component comprises iron oxide, a goethite, elemental iron, a nontronite, iron-rich clay or various mixtures thereof. Iron oxide can include hydrated forms, such as ferrihydrite. Ferrihydrite includes a dark brown or yellow brown mineral composed of about 20% (FeO 4 ) and 80% (FeO 6 ) polyhedral. The term “goethite” refers to an iron oxyhydroxide containing ferric iron. The term “nontronite” refers to the Fe(III) rich clay mineral having a typical structural formula Ca 0.5 (Si 7 Al 0.8 Fe 0.2 )(Fe 3.5 Al 0.4 Mg 0.1 )O 20 (OH) 4 . The iron component may be scrap metal, or any other source of ferric iron. The iron component can also serve as culture media for the Feammox bacterium in the medium, in some embodiments. For example, the iron component can comprise NH 4   + -ferric iron media in liquid or solid form. 
     The iron component can be present in the medium in any amount to support the oxidation of ammonium, as described herein. In some embodiments, ferric ion is present in the medium at a concentration of 1 mM to 200 mM. The concentration of ferric iron may also be from 1 mM to 2 mM, from 2 mM to 3 mM, from 3 mM to 4 mM, from 4 mM to 5 mM, from 5 mM to 6 mM, from 6 mM to 7 mM, from 7 mM to 8 mM, from 8 mM to 9 mM, from 9 mM to 10 mM, from 10 mM to 20 mM, from 20 mM to 30 mM, from 30 mM to 40 mM, from 40 mM to 50 mM, from 50 mM to 60 mM, from 60 mM to 70 mM, from 70 mM to 80 mM, from 80 mM to 90 mM, from 90 mM to 100 mM, from 100 mM to 150 mM, or from 150 mM to 200 mM. 
     An oxidant is also present in the medium, wherein the oxidant regenerates Fe(III) via oxidation of Fe(II). As discussed further below, regeneration of Fe(III) by the oxidant can conserve the Fe(III) used in the ammonium oxidation reaction and enhance or accelerate ammonium decomposition in the medium. In this way, iron is recycled in the ammonium decomposition process, and less iron is required for environmental remediation according to processes described herein. Additionally, in some embodiments, oxidation of Fe(II) by the oxidant can produce hydrogen ions. Hydrogen ions produced in the oxidation can be consumed in the ammonium oxidation reaction detailed in Equation 1 below. Accordingly, generation of hydrogen ions in the oxidation of Fe(II) can assist in maintaining a stable pH of the medium during ammonium oxidation. In some embodiments, pH of the medium is 4 to 8 or 5 to 7. 
     Subsequent to Fe(II) oxidation, the reduced oxidant may react with Fe(II) to provide one or more additional chemical species to the medium. Reaction of the reduced oxidant with Fe(II) can inhibit the accumulation of Fe(II) in the medium. In some embodiments, the reduced oxidant forms a precipitate with Fe(II). Alternatively, the chemical species formed between the reduced oxidant and Fe(II) is fully or partially soluble in aqueous-based media or water. 
     Any oxidant having the functionality of Fe(II) oxidation without interfering with ammonium oxidation processes can be employed. Suitable oxidant may be in elemental or molecular form. In some embodiments, the oxidant is elemental sulfur, S(0). Elemental sulfur can be present in the medium in any amount consistent with the environmental remediation objectives described herein. For example, elemental sulfur may be present in the medium in an amount in excess of the solubility limit of elemental sulfur in water. The amount of elemental sulfur may be in a range from 1 mg/L to 2 kg/L of the composition. The amount of sulfur may be any amount in a subrange within the range of 1 mg/L to 2 kg/L, where the subrange includes (1) a lower limit selected from 1 mg/L increments from 1 mg/L to 1.999 kg/L, and (2) a higher limit that is higher than the lower limit and selected from 1 mg/L increments from 1 mg/L to 2 Kg/L. For example, the lower limit may be 1 mg/L, 2 mg/L, 3 mg/L . . . 1.999 Kg/L, and the higher limit may be 2 mg/L, 3 mg/L, 4 mg/L . . . 2 Kg/L. The amount of elemental sulfur may be selected from any value within the range or subrange, or an endpoint of the range or subrange. 
     As described herein, the medium can comprise water, soil or mixtures thereof. The water can be any source of water, including ground water, lakes, streams and/or reservoirs. In some embodiments, the water is wastewater. As used herein, the term “wastewater” refers to any water that has been adversely affected in quality by anthropogenic influence. Wastewater may be municipal wastewater, industrial wastewater, agricultural wastewater, surface runoff, stormwater, or wastewater combining wastewater from multiple sources. Wastewater may be treated in a wastewater treatment plant. Wastewater may include nitrogen contaminants. As used herein, the term “contaminant” refers to compounds that are not occurring in water naturally, pose health or ecological risks or are subject to state and federal regulation. 
     Nitrogen contaminants may be an ammonium containing contaminant. The ammonium containing contaminant can comprise an industrial, agricultural, or human municipal waste. Ammonium containing contaminants, for example, may include fertilizers, domestic sewage, or industrial effluents. The ammonium containing contaminant may be ammonium chloride or any other ammonium salt. The ammonium containing contaminant may be a nitrogen containing organic compound, wherein nitrogen may be hydrolyzed to ammonium. 
     Similarly, soil may be any soil that has been adversely affected in quality by anthropogenic influence. The soil may include any nitrogen contaminants described herein. The soil may include groundwater. The groundwater may comprise wastewater described herein. The groundwater may contain any nitrogen contaminant described herein. 
     Water or soil medium may include at least one additional contaminant. The at least one additional contaminant may be inorganic contaminants. Inorganic contaminants may be but are not limited to heavy metals, radionuclides or trace metals. Inorganic contaminants may be copper, uranium, ferric iron, lead, zinc, arsenic, chromium, mercury or silver. The at least one additional contaminant may be organic contaminant(s). The organic contaminants can comprise chlorinated volatile organic compounds, perchloroethylene (PCE), trichloroethylene (TCE), trichloroethane, dichloroethane, vinyl chloride, polychlorinated biphenyls, fuel constituents, benzene, ethylbenzene, toluene, xylene, phenanthrene, methyl tert butyl ether, tertiary butyl alcohol, polyaromatic hydrocarbons, or ethylene dibromide. 
     In an embodiment, the ammonium containing contaminant may be added to a composition that would otherwise be low or deficient in ammonium when reactions in addition to or in place of ammonium oxidation are of interest. 
     In some embodiments, the medium may further comprise a carrier. The carrier may support growth of the Feammox bacterium. The carrier may comprise a filter, beads, agarized medium, or any surface that allows bacterial attachment. The carrier may include media for culturing the Feammox bacterium. The media may be inorganic NH 4   + -ferric iron media. The inorganic NH 4   + -ferric iron media may be solid media or liquid media. The liquid media may include but not limited to the following components: NH 4 Cl, (NH 4 ) 2 SO 4 , NaHCO 3 , KHCO 3 , KH 2 PO 4 , 100 mg MgSO 4 .7H 2 O, and CaCl 2 .2H 2 O. The liquid media may further include ferrihydrite, AQDS, trace element solution or vitamins. Vitamins may be but are not limited to ATCC® vitamins. The liquid media may have a pH in a range from 4.0 to 5.0. The media may include traces of dissolved oxygen. The solid medium may have the same composition as the liquid media but include elements to solidify the mixture. The solid media may be solidified with 0.8% agar. The solid media may include ferrihydrite that is spread on the surface of the medium. 
     In another aspect, systems for environmental remediation are provided. A system, for example, comprises a reactor including a medium comprising an ammonium containing contaminant, an iron component, an oxidant, and a Feammox bacterium and/or enzyme thereof capable of oxidizing ammonium with reduction of Fe(III) to Fe(II), wherein the oxidant regenerates Fe(III) via Fe(II) oxidation. In some embodiments, the reactor comprises an inlet and outlet for the medium, such as water and/or soil. The reactor, for example, can be operated continuously or in a batch mode. Components of the medium, including the ammonium containing contaminant, iron component, oxidant, and Feammox bacterium and/or enzyme thereof can have any properties and/or compositions described hereinabove. In some embodiments, the medium can comprise at least one additional contaminant. Additional contaminants can have any composition described hereinabove. Moreover, the medium can comprise water and/or soil. Water of the system can be any source of water, including wastewater, ground water, lakes, streams and/or reservoirs. 
     The reactor may be a continuous membrane reactor or a sequential batch reactor. In a non-limiting example the continuous membrane reactor may be a reactor illustrated in  FIG. 11 .  FIG. 11  illustrates a scheme of a membrane reactor for NH 4   +  oxidation via Feammox. Referring to  FIG. 11, 1  refers to the feed solution,  2  refers to the feed pump,  3  refers to the membrane module,  4  refers to the floater connected to an electrical on/off switch,  5  refers to the ceramic diffuser,  6  refers to the N 2  supplier,  7  refers to the water bath,  8  refers to outflow, and  9  refers to the outflow pump. The reactor may be an electrogenic microbial reactor. The electrogenic microbial reactor may be any bioelectrochemical system that extracts energy from a substrate (Call and Logan 2011  Biosen. Bioelectron.  26(11): 4526-4531, which is incorporated herein by reference as if fully set forth). The electrogenic microbial reactor may be any bioelectrochemical system that extracts energy from a substrate (Call and Logan 2011  Biosen. Bioelectron.  26(11): 4526-4531, which is incorporated herein by reference as if fully set forth). In the bioelectrochemical system, electrons may be harvested biologically, and then transferred to the anode that functions as the terminal electron acceptor for the microorganisms in the system, and H 2  is produced at the anode. The electrogenic microbial reactor may be a Microbial Fuel Cell (MFC) or Microbial Electrolysis cell (MEC). A non-limiting example of the electrogenic microbial reactor is illustrated in  FIG. 29 . Referring to  FIG. 29 , the reactor includes a tank, a graphite anode connected via titanium wire to the positive terminal of the power supply, a stainless steel cathode connected via stainless steel wire to the negative terminal of the power supply. MECs require a small potential applied from an external power source (E AP &gt;0.25 V), resulting in H 2  production at the anode (Logan, Hamelers et al. 2006  Environ. Sci. Technol.  40(17):5181-5192; Call and Logan 2008  Environ. Sci. Technol.  42(9):3401-3406; Call and Logan 2011, all of which are incorporated by reference herein as if fully set forth). In an embodiment, a reactor may be an industrial-type reactor. The reactor may operate within a water treatment plant. The reactor may be a treatment pond or a reservoir. The reactor may be a tank for wastewater storage. 
     Reactor conditions may include a temperature in a range from 4° C. to 35° C. The temperature may be in a range between any two integer value temperatures selected from 4° C. to 35° C. The temperature may be in a range between and including 4° C. to 10° C., 10° C. to 15° C., 15° C. to 20° C., 20° C. and 25° C., 25° C. and 30° C., 30° C. and 35° C. The temperature may be any one integer value temperature selected from those including and between 4° C. and 35° C. or 15° C. to 35° C. Temperatures between room temperature and 35° C. may be used. The temperature may be any one temperature including and between room temperature and 35° C. Temperatures between 20° C. and 35° C. may be used. The temperature may be any temperature including and between 20° C. and 25° C. 
     The reactor may be operated for a period of time ranging from 2 hours to 45 days. The time period may be 5 hours, 10 hours, 15 hours, 20 hours, 1 day, 2 days, 3 days, 4 days, 5 days, 10 days, 15 days, 20 days, 25 days, 30 days, 35 days, 40 days or 45 days. The time period may be any one integer value selected from those including and between value points, endpoints inclusive. The time period may be greater than 45 days. The time period may be less than 1 day. In continuous flow reactors or in batches, the process may last from several hours to several months. For continuous flow reactors, the time period may depend on the bacterial concentration in the inoculum. Higher bacterial concentration in the inoculum may result in a shorter remediation time. The time period may depend on hydraulic retention capacity of a continuous flow reactor. Lower retention capacity of the continuous flow reactor may result in a shorter remediation time. Hydraulic residence time for the continuous flow reactors may be from 3 hours to 4 hours, from 3 hours to 5 hours, from 3 hours to 6 hours, from 3 hours to 7 hours, from 3 hours to 8 hours, from 3 hours to 10 hours, from 3 hours to 15 hours, from 3 hours to 20 hours, from 3 hours to 1 day, from 3 hours to 2 days, from 3 hours to 3 days. Hydraulic residence time may be any integer value selected from those including and between value points, endpoints inclusive. 
     pH of the medium in the reaction can range from 2.0 to 8.0. The pH of the medium may be in a range between and including 2.0 and 3.0, 3.0 and 4.0, 4.0 and 5.0, 5.0 and 6.0, 6.0 to 7.0, 7.0 to 7.5. The pH may be any one integer value pH selected from those including and between 2.0 and 7.5. The pH may be any pH including and between 4.0 and 7.0. 
     In some embodiments, the reactor and associated processes may have nitrification and denitrification phases. The process may include a nitrification phase followed by a denitrification phase. The nitrification and denitrification phases may be performed in parallel. The parallel performance of nitrification and denitrification phases may occur at low levels of oxygen. The nitrification and denitrification phases may be performed in the same reactor. The reactor utilized in the process may be configured to allow a nitrification phase and a denitrification phase. There may be two separate reactors for each of the nitrification and denitrification phases. The process may further include adding Anammox bacteria to the reactor. The nitrification phase may be performed by the Feammox bacteria. In the nitrification phase, ammonium may be converted to nitrite. The denitrification phase may be performed by denitrifying bacteria. In the denitrification phase, nitrite may be converted to gaseous nitrogen (N 2 ). The denitrification phase may be performed by the Anammox bacteria. 
     In another aspect, methods of environmental remediation are described herein. A method comprises providing a medium including one or more ammonium containing contaminants and disposing a Feammox bacterium and/or enzyme thereof in the medium. The Feammox bacterium and/or enzyme thereof participates in the oxidation of the ammonium coupled with reduction of Fe(III) to Fe(II). An oxidant in the medium subsequently regenerates Fe(III) via Fe(II) oxidation. In some embodiments, oxidation of Fe(II) by the oxidant generates hydrogen ions that are consumed in the ammonium oxidation. Additionally, in some embodiments, the oxidant forms a compound with Fe(II) in the medium, as described hereinabove. The compound may be a precipitate, in some embodiments. Components of the medium, including the ammonium containing contaminant, iron component, oxidant, and Feammox bacterium and/or enzyme thereof can have any properties and/or compositions described hereinabove. In some embodiments, the medium can comprise at least one additional contaminant. Additional contaminants can have any composition described hereinabove. Moreover, the medium can comprise water and/or soil. Water can be of any source, including wastewater, ground water, lakes, streams and/or reservoirs. 
     In a non-limiting example, the oxidant can be element sulfur, S(0). Elemental sulfur oxidizes Fe(II) to regenerate Fe(III). The regenerated Fe(III) can subsequently participate in Feammox reactions occurring in the medium. The oxidation of Fe(II) by elemental sulfur can also produce hydrogen ions. The hydrogen ions may be consumed in Feammox reactions occurring in the medium as provided in Equation 1 below. The production of hydrogen ions can assist in maintaining a stable pH of the medium. Additionally, the regeneration of Fe(III) can reduce the iron content required for sufficient ammonium oxidation and/or removal of other contaminants from the medium. In reduced form, the elemental sulfur can be present as sulfide. The sulfide can react with Fe(II) to precipitate iron sulfide (FeS). Reaction of the reduced oxidant with Fe(II) inhibits accumulation of Fe(II) in the media. As shown in the examples below, presence of the oxidant can substantially enhance ammonium decomposition rates. While not wishing to be bound by any theory, the overall reaction scheme involving elemental sulfur oxidant, S(0), is presented in equations (1-4): 
     Oxidation of ammonium by Feammox bacterium and/or enzyme(s) thereof: 
       3Fe 2 O 3 0.5H 2 O+NH 4   + +10 H + →NO 2   − +6 Fe 2+ +8.5 H 2 O  (1)
 
     Oxidation of Fe 2+  by S(0): 
       2Fe 2+ +S+3.5 H 2 O→Fe 2 O 3 0.5H 2 O+HS − +5H +   (2)
 
       Precipitation of FeS: 
       Fe 2+ +HS − →FeS+H +   (3)
 
       Overall Reaction: 
       Fe 2 O 3 .0.5H 2 O+NH 4   + →NO 2   − +2 FeS+1.5 H 2 O+2H +   (4)
 
     Accordingly, with proper oxidant, a redox cycle can be established for enhancing ammonium oxidation and/or decomposition and removal of other contaminants from the media, while conserving Fe(III). 
     Methods of environmental remediation described herein may occur in low levels of oxygen or in the absence of oxygen. In some embodiments, methods may include removing oxygen. As used herein, “absence of oxygen” may include a complete lack of oxygen, low levels of oxygen or oxygen levels below detection. Absence of oxygen may include low oxygen concentrations that allow for iron reduction. Absence of oxygen fir example, may be 2 mg/l of dissolved oxygen or less. Absence of oxygen may be 0.5 mg/l of dissolved oxygen or less. Low levels of oxygen may be created by organisms degrading organic carbon when oxygen is consumed by organisms degrading organic carbon, and no or insufficient aeration is provided to compensate for low levels of oxygen. The process may include maintaining low levels of oxygen. 
     In another aspect, various compositions are described herein. In some embodiments, a composition comprises an Acidimicrobiaceae Feammox bacterium A6 having Accession Deposit Number PTA-122488, at least one of soil, wastewater, and a carrier, and elemental sulfur. The bacterium is capable of oxidizing ammonium coupled with reduction of Fe(III) to Fe(II). In other embodiments, a composition comprises at least one enzyme capable of oxidizing ammonium into nitrite, at least one of soil, wastewater, and a carrier, and elemental sulfur. The soil or wastewater comprises an ammonium containing contaminant, and the at least one enzyme comprises a sequence with at least 70% identity to the sequence selected from the group consisting of SEQ ID NOS: 29-49. 
     In another aspect, systems employing the various compositions are provided. In some embodiments, a system comprises a reactor and a composition that includes an Acidimicrobiaceae Feammox bacterium A6 having Accession Deposit Number PTA-122488, at least one of soil, wastewater and a carrier, and elemental sulfur. The bacterium is capable of oxidizing ammonium coupled with reduction of Fe(III) to Fe(II). 
     In another aspect, processes for reducing a nitrogen contaminant from soil and/or water are described herein. A process, in some embodiments, comprises mixing the wastewater with an Acidimicrobiaceae Feammox bacterium A6 having Accession Deposit Number PTA-122488 to form a mixture. The process also comprises adding elemental sulfur to the mixture. In some embodiments, the water can be wastewater or water from a ground water system. 
     In a further aspect, various hosts are provided including nucleic acids comprising a sequence with at least 70% identity to a reference sequence selected from the group consisting of SEQ ID NOS: 8-28. Additionally, compositions comprising such hosts are also contemplated. A composition, for example, can comprise one or more hosts, at least one or soil, wastewater, and a carrier and elemental sulfur. The soil or wastewater can comprise an ammonium containing contaminant. 
     In some embodiments, a synthetic nucleic acid encodes an enzyme capable of oxidizing ammonium coupled with iron reduction. The enzyme may be Feammox Ammonium Monooxygenase (FMO). The synthetic nucleic acid may comprise consists essentially of, or consists of a sequence with at least 70, 72, 75, 80, 85, 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, or 100% identity to a reference sequence selected from the group consisting of: SEQ ID NOs: 8-28. 
     Additionally, expression cassettes are provided that include any synthetic nucleic acid described herein. An expression cassette, for example, may include the synthetic nucleic acid encoding the FMO. The expression cassette may be introduced into a vector. Suitable vectors may be cloning vectors, transformation vectors, expression vectors, or virus-based vectors. The expression cassette portion of a vector may further include a regulatory element operably linked to a synthetic nucleic acid encoding the FMO. In this context, operably linked means that the regulatory element imparts its function on the synthetic nucleic acid. For example, a regulatory element may be a promoter, and the operably linked promoter would control expression of the synthetic nucleic acid. 
     Expression of a synthetic nucleic acid encoding the FMO from the expression cassette may be under the control of a promoter, which provides for transcription of the synthetic nucleic acid in a host. The promoter may be a constitutive promoter or, tissue specific, or an inducible promoter. A constitutive promoter may provide transcription of the nucleic acid throughout most cells and tissues of the host and during many stages of development but not necessarily all stages. An inducible promoter may initiate transcription of the synthetic nucleic acid sequence only when exposed to a particular chemical or environmental stimulus. A tissue specific promoter may be capable of initiating transcription in a particular host tissue. The promoter may provide transcription of a synthetic nucleic acid having a sequence with at least 70, 72, 75, 80, 85, 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, or 100% identity to a reference sequence selected from the group consisting of SEQ ID NOs: 8-28 and expression of the FMO that is capable of oxidizing ammonium coupled with iron reduction. 
     In some embodiments, any one of the vectors or expression cassettes described herein may be introduced to a host. The host can comprise a bacterium, plant, algae, or yeast. An embodiment includes a host herein comprising any one of the vectors or expression cassettes described herein. 
     The following non-limiting examples are provided to illustrate particular embodiments. The embodiments throughout may be supplemented with one or more detail from one or more example below, and/or one or more element from an embodiment may be substituted with one or more detail from one or more example below. 
     Example 1. Development of an Enrichment Culture Capable of Ammonium Oxidation Under Iron Reducing Conditions 
     An anaerobic NH 4   +  oxidation process coupled to iron reduction was first noted in a forested riparian wetland in New Jersey. In this reaction, NH 4   +  is the electron donor, which is oxidized to nitrite (NO 2   − ), and ferric iron [Fe(III)] is the electron acceptor, which is reduced to ferrous iron [Fe(II)]. The stoichiometry and change in free energy when ferrihydrite is the Fe(III) source is: 
       3Fe 2 O 3 .0.5H 2 O+10H + +NH 4   + →6Fe 2+ +8.5H 2 O+NO 2   − (ΔG r ≤−145.08 kJ mol −1 )  (Equation 1)
 
     These pathways have been reported to oxidize NH 4   +  to NO 2   − , to NO 3   − , or directly to N 2 , using Fe(III) as electron acceptor (Clement et al., 2005; Shrestha et al., 2009; Sawayama, 2006; Yang et al., 2012, all of which are incorporated by reference as if fully set forth). 
     Soil samples were collected from the same location and used for laboratory incubation experiments as well as to set up an enrichment system for Feammox in a continuous flow membrane reactor. Various incubation conditions [Fe(III) sources, inorganic carbon content, NH 4   +  concentration,  15 NH 4   + , and acetylene gas (C 2 H 2 ) as a selected inhibitor] were used to study the Feammox mechanism. Molecular biology methods, such as denaturing gradient gel electrophoresis (DGGE), 454 pyrosequencing, and real-time quantitative PCR (qPCR) analysis were used to investigate the bacterial community change during incubations. Production of both nitrite (NO2-) and ferrous iron were measured repeatedly during incubations when soil slurries were supplied with iron oxide (ferrihydrite or goethite) and ammonium chloride. 
     The Feammox process provided denitrifiers and anammox bacteria with the necessary NO2- under this anaerobic incubation, and achieved total nitrogen loss via denitrification and anammox pathways. Therefore, Feammox is an important process in the nitrogen cycle in soil environments under oxygen limited conditions, and reveals a new linkage between these two significant biogeochemical cycles (iron and nitrogen cycle). 
     Example 2. Sample Collection and Processing 
     Soils for all the experiments described in examples herein were taken from a temperate forested riparian wetland at the Assunpink Wildlife Management Area, New Jersey. Ten soil cores were collected from 10 cm below the surface with polyethylene column containers (8 cm diameter and 30 cm long) and transported to the laboratory within 2 hours. The soil pH was between 3.5 and 4.5, and no manganese oxides were detected. The detailed physicochemical characteristic of these wetland soils have been described elsewhere (Clement et al., 2005 Soil Biol Biochem 37: 2323-2328, which is incorporated by reference as if fully set forth). Prior to all incubation experiments, soil slurry from the field site was aerated for a month to degrade much of the labile organic carbon. After a 30 days of aeration, the dissolved organic carbon (DOC) content was stable at 2.06±0.20 mg g −1 . Following the aeration treatment, the soil was divided into 400×10 g (air-dry equivalent) subsamples, and added into 50 mL serum vials, with 30 mL deionized water. The soil slurries were purged thoroughly with a CO 2 :N 2  (80:20) mixture, resulting in a final pH of 4 to 4.5. The vials were sealed tightly with rubber stoppers and were stored in an anaerobic glove box for 30 days at ambient temperature to allow for stabilization before starting the incubations. 
     Example 3. Batch Incubation Experiments 
     All incubations, addition of reagents, and sampling were conducted in an anaerobic glove box with a solution of resazurin as the redox indicator. Soil samples were first incubated with different Fe(III) sources to determine which source would yield a more active Feammox process: 6-line ferrihydrite (Fe 2 O 3 .0.5H 2 O) or goethite [FeO(OH)]+NH 4   +  addition; ferric chloride+NH 4   +  addition; ferric citrate+NH 4   +  addition; either only ferrihydrite or NH 4   +  addition; and autoclaved soil with ferrihydrite+NH 4   +  addition (n=30 per treatment). 6-line ferrihydrite (Fe 2 O 3 .0.5H 2 O) or goethite [FeO(OH)] was prepared according to Cornell and Schwertmann, 2003 The Iron Oxides: Structure, Properties, Reactions, Occurrences, and Uses. John Wiley and Sons Ltd., which is incorporated herein by reference as if fully set forth. pH was adjusted to 4.5 in the ferrihydrite/goethite augmented samples, and to between 3.5˜4.0 in the ferric chloride/citrate augmented samples. Soil-slurry samples, which were prepared to have an initial concentration of 12.0 mmol L −1  Fe(III) and/or 2.00 mmol L −1  NH 4   + , were incubated in a series of 50 ml vials with an oxygen-free headspace, created by purging with a CO 2 :N 2  (80:20) mixture. Triplicate samples were collected destructively every two days to analyze iron and nitrogen species. 
     The second incubation was conducted to extend the anoxic incubation with ferrihydrite to 180 days, with repeated NH 4 Cl additions after the Nile in solution was exhausted. The initial concentration of Fe(III) was 25.0 mmol L −1  and 1.00 mmol L −1  NH 4   +  was added on days 4, 24, and 60, furthermore, 0.20 mmol L −1 NaHCO 3  was added on day 50 and day 90 of the incubation. On day 125, incubation vials were divided into two sets to study the effect of different inorganic carbon contents on Feammox. Either 1.20 mmol L −1  or 0.20 mmol L −1  of NaHCO 3  plus 2 mmol L −1  of NH 4 Cl were added to each set. NaHCO 3  was then added every 10 days, which increased the soil pH to ˜5 in the samples amended with 1.20 mmol L −1  of NaHCO 3 . For this incubation, samples were collected every four days. Finally, soil samples collected on day 180 of the incubations were used to enrich the Feammox bacteria in a membrane reactor. To study how the organic carbon content affects the Feammox bacteria, 1.00 mmol L −1  sodium citrate was also supplied on day 125 to four of the 1.20 mmol L −1  NaHCO 3  amended samples. 
     In the third experiment, inorganic nitrogen species were quantified through incubations in the presence of C 2 H 2 . Soil slurries were first incubated for 90 days in eighty 50 mL vials. The Fe(III) concentration at the beginning of the incubations was 25 mmol L −1 . One mmol L −1  NH 4 Cl and 0.20 mmol L −1 NaHCO 3  was added on days 24, 60, and 90. After this incubation, 5 mL of pure C 2 H 2  gas were added to 40 vials, which resulted in a finial C 2 H 2  concentration of 100 L −1 . Samples with and without C 2 H 2  were then incubated anaerobically for 20 days. The headspace gas was sampled every 24 hours for N 2 O analysis, and soil samples were analyzed every two days for Fe and N species. 
     Example 4. Continuous Flow Membrane Feammox Reactor 
     Soil samples collected on day 180 from the incubation with ferrihydrite, NH 4 Cl, and 1.20 mmol L −1  NaHCO 3  additions were inoculated into a continuous flow membrane reactor, which was operated under anaerobic conditions by constantly purging N 2  through the reactor&#39;s headspace at a room temperature (25° C.), and with a 48 hour hydraulic retention time (Abbassi et al., 2014  J. Environ. Management  142: 53-59, which is incorporated herein by reference as if fully set forth). 
     The enrichment medium contained the following components per liter: 177 mg NH 4 Cl, 77.9 mg (NH 4 ) 2 SO 4 , 19.8 mg NaHCO 3 , 71.0 mg KHCO 3 , 9.00 mg KH 2 PO 4 , 100 mg MgSO 4 .7H 2 O, and 60.0 mg CaCl 2 .2H 2 O. After autoclaving, 1 mL trace element solution was added to the medium (Van de Graaf et al., 1996  J. Microbiol.,  142:2187-2196, which is incorporated herein by reference as if fully set forth). 50.0 mmol L −1  ferrihydrite were added once every two weeks directly into the reactor. To aid in maintaining anaerobic conditions, 0.10-0.20 mmolL −1  sodium citrate was fed to the reactor about twice per month. pH was controlled at around 4˜5, and dissolved oxygen was &lt;0.10 mg/L. Samples form the outflow were collected every two days, and sludge samples from reactor were collected and kept at −20° C. for molecular biology analysis. 
     Finally,  15 N isotope tracer incubations were conducted using slurries collected form the stable Feammox membrane reactor. Five treatments (n=3 per treatment) were conducted: (1) control with only anoxic deionized (DI) water; (2) 15 NH 4 Cl addition; (3)  15 NH 4 Cl+Fe(III) addition; (4) 15 NH 4 Cl and C 2 H 2  addition; (5) 15 NH 4 Cl, C 2 H 2 , and Fe(III) addition. The headspace gas of each 50 mL incubation vial was sampled every 24 hours for  15 N 2 O analysis. 
     Example 5. Chemical Analyses 
     For each sample collection during the incubations, a set of vials was destructively sampled in a glove box under oxygen-free conditions and the pH was measured immediately using a pH electrode. An extraction with 0.5N HCl was conducted for 24 hours at room temperature to determine acid-extractable Fe(II) and NH 4   +  concentrations in the soils. Fe(II) was analyzed using the ferrozine assay method (Stookey, 1970 Anal Chem 42: 779-781; Komlos et al., 2007 Water Res 41: 2996-3004, which are incorporated herein by reference as if fully set forth). Extraction efficiency of Fe(II) was affected by the HCl concentration and the extraction time. About 5-10% more Fe(II) could be extracted with either 1N HCl extraction over 24 hours or with 0.5N HCl over 36 hours as opposed to 0.5N HCl over 24 hours. Furthermore, after more Fe(II) was produced in the system with increasing incubation time, the Fe(II) extraction efficiency improved. Only a 1-2% difference was observed in the Fe(II) extracted over 24 hours using 0.5N vs. 1N HCl towards the end of the incubation period. Clays, present in the soil incubations, typically sorb Fe(II) more efficiently when the total Fe(II) is low, furthermore ferrihydrite is slowly converted to magnetite, resulting in relatively different associations to different phases of the Fe(II) over the duration of the incubation. All of which leads to incomplete Fe(II) extractions, especially when the Fe(II) is low. Fe(II) data obtained herein via 0.5N HCl extractions over 24 hours to ensure that the methods and hence data are comparable to those reported by other researchers focusing on iron reduction and iron bioavailability. 
     NH 4   +  was analyzed using a Dionex™ Ion Chromatograph (LC3000) with a CS-16 Column and a CS-16 guard column (flow rate=1.00 mL min −1 , detection limit=0.012 ppm). NO 3   −  and NO 2   −  were extracted with DI water for 1 hour anaerobically, and measured via Ion Chromatography, using an AS-22 Column along with an AG-22 guard column (flow rate=1.20 mL min −1 , detection limit=0.016 ppm). For the total organic carbon (TOC) and total nitrogen (TN) analyses a Shimadzu TOC-5000(A) was used. N 2 O concentrations were determined on a gas chromatograph Shimadzu 2014 equipped with an electron capture detector. 
     Example 6. DNA and RNA Isolation 
     DNA and RNA samples were extracted from soils collected at the wetland prior to any laboratory incubation, from the samples taken at different time points during the incubation experiments and from the reactor. DNA was extracted from 500 mg soil or sludge samples using the FastDNA® spin kit for soil (MP Biomedicals, USA) as described by the manufacturer, and RNA using the FastRNA® pro Soil Direct Kit. The concentrations were measured using a Nano-drop 2000 spectrophotometer (Thermo Scientific, USA). 
     Example 7. PCR-DGGE and 454 Pyrosequencing Analysis 
     Bacterial universal 16S rRNA gene primer sets V3-2/V3-3 were used for PCR amplification (Jensen et al., 1998 FEMS Microbiol Ecol 26: 17-26, which is incorporated herein by reference as if fully set forth). DGGE was performed with an 8% polyacrylamide gel containing a gradient from 40% to 80% denaturant using the gradient gel electrophoresis system (C.B.S. SCIENTIFIC, USA). The electrophoresis was carried out at 60 V for 15 hours. After that the gel was stained with 0.1 μL mL −1  SYBR Green I and visualized with an UV transilluminator. All visible bands were excised from the gel and used as templates for re-amplification, using the primer set V3-1/V3-2 and followed by cloning (Jensen et al., 1998, which is incorporated herein by reference as if fully set forth). PCR products were purified via agarose gel extraction and cloned into a pGEM-T vector (Promega). A total of 10 to 30 positive recombinant clones for each band were identified by colony PCR, and were sent for sequencing to avoid erroneous interpretations. DNA sequencing was then conducted by Genewiz, Inc. Bacteria were classified and the phylogenetic tree of Acidimicrobiaceae-related sequences was constructed using the Bayesian inference (Huelsenbeck et al., 2001 Science, 294:2310-2314, which is incorporated herein by reference as if fully set forth). Sequences obtained in this study were submitted to the GanBank database on Feb. 4, 2013, and are available therein under accession numbers KC581755-KC581779. See also Huang S and Jaffe P R,  Characterization of incubation experiments and development of an enrichment culture capable of ammonium oxidation under iron reducing conditions,  2014, Biogensciences Discuss, 11, 12295-12321, which is incorporated herein by reference as if fully set forth. To further confirm the changes in the bacterial community, 454 pyrosequencing was performed with samples collected from the incubation on days 0, 30, 90, 160 and from the membrane reactor after 150 days of reactor operation. Domain-specific primers Bact-338F1/909R, targeting the V3-V5 region of the 16S rDNA of bacteria were amplified and sequenced according to Pinto et al. (2012, PLoS One 7: 43093, which is incorporated herein by reference as if fully set forth). 
     Example 8. Quantitative PCR (qPCR) Assay 
     qPCR experiments were carried using a StepOnePlus™ Real-Time PCR System (Life Technologies, USA), represented by 16S rRNA genes, using primer sets 1055f/1392r for total bacteria (Harms et al., 2003), Amx368f/Amx820r for anammox bacteria (Schmid et al., 2000; Schmid et al., 2003), acd320f-432r which were developed for Acidobacteriaceae bacteria, and acm342f-439r which were developed for Acidimicrobiaceae bacteria. See Harms et al. 2003 Environ Sci Technol 37: 343-351, for total bacteria; a Schmid et al., 2000 Syst Appl Microbiol 23:93-106, and Schmid et al., 2003 Syst Appl Microbiol 26:529-538 for anammox bacteria. For the detection of denitrifiers, AOB and AOA, denitrifying functional genes (nirS and nirk), ammonia monooxygenase structural gene (amoA) were quantified with primer sets NirS3F/NirS5R, NirK1F/NirK5R, amoA-1F/amoA-2R for AOB-amoA and Arch amoA-F/amoA-R for AOA-amoA (Braker et al., 1998 Appl Environ Microbiol 64:3769-3775; Rotthauwe et al., 1997 Environ Microbiol 9:1761-1771; Francis et al., 2005 Proc. Natl. Acad. Sci. 102:14683-14688, all of which are incorporated by reference herein as if fully set forth). Primer pairs CrenamoA23f/616r, was also used to quantify the thaumarchaeal amoA genes which represented acidophilic ammonia oxidizers (Tourna et al., 2008  Environ Microbiol  10: 1357-1364, which is incorporated herein by reference as if fully set forth). For DNA quantification, each qPCR mixture (20 μL) was composed of 10 μL of SYBR Premix Ex Taq® II (Takara, Japan), 0.8 μL 10 μM of each primer, and ˜10 ng DNA template. RNA quantification was conducted through a real-time quantitative reverse transcription-PCR (RT-qPCR) analysis, by using the One Step SYBR® PrimeScript® RT-PCR Kit (Takara, Japan) according to the manufacturer&#39;s recommendations. Thermal cycling conditions for total 16S rDNA, nirS and AOB-amoA gene numbers was initiated for 30 s at 94° C., followed by 40 cycles of 5 s at 94° C., 30 s at 57° C., and 30 s at 70° C. 16S rDNA numbers of anammox, Acidobacteriaceae and Acidimicrobiaceae bacteria were performed at 56° C., 55° C., and 58° C. as annealing temperature respectively, with the same program. For AOB-amoA gene and thaumarchaeal amoA genes, annealing temperature was 53° C. and 55° C., and the annealing time was adjusted to 45 s. For RNA quantification, the cycling conditions were identical to those described for measuring gene numbers, with the exception that an initial incubation was conducted for 5 min at 42° C. to facilitate reverse transcriptase activity. Each assay contained a standard using a serial dilution of plasmids containing specific target genes, independent triplicate templates for each soil sample, and triplicate no template controls (NTC). 
     Example 9. Thermodynamic Consideration of Feammox 
     The change in Gibbs free energy of Equation 1 was calculated to determine the thermodynamic feasibility of the Feammox reactions using the following equation 
     
       
         
           
             
               
                 a 
                  
                 A 
               
               + 
               bB 
             
             -&gt; 
             
               cC 
               + 
               
                 d 
                  
                 D 
               
             
           
         
       
       
         
           
             
               Δ 
                
               
                 G 
                 r 
               
             
             = 
             
               
                 Δ 
                  
                 
                     
                 
                  
                 
                   G 
                   r 
                   0 
                 
               
               + 
               
                 RT 
                  
                 
                     
                 
                  
                 ln 
                  
                 
                   
                     
                       
                         ( 
                         C 
                         ) 
                       
                       c 
                     
                      
                     
                       
                         ( 
                         D 
                         ) 
                       
                       d 
                     
                   
                   
                     
                       
                         ( 
                         A 
                         ) 
                       
                       a 
                     
                      
                     
                       
                         ( 
                         B 
                         ) 
                       
                       b 
                     
                   
                 
               
             
           
         
       
       
         
           
             
               and 
                
               
                 : 
               
                
               
                   
               
                
               Δ 
                
               
                   
               
                
               
                 G 
                 r 
                 0 
               
             
             = 
             
               
                 c 
                  
                 
                     
                 
                  
                 Δ 
                  
                 
                     
                 
                  
                 
                   G 
                   
                     f 
                      
                     C 
                   
                   0 
                 
               
               + 
               
                 d 
                  
                 Δ 
                  
                 
                   G 
                   
                     f 
                      
                     D 
                   
                   0 
                 
               
               - 
               
                 a 
                  
                 Δ 
                  
                 
                   G 
                   
                     f 
                      
                     A 
                   
                   0 
                 
               
               - 
               
                 b 
                  
                 Δ 
                  
                 
                   G 
                   
                     j 
                      
                     B 
                   
                   0 
                 
               
             
           
         
       
     
     R is the gas constant, which equals 0.008314 kJ mol −1 . K, and T is the absolute temperature in ° Kelvin (297.15 K). Free energies of formation were obtained from Stumm and Morgan (1996): ΔG ƒ   0  (NH 4   + )=−79.37 kJ mol −1 , ΔG ƒ   0  (NO 2   − )=−37.2 kJ mol −1 , ΔG ƒ   0  (H 2 O)=−237.18 kJ mol −1 , ΔG ƒ   0  (Fe 2+ )=−78.87 kJ mol −1 . ΔG ƒ   0  (Fe 2 O 3 .0.5H 2 O)=−711 kJ mol −1  (Stumm and Morgan 1996 Aquatic Chemistry: Chemical Equilibria and Rates in Natural Waters (John Wiley, New York); Majzlan et al., 2004 Geochim. Cosmochim. Acta. 68, 1049-1059, which are incorporated herein by reference as if fully set forth). For biogeochemical reactions involving H+, requires converting from standard condition (pH=0) to biochemical conditions: ΔG 0 ′=ΔG 0 +mΔG ƒ ′ (H + ), where in is the net number of H +  in the reaction and ΔG ƒ ′ (H+) is calculated as −5.69 kJ mol −1  per pH unit (Madigan et al., 2002  Brock Biology of Microorganisms,  10 th  ed. Appendix 1: energy calculations in microbial bioenergetics, which is incorporated by reference herein as if fully set fort). The chemical activity values used in the calculation are based on our incubation experiments: C NH     4       +   =2 mmol L −1 , C NO     2       −   =10 μmol L −1 , C Fe     2+   ≤0.01 μmol L (detection limit), respectively, and pH=4.0. The dissolved Fe(II) was below the ferrozine method detection limit in the solution due to its sorption onto the Fe(III) oxides. Measurable dissolved Fe was only present in the samples extracted with 0.5M HCl. An activity of 1 was used for the solid-phase Fe(III) oxide minerals, and water. 
     
       
         
           
             
               
                 
                   
                     
                       
                         3 
                          
                         
                           
                             Fe 
                             2 
                           
                           · 
                           
                             O 
                             3 
                           
                           · 
                           0.5 
                         
                          
                         
                           H 
                           2 
                         
                          
                         O 
                       
                       + 
                       
                         10 
                          
                         
                           H 
                           + 
                         
                       
                       + 
                       
                         N 
                          
                         
                           H 
                           4 
                           + 
                         
                       
                     
                     → 
                     
                       
                         6 
                          
                         
                           Fe 
                           
                             2 
                             + 
                           
                         
                       
                       + 
                       
                         8.5 
                          
                         
                           H 
                           2 
                         
                          
                         O 
                       
                       + 
                       
                         NO 
                         2 
                         - 
                       
                     
                   
                    
                   
                     
 
                   
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                         r 
                       
                     
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                         [ 
                         
                           
                             6 
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                               G 
                               
                                 fFe 
                                 
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                               0 
                             
                           
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                             8.5 
                              
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                                 4 
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                               0 
                             
                           
                         
                         ] 
                       
                       + 
                       
                         
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                             8 
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                              
                             kJ 
                              
                             
                                 
                             
                              
                             
                               mol 
                               
                                 - 
                                 1 
                               
                             
                           
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                          
                         
                           ( 
                           
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                              
                             
                               
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                                     + 
                                   
                                 
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                        
                       
                         
 
                       
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                           ( 
                           
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                              
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                              
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                              
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                              
                             
                                 
                             
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                               mol 
                               
                                 - 
                                 1 
                               
                             
                           
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                          
                         
                           ( 
                           
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                        
                       
                           
                       
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                         14 
                       
                        
                       
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                         . 
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                        
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                        
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                        
                       
                           
                       
                        
                       
                         mol 
                         
                           - 
                           1 
                         
                       
                     
                   
                 
               
               
                 
                   ( 
                   
                     Equation 
                      
                     
                         
                     
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                     1 
                   
                   ) 
                 
               
             
           
         
       
     
     The ≤ sign is because an upper limit (detection limit) was used for the Fe(II) concentration. 
       FIG. 10  illustrates a graph of ΔG vs. pH. Referring to this figure, pH shows that when maintaining all species concentrations constant except H + , Feammox should not be feasible when the pH is above 6.5. Hence, Feammox is expected to occur in acidic environments. 
     Example 10. PCR Amplification, DGGE Analysis and Pyrosequencing 
     Bacterial universal 16S rRNA gene primer sets V3-2/V3-3 and 27f/519r were used for PCR amplification (Jensen et al., 1998; Lane, 1991, both of which are incorporated herein by reference as if fully set forth). Each 25 μL reaction mixture contained 2.5 μL 10×PCR Buffer (500 mM KCl, 25 mM MgCl 2 , 200 mM Tris-HCl [pH 8.4], 0.1% Triton X-100), 2.0 μL 2.5 mM DNTP mixture (Takara, Japan), 0.3 μL of 10 μM V3-2 and V3-3, 0.13 μL 5U Taq polymerase, 1 μL of template DNA, and 18.77 μL sterilized ddH 2 O. The PCR protocol was as follows: 30 s initial denaturation at 94° C.; 10 cycles with each cycle consisting of 30 s of denaturation at 94° C., 30 s of annealing at 61° C. (the temperature of anneal decreased 0.5° C. after each cycle), and 40 s extension at 72° C.; 25 cycle with each cycle included 30 s denaturation at 94° C., 30 s annealing at 55° C., and 40 s extension at 72° C.; followed by a final 5 min extension at 72° C. PCR products stained with 0.02 μL mL −1  Genefinder were visualized on 1% (w/v) agarose gel at 120 V for 20 min, and visualized under SYNGENE Genesnap. A much higher degree of diversity was observed with primer sets V3-2/V3-3, hence its DGGE products were used for the following analysis. 
     After the DGGE was performed, all visible bands were excised from the gel and used as templates for re-amplification, using primer set V3-1/V3-2 (Jensen et al., 1998, which is incorporated herein by reference as if fully set forth). The PCR program was initiated with 30 s at 94° C., followed by 40 cycles of 5 s at 94° C., 30 s at annealing at 56° C., and 30 s at 70° C. The PCR products were purified using Qiaquick PCR preps (Qiagen, Valencia, Calif.) and cloned into a pGEM-T vector (Promega, USA). Positive recombinant clones were identified by PCR, and the PCR products were cleaned with ExoSap treatment and sequences were conducted by Genewiz, Inc., USA. Clone libraries from 12 samples resulted in 721 sequences of partial 16S rRNA gene fragments and the sequences were grouped into operational taxonomic units (OTUs) based on a 5% sequence distance cutoff calculated using the DOTUR program (Schloss and Handelsman, 2005  Appl. Environ. Microbl.  71, 1501-1506, which is incorporated herein by reference as if fully set forth). Six groups of bacteria were classified via a phylogenetic analysis using the Bayesian inference (BI), implemented with MrBayes version 3.1.2 (Huelsenbeck et al., 2001; Ronquist et al., 2003  Bioinformatics.  19, 1572-1574, which are incorporated herein by reference as if fully set forth). A best fit model of nucleotide substitution was identified using the Akaike information criterion (AIC) (Akaike, 1973) as implemented in MrModelTest 2.3 (Nylander, 2004). Bayesian analysis was carried out using GTR+I+G model selected by MrModelTest 2.3, in which model parameters were treated as unknown and estimated through the BI. The following settings were applied: implementing two Markov chain Monte Carlo (MCMC) runs, running four simultaneous Markov chains for 19 million generations, and sampling the Markov chains every 100 generations. Tracer V1.5 (Rambaut and Drummond, 2009) was used to judge convergence of the Bayesian Markov chain Monte Carlo runs. The first 10,000 sampled trees were discarded as burn-in. A consensus tree was constructed from the remaining sampled trees. Sequences obtained in this study were submitted to the GanBank database on Feb. 4, 2013, and are available therein under accession numbers KC581755-KC581779. See also Huang S and Jaffe P R,  Characterization of incubation experiments and development of an enrichment culture capable of ammonium oxidation under iron reducing conditions,  2014, Biogensciences Discuss, 11, 12295-12321, which is incorporated herein by reference as if fully set forth. Approximately 2.5 ng of each DNA extract from samples collected from the incubation on days 0, 30, 90, 160 and from the membrane reactor after 150 days of reactor operation were used for 454 pyrosequencing analysis. To amplify a 16S rRNA gene fragment of the appropriate size and sequence variability for the 454 pyrosequencing, specific primers Bact-338F1(CCTACG GGRGGCAGCAG) (SEQ ID NO: 2)/909R(CCGTCAATTYHTTTRAGT) (SEQ ID NO: 3), targeting the V3-V5 region of the 16S rRNA gene of bacteria were chosen (Pinto and Raskin 2012, which is incorporated herein by reference as if fully set forth). The PCR conditions used were 94° C. for 2 min, 20 cycles of 94° C., 45 s denaturation; 55° C., 45 s annealing and 72° C., 1 min extension; followed by 72° C., 6 min. After 20 rounds of amplification, another 3 rounds of amplification were done to add the A and B adapters required for 454 pyrosequencing to specific ends of the amplified 16S rRNA fragment for library construction (Margulies et al., 2005 Nature, 437, 376-380, which is incorporated herein by reference as if fully set forth). Approximately 4 ng/μl of 16S rRNA gene fragment from each soil samples was required to construct the five libraries for 454 sequencing. Polymerase chain reaction products were cleaned using the QIAquick PCR Purification Kit (Qiagen) following the manufacturer&#39;s instructions, quantified using a Qubit Fluorometer (Invitrogen), and then sent for 454-pyrosequencing using a Roche/454 GS FLX sequencer. 
     A total of 19,021 partial 16S rRNA sequences were obtained from the five soil samples. The sequences were then passed through the DOTUR program to further reduce errors as outlined previously (Schloss and Handelsman, 2005, which is incorporated herein by reference as if fully set forth). Briefly, after trimming, pre-clustering, removal of chloroplast sequences and alignments, a total of 10172 sequences remained. These were clustered with the average neighbor algorithm with a 3% dissimilarity cutoff, which resulted in 1015 OTUs (Pinto and Raskin 2012, which is incorporated herein by reference as if fully set forth). 
     Example 11. Primer Design for Real-Time PCR Assay 
     Two sets of primers, acd320f (5′-CGG TCC AGA CTC CTA CGG GA-3′) (SEQ ID NO: 4)-432r (5′-GAC AGG GTT TTA CAG TCC GAA GA-3′) (SEQ ID NO: 5) and acm342f (5′-GCA ATG GGG GAA ACC CTG AC-3′) (SEQ ID NO: 6)-439r (5′-ACC GTC AAT TTC GTC CCT GC-3′) (SEQ ID NO: 7) were designed for Acidobacteriaceae bacteria A8 and Acidimicrobiaceae bacterium A6 respectively from clone libraries in this study, using an NCBI Primer-Blast program (http://www.ncbi.nlm.nih.gov/tools/primer-blast). This program did not show any putative sequences deposited in the GenBank, that amplified with the selected primers, could interfere with the experiment. The sequences of Acidobacteriaceae bacteria and Acidimicrobiaceae bacterium A6 acquired from this study did not exhibit any mismatches with the above primer sequences. Primers were then used for real-time PCR amplification in the soil samples from the incubation experiments. 
     Example 12. Isotope Tracer Incubations  
     After 270 days of operation, Feammox enrichment slurries collected form the Feammox membrane reactor were used for isotope tracer incubations. Slurries were first incubated for 20 days in 50 mL vials under anaerobic conditions. Five treatments (n=3 per treatment) were conducted as follows: (1) control treatment with only anoxic DI water; (2) 15 NH 4 Cl addition; (3) 15 NH 4 Cl+Fe(III); (4) 15 NH 4 Cl and C 2 H 2  addition; (5)  15 NH 4 Cl, C 2 H 2  and Fe(III) addition. The final concentration of  15 NH 4 Cl was 1 mmol L −1 , and 5 mmol L −1  of ferrihydrite was add as the Fe(III) source. 5 mL of pure C 2 H 2  gas was added to the vials, which resulted in a finial C 2 H 2  concentration of 100 μmol L −1 . Samples were then incubated anaerobically for 7 days. The headspace gas was sampled every 24 hours for  15 N 2 O analysis. All these processes were conducted in an anaerobic glove box. N 2 O was determined by isotope ratio mass spectrometry (IRMS, Thermo Finnigan Delta V Advantage, Bremen, Germany).  15 N 2 O concentration was also calculated as  15 N 2 O atom % excess above its natural abundance, following methods described by Ding et al. 2014  Environ Sci Technol.  48(18):10641-7, which is incorporated herein by reference as if fully set forth.  15 N 2 O production rates were calculated from the linear change in  15 N 2  concentrations in the vial headspace between two given time points. 
     Example 13. Change in Fe and N Species Under Different Operational Conditions 
     Batch incubation experiments were conducted. Batches included soil slurry included with three different Fe(III) sources.  FIGS. 1A-1B  illustrate concentration of Fe(II) ( FIG. 1A ) and NH 4   +  ( FIG. 1B ) in incubation with three different Fe(III) sources: ferrihydrite (open circle), ferric chloride (closed square), and ferric citrate (closed triangle). Referring to these figures, the values represent the mean and standard error (n=3). After incubating the pre-treated soil slurry with the three different Fe(III) sources for 30 days, only samples to which either ferrihydrite or goethite had been added showed measurable NH 4   +  oxidation. Referring to  FIGS. 1A-1B , in samples incubated with ferric citrate and NH 4 Cl, Fe(III) reduction was much faster than in those supplied with Fe(III) oxides, but the NH 4   +  concentration remained fairly constant.  FIGS. 2A-2B  illustrate concentration of Fe(II) ( FIG. 2A ) and NH 4   +  ( FIG. 2B ) in 25-day incubation with NH 4 Cl and ferrihydrite (open circle), NH 4 Cl and goethite (closed circle). The values represent the mean and standard error (n=3).  FIGS. 3A-3B  illustrate concentration of Fe(II) ( FIG. 3A ) and NH 4   +  ( FIG. 3B ) during the 180 day incubation. 25 mmol L −1  Fe(III) was added on day 0. 1.0 mmol L −1  NH 4   +  was added on days 4, 24, and 60. 0.2 mmol L −1  NaHCO 3  was added on day 50 and day 90. 1.2 mmol L −1 +2 mmol L −1  of NH 4 Cl were added on day 125. The values represent the mean and standard error (n=3).  FIGS. 4A-4B  illustrate concentration of Fe(II) ( FIG. 4A ) and NH 4   +  ( FIG. 4B ) in 25-day incubations in samples with NH 4 Cl (open square), ferrihydrite (open circle), sterilized soil with NH 4 Cl and ferrihydrite (closed triangle). Referring to these figures, the values represent the mean and standard error (n=3). Still referring to  FIGS. 4A-4B , no detectable Fe(II) reduction or NH 4   +  oxidation was found in the sterilized soils amended with ferrihydrite and NH 4 Cl. Referring to  FIGS. 2A-2B , faster iron reduction and NH 4   +  removal was observed in ferrihydrite than in goethite-amended sediments. 
     Since samples incubated with ferrihydrite and NH 4 Cl resulted in the fastest NH 4   +  oxidation, the anaerobic incubation with ferrihydrite was extended to 180 days. Ferrihydrite as the Fe(III) source results in a larger negative ΔG value than goethite. The NH 4   +  oxidation rate increased as NH 4 Cl was supplied repeatedly, especially after 125 days of incubation when the NaHCO 3  additions were increased from 0.20 to 1.20 mmol L −1  in addition to the 2.00 mmol L −1  NH 4   +  added. Referring to  FIGS. 4A-4B , the increased NaHCO 3  dosing also increased the generation of Fe(II).  FIG. 9  illustrates stoichiometry between the Fe(II) production and NH 4   +  consumption during 180 day incubation. Referring to  FIG. 9 , 25 mmol L −1  Fe(III) was added on day 0; 1.0 mmol L −1  NH 4   +  was added on days 4, 24, and 60; 0.2 mmol L −1 NaHCO 3  was added on day 50 and day 90 of the incubation. 1.20 mmol L −1 +2 mmol L −1  of NH 4 Cl were added on day 125. The values represent the mean ratio (n=3). During the 180-day incubation, the ratio of Fe(II) produced to NH 4   +  removed gradually increased until it reached 5.3:1 by day 160 after which it remained stable. 
       FIGS. 5A-5B  illustrate concentration of NO 3   −  (open circle) and NO 2   −  (closed square) ( FIG. 5A ) and DOC (open triangle) and TN (open square) ( FIG. 5B ) during the 180 day incubation. Referring to these figures, 25 mmol L −1  Fe(III) was added on day 0. 1.0 mmol L −1  NH 4   +  was added on days 4, 24, and 60. 0.2 mmol L −1  NaHCO 3  was added on day 50 and day 90 of the incubation; 1.20 mmol L −1 +2 mmol L −1  of NH 4 Cl were added on day 125. The values represent the mean and standard error (n=3). 
     Referring to  FIGS. 5A-5B , NO 2   −  appeared within a few days after the addition of NH 4   + , with a maximum concentration 0.44±0.17 mmol L −1  in the second NH 4   +  oxidation cycle. Referring to  FIG. 5A , NO 2   −  did not accumulate in the system and was immediately consumed after generation. Referring to  FIGS. 5A-5B , NO 3   −  production showed a similar pattern to that of NO 2   −  ( FIG. 5A ), and TN loss similar to the decrease in NH 4   +  ( FIG. 5B ). During 180 days of incubation, the system experienced a loss of TN of 57.2±3.13 mg L −1 . Referring to  FIG. 5B , the DOC content fluctuated slightly in the early stage of incubation, but overall, the DOC concentration was relatively stable at around 45˜50 mg L −1 . 
     A 64.5% NH 4   +  removal, between inflow and outflow was achieved in the membrane reactor after 150-days of operation. 
     Example 14. Phylogenetic Analysis of the Microbial Community Based on 16S rRNA Gene 
       FIG. 6  illustrates comparison of denaturing gradient gel electrophoresis (DGGE) analysis profiles of soil communities during anaerobic incubations. Samples from 0, 30, 90 and 160 days of incubation with ferrihydrite+NH 4 Cl+ NaHCO 3  (lane 1-4); 160 days of incubation with only ferrihydrite (lane 5); ferric chloride+NH 4 Cl (lane 6); ferric citrate+NH 4 Cl (lane 7); 120 days incubation with ferrihydrite+NH 4 Cl+ NaHCO 3 + organic carbon (band 8); ferrihydrite+NH 4 Cl+ organic carbon (lane 9). Still referring to  FIG. 6 , samples from 6 and 120 days of incubation without any addition (lanes 10 and 11) were used as controls. 
     Still referring to  FIG. 6 , all visible bands observed in the DGGE analysis (significant bands were marked) were excised from the gel and sequenced after cloning. Clone libraries from 12 samples resulted in 721 sequences of partial 16S rRNA gene fragments, and six groups of bacteria were classified via a phylogenetic analysis. During this 180-day anaerobic incubation with ferrihydrite and NH 4 Cl, the microbial communities shifted dramatically and the microbial diversity decreased with time. See  FIG. 6 , lanes 1-4. Some DGGE bands disappeared gradually with time, such as band A5 and band A7. Band A5, represents a dissimilatory iron-reducing bacteria,  Geobacter  sp., which existed in this Fe(III)-rich wetland soil and reappeared for a short time during the initial anaerobic incubation. Band A7, represents an ammonia-oxidizing bacterium,  Nitrosomonas  sp., which showed a strong presence in the samples at 30 days of incubation and was attenuated after longer incubation times. In contrast, DGGE bands A6, A8 and A9 became more significant as the incubation time increased, showing that there were three groups of bacteria dominating in the system after 160 days of incubation. Band A6 represents a group of bacteria belonging to the Acidimicrobiaceae family. Bacteria from the Acidobacteriaceae family are represented by band A8. Some species in this family have been described as iron reducers and obligate heterotrophs (Kishimoto et al, 1991 Water Res 41: 2996-3004; Rowe et al., 2007 Environ Microbiol 9:1761-1771; Coupland and Johnson, 2008 FEMS Microbiol Lett 279:30-35). DGGE band A9 represents bacteria of the Rhodocyclaceae family. This family contains mainly denitrifying bacteria, which exhibit very versatile metabolic capabilities (Smith et al, 2005 Water Res 39: 2014-2023; Huang et al., 2011 Biogeosciences 8: 5251-5280). 
     Microbial communities also differed between samples incubated with various Fe(III) sources, and between samples with or without the addition of inorganic carbon. Samples supplied with either ferric chloride or ferric citrate as the Fe(III) source plus NH 4   + , and samples supplied with just ferrihydrite and no NH 4   + , had a decreased diversity in their bacterial communities. See  FIG. 6 , lanes 5-7. Samples supplied with both organic carbon (1.00 mmol L −1  sodium citrate) and inorganic carbon (1.20 mmol L −1  NaHCO 3 ) had a higher bacterial diversity. See  FIG. 6 , lane 8. 
     Changes in the microbial community after 180 days of incubation were also confirmed via 454-pyrosequencing, and the obvious growth of Actinobacteria, Acidobacteria and β-Proteobacteria groups (which band A6, A8 and A9 belong to) was consistent with the DGGE results, where the Actinobacteria cell number increased the most. Planctomycetes phylum, with which anammox bacteria are affiliated, was detected in the first 90 days of incubation, but disappeared or was below detection on day 160. Actinobacteria were also the dominant species in the Feammox enrichment reactor based on the results of the 16S rDNA library obtained via pyrosequencing. 
     The Acidimicrobiaceae bacterium, represented by band A6, which belongs to the Actinobacteria phylum, was the dominant species in the incubation experiments after 180 days of incubation (14.8% in total 16S rRNA gene sequences) as well as in the membrane reactor after 150 days of operation (40.2% in total 16S rRNA gene sequences). Its similarity to other Acidimicrobiaceae-related sequences was shown using a phylogenetic tree. The tree was constructed using the Bayesian inference (BI) method with 16S rRNA gene sequences from DGGE band A6 and bacteria from the Acidimicrobiaceae family from other studies. Unlike the bacteria represented by band A8 and A9, which were also found in samples that did not show Feammox transformations, this Acidimicrobiaceae bacterium was only detected in incubations (or reactor) that were augmented simultaneously with ferrihydrite, NH 4 Cl, and NaHCO 3  and have shown Feammox activity. 
     Example 15. Changes of Bacterial Abundance and Activity During Incubations and in the Reactor 
     The total bacterial abundance determined via the 16S rRNA gene copy number, decreased during the 180-day incubation.  FIG. 7  illustrates abundance of total bacteria (closed rhombus) during 180 days of anaerobic incubation. 16S rRNA gene (black bars) and RNA copy numbers (gray bars) of Acidimicrobiaceae bacterium A6 in soil samples with 1.20 mmol L −1  NaHCO 3  addition. 16S rRNA gene (white bars) and RNA copy numbers (dotted bars) of bacterium A6 with 0.20 mmol L −1  NaHCO 3  addition. Referring to  FIG. 7 , both, 16S rRNA gene and rRNA fragment copies of Acidimicrobiaceae bacteria (DGGE band A6) increased during the incubation, particularly after 90 days. Still referring to  FIG. 7 , the rRNA numbers increased slowly during the first 3 months and doubled between day 130 and day 140 of the incubation period. rRNA as a biomarker for changes of protein level, even though not as specific as mRNA, is a good indicator for bacterial activity (Poulsen et al., 1993 Appl Environ Microbiol 59: 1354-1360; Park et al., 2010 Environ Sci Technol 44: 6110-6116), both of which are incorporated by reference herein as if fully set forth. Increase in the denitrifier activity was most likely stimulated by the NO 2   −  generated via Feammox. The number of the amoA gene, representing the abundance of ammonia-oxidizing bacteria, decreased sharply with time and was hardly detected after 90 days of incubation. Through quantification of thaumarchaeal amoA genes, none of the acidophilic ammonia oxidizers were detected in the system. 
     In the Feammox reactor, the copy number of Acidimicrobiaceae bacterium A6, Anammox bacteria and nirS gene were 0.37×10 7 , 0.13×10 6 , and 0.92×10 6  copies g −1  dw, respectively, while the amoA gene was not detected. 
     Example 16. Changes of Bacterial Abundance and Activities with NaHCO 3  Amendment 
     Abundance and activity of Acidimicrobiaceae bacteria, represented by band A6, were compared between samples incubated under the same conditions except the amounts of NaHCO 3  added (0.20 mmol L −1  vs. 1.20 mmol L −1 ). From day 125 to day 180 of the incubation, both 16S rRNA gene and rRNA fragment numbers of Acidimicrobiaceae bacteria were higher in the soils with the higher inorganic carbon content. Referring to  FIG. 7 , the 16S rRNA gene copies of samples augmented with 1.20 mmol L −1  NaHCO 3  were four times higher than those in samples that had been augmented with only 0.20 mmol L −1  NaHCO 3 . The rRNA copies of the Acidimicrobiaceae bacteria, showed even larger differences in response to the amounts of NaHCO 3  added. In the samples augmented with 1.20 mmol L −1 NaHCO 3 , the rRNA copy number increased from 0.04±0.06×10 6  to 0.19±0.09×10 6  copies g −1  dw over 50 days of incubation (day 130 to day 180). Still referring to  FIG. 7 , however, in the samples to which only 0.2 mmol L −1  NaHCO 3  were added on day 125, the rRNA number gradually deceased from 0.29±0.10×10 5  to 0.19±0.05×10 5  copies g −1  dw during the same 50 days incubation. 
     Example 17. Nitrogen Species Changes in Samples Incubated in the Presence of C 2 H 2    
     C 2 H 2  can inhibit the oxidation of NH 4   +  to NO 2   −  under aerobic conditions, and the reduction of N 2 O to N 2  as well as the anammox pathway under anaerobic conditions (Yoshinari et al., 1977 Soil Biol Biochem 9: 177-183; Jensen et al., 2007 FEMS Microbiol Ecol 26: 17-26; Kartal et al., 2011 Nature 479:127-130, all of which are incorporated by reference herein as if fully set forth). To gain further insights into the nitrogen removal process observed, incubations with C 2 H 2  were conducted.  FIGS. 8A-8D  illustrate concentration of NH 4   +  ( FIG. 8A ), NO 2   −  ( FIG. 8B ), NO 3   −  ( FIG. 8C ), and N 2 O ( FIG. 8D ) in the samples incubated with (open circle) or without (closed square) C 2 H 2 . The values represent the mean and standard error (n=3). After 20 days of incubation, less NH 4   +  was oxidized in the samples amended with C 2 H 2 , compared to those incubated without C 2 H 2 . Referring to  FIG. 8A , NO 2   − , which is postulated to be the direct product of the NH 4   +  oxidation, accumulated slowly in samples incubated with C 2 H 2 . Referring to  FIG. 8B , NO 3   −  reached a higher concentration in samples without C 2 H 2  than in samples incubated with C 2 H 2 . Referring to  FIG. 8C , N 2 O, a product of NO 2   −  reduction, accumulated in samples incubated with C 2 H 2 , which inhibits the reduction of N 2 O to N 2 . Fe(II) production was not much affected by the presence of C 2 H 2 , and after 20 days incubation was 4.36±0.72 and 5.71±0.67 mmol L −1  in sample incubated with and without C 2 H 2 , respectively. 
     In  15 N isotope tracer incubations, detectable  15 N—N 2 O was only found in samples amended with both,  15 NH 4 Cl and Fe(III), with  15 N—N 2 O production rates 2.14±0.059 or 0.072±0.023 μg g −1  d −1  in samples incubated with or without C 2 H 2  treatment. 
     Referring to  FIG. 6 , DGGE band A5 represents dissimilatory iron-reducing bacteria, which appeared for a short time at the beginning of the anaerobic incubation. For longer incubation times these heterotrophic bacteria decreased rapidly. Referring to  FIG. 2A  and  FIG. 4A , over a 25 day incubation period, more than three times the mass of Fe(II) was produced in samples amended with ferrihydrite and NH 4   +  as compared to the samples amended only with ferrihydrite, indicating that most of the Fe(III) reduction came from the Feammox reaction, and not from dissimilatory Fe(III) reduction. 
     Referring to  FIG. 6 , AOB represented by DGGE band A7, as well as the amoA gene, decreased after 30 days of incubation. Also, no AOA or acidophilic ammonia oxidizers were detected although the pH condition seems suitable for them in these incubations. Oxygen deficiency was the most likely reason for the decline in AOB in this system over time (Laanbroek et al., 1994 rch Microbiol 161:156-162). Referring to  FIGS. 4A-4B , even though a small amount of AOB would be enough for NH 4   +  oxidation, in control samples to which no Fe(III) was added, and which AOB do not require, no NH 4   +  consumption was detected. Moreover, the decrease in amoA gene at a time of increasing NH 4   +  oxidation also indicates that neither AOB nor acidophilic ammonia oxidizers were the drivers of the NH 4   +  oxidation in the later incubation times. 
     An uncultured Acidimicrobiaceae bacterium became the dominant species during the 180-day anaerobic incubation period, increasing from 0.92% on day 0 in terms of cell numbers to 14.8% on day 160. Referring to  FIGS. 1A-1B ,  FIGS. 2A-2B , and  FIG. 6 , in the incubation experiments conducted (which included controls with only NH 4   + , only iron, autoclaved, and various Fe(III) sources), this Acidimicrobiaceae bacterium was only detected and growing in samples to which NH 4   +  was supplied as an electron donor, ferrihydrite was supplied as electron acceptor, and NaHCO 3  was supplied as a carbon source. The abundance and activity of this Acidimicrobiaceae bacterium increased along with the Feammox activity during the incubations. Referring to  FIG. 7 , during the incubation period its rRNA changed from (0.22±0.01)×10 5  copies g −1  dw to (0.28±0.07)×10 6  copies g −1  dw, indicating a substantial increase in its activity. In the continuous flow membrane reactor, which had a high NH 4   +  removal and Fe(III) reduction rate, this Acidimicrobiaceae bacterium was enriched from an initial 14.8% to 40.2% after 150 days operation, and no other known NH 4   +  oxidizers (AOB or anammox) were detected. These results indicated that this Acidimicrobiaceae bacterium might play an important role in the Feammox reactions described in this study. According to a phylogenetic analysis, this bacterium has a 92% identity with  Ferrimicrobium acidiphilum  sp.  F. acidiphilum , which belongs to the Acidimicrobiaceae family, and was first isolated from mine environments, and  F. acidiphilum  strain T23 is the only pure strain with a comprehensive characterization. Uncultured  Ferrimicrobium  sp. has been detected in mine water, but so far not in wetland soils.  Ferrimicrobium  sp. is an acidophilic heterotrophic ferrous iron oxidizing bacterium, which can also reduce Fe(III) under anoxic conditions (Johnson et al., 2009). The uncultured Acidimicrobiaceae bacterium, also has a 90% identity with  Acidimicrobium ferrooxidans , a facultative autotroph in the same family that can reduce Fe(III) in anaerobic environments while oxidizing sulfide to sulfur and exists widely in soil environments. 
     According to a phylogenetic comparison with similar clones from studies reported in the GenBank, and taking into account its special growth characteristics (stimulated by inorganic carbon, oxidizing NH 4   +  coupled to Fe(III) reduction), also its gradual activity increase with increased Feammox activity, as well as a strong link with a Feammox enrichment reactor, this uncultured Acidimicrobiaceae bacterium A6 is probably a previously unreported species in the Acidimicrobiaceae family that might be either responsible or play a key role in the Feammox process described here. Referring to  FIGS. 3A-3B  and  FIG. 7 , Acidimicrobiaceae bacterium A6 was more active and the Feammox pathway was faster in samples with higher NaHCO 3  amendments, which, in addition to the fact that ΔG in Equation 1 is negative, indicates that if this Acidimicrobiaceae bacterium is actually responsible for conducting the Feammox reaction as depicted in equation 1, it may be an autotroph. Growth of nirS gene suggested that denitrification pathways were also active in the incubations described here. NO 2   −  that was being produced during the anaerobic NH 4   +  oxidation was reduced to N 2  by denitrifiers, and NO 2   −  did not accumulate in the system. 
     Referring to  FIGS. 1A-1B  and  FIGS. 2A-2B , the Feammox reaction studied here proceeded only when iron oxides (ferrihydrite or goethite) were supplied as electron acceptor, whereas samples incubated with ferric chloride or ferric citrate as the Fe(III) source showed no measurable NH 4   +  oxidation. In the incubations to which ferric citrate was added as the Fe(III) source, Fe(III) was reduced rapidly by dissimilatory iron reducers, using organic carbon as electron donor. Referring to  FIG. 6 , the DGGE results for incubations with ferric citrate (lane 7) show that the most dominant species was an  Actinobacterium , known to reduce iron under anaerobic conditions. Acidimicrobiaceae bacterium A6 was not detected in these incubations. Since acidic conditions as well as minimal dissolved Fe(II) and NO 2   −  concentrations are required to make the Feammox reaction energetically favorable as shown in Equation 1, the presence of iron oxides as the main Fe(III) source may have helped to maintain the concentrations of Fe(II) in solution below the detection limit through the incubation since iron oxides can sorb Fe(II) and/or incorporate it into their structure. 
     Various NH 4   +  oxidation products, i.e. NO 3   − , NO 2   −  and N 2 , generated through the Feammox process are thermodynamically feasible, and were reported in different Feammox studies (Sawayama, 2006; Shrestha et al., 2009; Yang et al., 2012, which are incorporated by reference herein as if fully set forth). Because there was no initial nitrate or nitrite in the system, because all experiments were conducted under strict oxygen free conditions, and because of the rapid decrease of amoA genes, neither NO 3   −  reduction nor aerobic NH 4   +  oxidation could be the reason for the formation of NO 2   −  during the incubations. In all incubations where NH 4   +  was removed, the production of NO 2   −  was observed, although NO 2   −  did not accumulate. Most of the NO 2   −  produced from the NH 4   +  oxidation was reduced rapidly by denitrifiers, which were present in the incubations. 
     When C 2 H 2  was used to stop the reduction of N 2 O to N 2 , the total N 2 O (0.72±0.23 mmol L −1 ) plus NO 2   −  produced (0.13±0.07 mmol L −1 ) was equal to the NH 4   +  consumed, showing that NH 4   +  was not oxidized directly to N 2  in the samples.  15 N—NH 4   +  incubations, as an extension of C 2 H 2  treatment, showed that  15 N—N 2 O built up when  15 NH 4 Cl was added as the NH 4   +  source, demonstrating that NH 4   +  was oxidized during the Feammox process rather than be adsorbed or taken uptake by microorganisms in the system. 
     Although nitrification might happen in suboxic environments (oxygen &lt;5 μM, Lam et al., 2007), NH 4   +  oxidation in the presence of C 2 H 2  has never been reported. C 2 H 2  is an inhibitor of ammonia monooxygenase (AMO), and can restrain aerobic NH 4   +  oxidizers from using oxygen by binding covalently to AMO (Hynes and Knowles, 1982; Hyman and Wood, 1985; Gilch et al., 2009). C 2 H 2  can also inhibit the NH 4   + -activation step of anammox cells, which use NO 2   −  as the oxidant (Kartal et al., 2011). Therefore these Feammox bacteria might differ from common NH 4   +  oxidizers, by using an alternative NH 4   +  oxidation pathway that is not inhibited by C 2 H 2 , and AMO might not play a role in Feammox. The fact that NH 4   +  oxidation was not affected by the presence of acetylene is a further indication that AOB are not responsible for this process since they would be affected by acetylene. Furthermore, in the isotope tracer incubations,  15 N—N 2 O was below the detection limit in samples to which Fe(III) was not supplied, showing again that NH 4   +  oxidation proceeded only when iron was being reduced. 
     Referring to  FIG. 9 , the role of anammox during the incubations was also evaluated. During the incubations the ratio of NH 4   +  oxidized to Fe(III) reduced increased gradually from 1:1.9 to 1:5.3, which is close to the stoichiometry of 1:6, shown in Equation 1. Although the discrepancies in the Feammox stoichiometry between iron and NH 4   +  are attributed in part to incompletely Fe(II) extraction, the influence of anammox activity in the earlier incubations would have contributed to a lower Fe(II) produced to NH 4   +  removed ratio than the theoretical value of 1:6. 
     The Feammox reaction became more dominant in terms of NH 4   +  oxidation after 125 days of incubation due to a relative increase in the activity of the Feammox bacteria. A parallel pathway to Feammox, such as anammox, could as mentioned above, explain the lower stoichiometric ratio, especially at earlier incubation times. In the samples taken before the incubation, 0.17±0.05×10 6  copies g −1  dw of anammox rRNA gene were found, which decreased to 0.09±0.06×10 5  on day 130. It was postulated that anammox was responsible for some initial NH 4   +  and NO 2   −  removal, and denitrification became more dominant for NO 2   −  removal later during the incubation period. NH 4   +  removal via Anammox in the early incubations may also explain why the observed NH 4   +  oxidation rates and the abundance of Acidimicrobiaceae A6 did not change proportionally over the full incubation period. 
     Example 18. Influence of Environmental Factors on Feammox Pathway in Soil Environments 
     Sample collection. Soils for all the experiments described in this study were taken from a series of local wetland-, upland-, as well as storm-water detention pond-sediment at New Jersey and labeled according to the samples location as L, A, P, C, B, V and W. Three soil cores were collected from 0 cm to 20 cm soil from each sample location, and transported to the laboratory within 2 hours for further analysis. 
     Analysis of Chemical Properties. 
     Physicochemical characteristic of these soils such as soil pH; Fe content [Fe(III) and Fe(II)]; nitrogen species (NO 3   − , NO 2   −  and NH 4   + ); sulfate (SO 4   2− ); phosphate (PO 4   3− ); dissolve organic carbon (DOC) were determined. pH was measured immediately using a pH electrode. A 0.5N HCl extraction was conducted for 24 hour at room temperature to determine acid-extractable Fe(II) and NH 4   +  concentrations in the soils. Fe(II) was analyzed using the ferrozine assay method (39), and NH 4   +  was analyzed using a Dionex™ Ion Chromatograph (LC3000) with a CS-16 Column and a CS-16 guard column (flow rate=1.0 mL min −1 , detection limit=0.012 ppm). NO 3   − , NO 2   − , SO 4   2−  and PO 4   3−  concentrations were measured from anaerobic DI water extraction for 1 hour, via Ion Chromatography, using an AS-22 Column along with an AG-22 guard column (flow rate=1.2 mL min −1 , detection limit=0.016 ppm). For the DOC analyses a Shimadzu TOC-5000(A) was used. 
     Batch Incubation. 
     A series of incubation experiments were conducted. Soil samples from each location were divided into 12×10 g (air-dry equivalent) subsamples, and added into 50 mL serum vials, with 30 mL deionized water. The soil slurries were purged thoroughly with a CO 2 :N 2  (80:20) mixture, and then incubated under anaerobic condition in glove box. 
     In the first incubation experiment, Feammox activities of each sample were checked. In day 0 to 15, no NH 4   +  or Fe(III) was added to the incubations. On day 16, samples were amended with 5 mmol·NH 4 Cl and 30 mmol·L 1  ferrihydrite, and continue incubated under anaerobic condition. On day 45, 2 mmol·L −1  NH 4 Cl and 5 mmol·L −1  ferrihydrite were added again after NH 4   +  was exhausted. Autoclaved sterilized soils were incubated as controls. Triplicate samples were collected from two vials every four days to analyze iron and nitrogen species. 
     The second incubation was conducted to check how pH and NO 2   −  concentration control Feammox reaction. For pH incubation, enrichment culture with Acidimicrobiaceae bacterium A6 were exposed to different pH gradients, pH=2, 4.5, 6.5, 8 (adjusted with HCl and NaOH). For NO 2   −  incubation, enrichment cultures were added with different concentration of NO 2   −  (0.02, 0.2, 1.0, 2.0 mmol·L −1  as final concentrations). The initial concentrations of Ferrihydrite were 25 mmol·L −  land 2 mmol·L −1  NH 4   +  was added. Triplicate samples were collected every two days to analyze iron, nitrogen species, and also the copy number of Acidimicrobiaceae bacterium A6. 
     DNA was isolated as described in Example 6. 
     QPCR was carried out for total bacteria, anammox bacteria and Acidimicrobiaceae bacteria, represented by 16S rRNA genes, using primer sets 1055f/1392r, Amx368f/Amx820r and acm342f/439r, respectively. (Harms et al. 2003; Schmid et al, 200, 2003 and Huang and Jaffe, 2013, all of which are incorporated by reference as if fully set forth) For the detection of denitrifiers, denitrifying functional genes (nirS) were quantified with primer sets NirS3/NirS5 (Braker et al., 1998, which is incorporated by reference herein as if fully set forth). Thermal cycling conditions for total 16S rDNA and nirS gene numbers were essentially as described in Example 7. 
     Statistical Analysis. 
     Correlations between the bacterial distributions vs. the environmental factors were analyzed with the canonical correspondence analysis (CCA) using R (22). Analyses of Spearman rank, multivariate and stepwise linear regressions of environmental and bacterial abundance variables were carried out using SPSS v12 on both raw and log-transformed data. All data were analyzed using one-way analysis of variance (ANOVA) with the significant level P&lt;0.05. 
     It has been shown that anammox activity is optimal at a pH of 7.8-8.0 and temperatures between 28° C.-35° C. In anammox reactors, the DO concentration is usually maintained between 0.2 mg/L-1 mg/L to allow for partial nitritation, which is required to achieve satisfactory NH 4   +  removal. In soils environments, anammox bacteria are usually present under slightly oxic conditions, which again, ensures that AOB are able to provide adequate NO 2   −  levels. Both AOB and anammox bacteria are autotrophic, therefore the organic carbon content in soils does not affect their NH 4   +  oxidation rate, except for  Nitrosopumilis maritimus  (an AOB species) which was reported to be inhibited by organic substrates even at very low concentrations. 
     AOB and anammox bacteria usually coexist in hypoxic environments, since AOB provide the NO 2   −  for the anammox reaction. Hence, Feammox bacteria, which also produce NO 2   −  while oxidizing NH 4   + , may enhance anammox in environments where AOB are not active. Batch incubations of soil samples at sites where Feammox activity was observed have shown that after NH 4   +  was oxidized to NO 2   −  by the Feammox process, nitrogen loss proceeded via denitrification and/or anammox. Since, as shown by equation 1, removal of NO 2   −  makes the reaction more favorable, the coexistence of Feammox with denitrifiers and/or anammox may be key for anaerobic ammonium oxidation in soil environments. 
     Therefore, influence of the different environment factors on the Feammox presence/activity in soil environments was investigated, the relationships between Feammox bacteria and other microorganisms responsible for nitrogen transformations in soils were determined. 
     Chemical Properties of Samples Collected from Different Locations 
     Soil and sediment samples collected for this study cover a wide range of chemical properties: pH from 4.26 to 7.21; Fe(III) from 120 to 1243 mg kg −1 ; Fe(II) from 7.92 to 356 mg kg −1 ; NH 4   +  from 6.02 to 86.0 mg kg −1 ; NO 3   −  from 6.71 to 274.8 mg kg −1 ; NO 2   −  from 4.74 to 152.8 mg kg −1 ; SO 4   2−  from 4.89 to 128.6 mg kg −1 ; PO 4   3−  from 2.97 to 28.5 mg kg −1 ; DOC from 9.37 to 28.09 g kg −1 . 
     Most of the soil and sediment samples selected for this study were acidic. pH value of surface soil samples (top 5 cm of soil,) was higher than that of soil below 10 cm. Concentrations of NO 3   −  and DOC were also higher in the surface soils. NO 3   −  were only showed in samples from 0 to 5 cm of soil, but hardly detected in soils collected from 10 to 20 cm in L7. On the contrary, NO 2   −  was found more rich below 10 cm than the upper soil samples in most of the locations. 
     All of these soil samples were iron rich, compared to the total iron levels usually reported for wetland soils (100 mg·kg −1  to 620 mg·kg −1 ) and sediment environments (30 to 120 mg·kg −1 ). Fe(III) concentrations in vegetation-covered soil samples were obvious higher than the other samples. In additional, Fe(III) concentrations in soil collected from rhizosphere, were much higher than that from non-rooting zone at the same location. Fe(II) abundance shown a different trend, and was found negatively correlated (r=−0.61 p=0.001) with Fe(III) in the same sample locations. 
     Among these samples, samples originated from a forested riparian wetland area that was 0.5 km near some agricultural lands, have higher NH 4   +  and PO 4   3−  contents. The distribution of SO 4   2−  in samples of this study was similar to that of NO 3   −  between different sample locations but shown no obvious discrepancy with sample depth. 
     Feammox activity and abundance of Acidimicrobiaceae bacterium A6 Fe(II) production and NH 4   +  consumption were checked after two weeks anaerobic incubation to monitor the Feammox activity in different samples. After 15 days of anaerobic incubation without the addition of extra NH 4   +  and Fe(III), all samples showed clearly iron reduction, form 2.10 to 8.86 mmol·L −1 . 
     The existence and abundance of the Feammox Acidimicrobiaceae bacterium A6 in soil and sediment samples were determined via qPCR analysis. Abundance of Acidimicrobiaceae bacterium A6 in the field samples shown consistent with the anaerobic NH 4   +  consumption in incubations, and a positively correlation (r=0.58 p=0.012) were revealed between them. 
     Feammox activity in incubation with different pH and NO 2   −  concentrations. The Feammox reaction was most active in samples with pH 4.5. When pH increased or decreased, NH 4   +  oxidation and Fe reduction slow down, and Feammox reaction seem to stop at a pH 2.0 or 8.0. Abundance of Feammox Acidimicrobiaceae bacterium A6 increased after 14 days anaerobic incubation in samples with pH 2, 4.5, or 6.5 and slightly decreased in alkaline conditions. There was no significant difference between number of Acidimicrobiaceae bacterium A6 in samples incubated with pH 4.5 and 6.5, which is 2.37×10 4  and 2.41×10 4  copies mL −1 , respectively. 
     Feammox activity was sensitive to NO 2   −  concentration in the samples. Feammox reaction processed when NO 2   −  concentrations were 0.02 and 0.2 mmol·L −1 , but it was inhibited when NO 2   −  reached to 1.0 mmol·L −1 . Changes of Acidimicrobiaceae bacterium A6 abundance were consistent with Feammox activities with different concentration of NO 2   −  were added. In samples with 1.0 and 2.0 mmol·L −1 NO 2   −  were added, the numbers of Acidimicrobiaceae bacterium A6 were decreased after incubation. 
     CCA Analysis of Feammox Distributions in Soil Samples. 
     Soils for all the experiments described in this study were taken from three areas: New Jersey and South Carolina in Unities States, Guangdong province in China. A total of 52 locations were selected and cover 4 different types of soil samples, which are wetland soils (W), river sediments (R), forest soils (F), paddy soils (P).  FIGS. 12A-12B  illustrate ordination plots of the canonical correspondence analysis (CCA) for the first two dimensions of CCA of the relationship between the environmental factors and Feammox bacteria vs. environment factor of soil analysis and relation of Feammox to other bacterial communities affecting the nitrogen cycle.  FIG. 12A  illustrates the total variance in the bacterial abundance and the cumulative variance of the bacteria-environment relationship.  FIG. 12B  illustrates the total variance in the microbial composition and the cumulative variance of the bacteria-sampling location relationship. 
     Referring to  FIG. 12A , the CCA analysis of Feammox bacteria and nitrogen microorganisms in response to environmental variables confirmed the influence shown in this figure. The first two CCA axes (CCA1 and CCA2) explained 73.2% of the total variance in the bacterial abundance and 80.6% of the cumulative variance of the bacteria-environment relationship. pH value (p=0.030) and Fe(III) content (p=0.021) had significant effects on the distributions of Acidimicrobiaceae bacterium A6, and NO 2   −  seemed to inhibit this bacteria by showing a negatively correlation. Concentrations of NO 2   −  were supporting anammox bacterial existence (p=0.025), and the combined effects of SO 4   2−  and NO 2   −  affects the distribution of nirS genes. NH 4   +  content was not limited for either Feammox or aerobic/anaerobic NH 4   +  oxidation bacteria. Referring to  FIG. 12B , the first two CCA axes (CCA1 and CCA2) explained 71% of the total variance in the microbial composition and 81% of the cumulative variance of the bacteria-sampling location relationship. The CCA analysis showed that CCA1 represented the pH level of the soils. Referring to  FIG. 12B , sample with Feammox activity assembled in a low pH area, while other soil samples distributed in the opposite pH area showed no Feammox reaction. CCA2 represents the vertical distributions of soil samples, soils collected from similar depth gathered together. More aerobic or anaerobic NH 4   +  oxidation bacteria were found in surface soil samples. It was observed that Feammox bacteria and denitrifiers tended to be active at depths below 10 cm of the soil environments. 
     Example 19. Reduction of Uranium by Acidimicrobiaceae Bacteria A6 with Ferrihydrite as the Iron Source 
     Acidimicrobiaceae bacteria A6 from a pure culture were prepared for uranium (U) bioreduction experiments. Twelve 15-mL vials of bacteria in their normal growth medium were centrifuged after which the bacteria were resuspended in a modified anaerobic growth medium. Of the twelve vials, three contained bacteria that had been autoclaved to establish a control condition with dead bacteria. The centrifugation and washing was repeated twice. The modified anaerobic growth medium consisted of NaHCO 3 , KHCO 3 , MgSO 4 . 7H 2 O, CaCl 2 , and AQDS. It differed from the normal growth medium in that it did not contain KH 2 PO 4 , which was removed due to its high sorption of U, or NH 4 Cl, which was added separately. Uranyl acetate was added to all vials such that the initial concentration of U was approximately 64 μM. 
     The twelve vials were divided into four groups: three different control conditions and the experimental condition as shown in Table 1. Ammonium (NH 4   + ) in the form of NH 4 Cl was added to the three experimental vials as an electron source for the bacteria. In the first control condition, NH 4 Cl was also added, but the microbial monoxygenase enzyme was inhibited by the addition of Na 2 S. The second control condition, mentioned earlier, contained bacteria that had been killed in an autoclave. NH 4 Cl was added to this condition, as well. No NH 4 Cl was added to the third control condition to establish an electron donor-limited control. No iron (Fe) was added to any vials, but some ferrihydrite, a common ferric oxyhydroxide, which acted as the Fe source in the original pure culture medium remained with the bacteria through the washing process. 
     
       
         
           
               
             
               
                 TABLE 1 
               
             
            
               
                   
               
               
                 Experimental and control conditions in U bioreduction 
               
               
                 experiment with ferrihydrite as Fe source 
               
            
           
           
               
               
               
               
               
            
               
                   
                   
                 Control 1: 
                 Control 2: 
                   
               
               
                   
                   
                 Enzyme 
                 Autoclaved 
                 Control 3: 
               
               
                   
                 Experimental 
                 Inhibited 
                 Bacteria 
                 No NH 4 + 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
            
               
                 NH 4 +, mM 
                 3.98 ± 0.01 
                 3.96 ± 0.01 
                 4.01 ± 0.02 
                 0.03 ± 0.01 
               
               
                 Initial total U, μM 
                 64.8 ± 15.6 
                 65.5 ± 6.3  
                 65.4 ± 6.1  
                 59.3 ± 17.0 
               
               
                 Na 2 S, μM 
                 0 
                 20 
                 0 
                 0 
               
               
                 Acidimicrobiaceae 
                 Live 
                 Live 
                 Dead 
                 Live 
               
               
                 bacteria A6 
               
               
                   
               
            
           
         
       
     
     In Table 1, values given for NH 4   +  and U concentrations are the averages of three vials±one standard deviation 
     The extent of Acidimicrobiaceae bacteria A6 activity in each condition was monitored by measuring concentrations of U and NH 4   +  on the day the experiment started and again six days later. Samples for NH 4   +  analysis were filtered using 0.2 μm nylon filters and stored at 4° C. until they were analyzed using a Dionex™ Ion Chromatograph ICS3000 with a CS-16 column, a CS-16 guard column, and a CERS 500 (4 mm) suppressor. Samples for U(VI) analysis were also filtered at 0.2 μm to remove reduced U(IV) precipitates and were preserved in 2% HNO 3 . Unfiltered samples for total U analysis were mixed in a 1:1 ratio with 0.2 M NaHCO 3  to dissolve any U(IV) that had been reduced by the bacteria. After a 24-hour extraction at room temperature, these samples were also preserved in 2% HNO 3 . U measurement in acidified samples was completed on a Thermo Scientific Element 2 inductively-coupled plasma mass spectrometer (ICP-MS). 
     Reduction of Uranium by Acidimicrobiaceae Bacteria A6 with Ferrihydrite as the Iron Source. 
     NH 4   +  analyses indicate that Acidimicrobiaceae bacteria A6 were only active in the experimental condition which contained live bacteria with NH 4   +  and U.  FIG. 13  illustrates NH 4   +  oxidized over 6 days by Acidimicrobiaceae bacteria A6. Uranium (U) was present in all conditions. Referring to  FIG. 13 , percentages shown are an average of three replicates. Error bars indicate one standard deviation. Referring to  FIG. 13 , over 6 days, bacteria in this condition oxidized an average of 7.0 mg L −1  of NH 4   +  which is equivalent to the removal of 9.8% of the initial NH 4   + . NH 4   +  oxidation was not seen in any of the control conditions which suggests that Acidimicrobiaceae bacteria A6 were not active in these conditions. In the control conditions in which the relevant monoxygenase enzyme was inhibited, the average NH 4   +  concentration increased by 0.31 mg L −1  indicating no NH 4   +  oxidation. Similarly, in the control condition containing autoclaved bacteria, the average NH 4   +  concentration decreased by 0.20 mg L −1  indicating no significant NH 4   +  oxidation. In the control in which no NH 4   +  was added, the concentration of NH 4   +  actually increased from an average concentration of 0.52 mg L −1  to 1.83 mg L −1 . This increase was seen in all three replicates and could indicate nitrogen release through the death and decay of Acidimicrobiaceae bacteria A6 that were deprived of their requisite electron donor NH 4 +. 
     Measurement of U concentrations indicates that biological reduction is one of multiple pathways by which U was removed from solution in these experiments. Across all experimental and control conditions, between 74% and 91% of the added U disappeared from solution within 2 hours of uranyl acetate addition. It is likely that this U(VI) sorbed to ferrihydrite which remained with the bacterial cells through the centrifugation and washing procedure. As a result, the effective initial aqueous U(VI) concentrations varied from 7.2 μM to 13.2 μM U(VI).  FIG. 14  illustrates uranium U(VI) removed from solution over 6 days. Referring to  FIG. 14 , the difference between the “Live and active A6” condition and both the “Autoclaved A6” and the “Limitation of electron donor” conditions is attributable to U reduction by Acidimicrobiaceae bacteria A6. Percentages shown are an average of three replicates. Error bars indicate one standard deviation. 
     Referring to  FIG. 14 , significant U(VI) removal in all conditions continued after the initial removal by sorption. In the three control cases, the lack of NH 4   +  oxidation indicates that Acidimicrobiaceae bacteria A6 were inactive and thus the U(VI) removal in those cases must have been abiotic. It is likely that U diffusion into the matrix of ferrihydrite caused the removal of 51.4% and 65.6% of effective initial aqueous U(VI) over 6 days in the NH 4   + -limited and autoclaved controls, respectively. This two-step uranyl sorption to ferric oxyhydroxides is an established phenomenon (Hsi C K D and Langmuir D 1985  Geochim Cosmochim Ac  49, 1931-1941; Morrison, S J et al., 1995  J Contam Hydrol  17, 333-346, both of which are incorporated herein by reference as if fully set forth). In the enzyme inhibited control, even more U(VI) was abiotically removed over 6 days than in the autoclaved or NH 4   + -limited control. The additional U(VI) removal in this case is likely due to abiotic U(VI) reduction by the added enzyme inhibiting compound, Na 2 S. The sulfide in Na 2 S is able to act as an electron donor for U(VI) reduction (Hua B et al. 2006  Environmental Science  &amp;  Technology  40, 4666-4671, which is incorporated herein by reference as if fully set forth). 
     Referring to  FIG. 14 , comparison of U(VI) removal in the experimental condition and the controls with autoclaved bacteria and with NH 4   +  limitation suggests that biotic reduction of U(VI) by Acidimicrobiaceae bacteria A6 is significant. Without the help of reductants like Na 2 S, the U(VI) removal in vials with live and active bacteria exceeds the highest removal in vials with dead bacteria by 25%. Since these conditions are identical except for the state of the bacteria, it is reasonable to conclude that the additional U(VI) reduction is performed by Acidimicrobiaceae bacteria A6. 
     Example 20. Reduction of Uranium by Acidimicrobiaceae Bacteria A6 with Nontronite as the Iron Source 
     Cell suspension experiments with nontronite, an Fe-rich clay, were performed to study U bioreduction by Acidimicrobiaceae bacteria A6 in an environment rich in electron accepting Fe(III) to promote Acidimicrobiaceae bacteria A6 activity. This experiment was similar to the cell suspension experiments without the addition of an Fe source as described above. Pure culture of Acidimicrobiaceae bacteria A6 in twelve 15-mL vials was washed by centrifugation and resuspension in anaerobic growth medium consisting of NaHCO 3 , KHCO 3 , MgSO 4 .7H 2 O, CaCl 2 , and AQDS. 
     Nontronite (NAu-2) from the Source Clay Repository of the Clay Minerals Society was selected as an electron acceptor for this experiment due to its inability to sorb significant amounts of U at slightly acidic pH. The structural formula of this clay is M +   0.72  [Si 7.55 Al 0.45 ][Fe 3.83 Mg 0.05 ]O 20 (OH 4 ) where M +  represents monovalent interlayer cations (Keeling J L et al. 2000  Clay Clay Miner  48, 537-548, which is incorporated herein by reference as if fully set forth). This clay is 23.4% Fe by weight, of which 99.4% is Fe(III) (Liu D et al. 2011  Geochim Cosmochim Ac  75, 1057-1071, which is incorporated herein by reference as if fully set forth). A stock solution of 20 g L −1  nontronite was prepared using a previously established protocol (Liu et al. 2011, which is incorporated herein by reference as if fully set forth). Briefly, the clay was ground by hand with mortar and pestle before it was soaked in 0.5 mM NaCl overnight. The solution was centrifuged to eliminate all but the 0.02-0.5 μm size fraction. These remaining particles were washed with deionized water and dried in an oven at 100° C. The clay was diluted to 20 g L −1  in deionized water and autoclaved to create a sterile stock solution. This stock solution was added to all 12 vials so that the final concentration of nontronite in each vial was 5 g L −1 . 
     Again, the twelve vials were divided into four groups: one experimental group and three control groups as described in Table 2. To establish the experimental condition with live and active Acidimicrobiaceae bacteria A6, NH 4 Cl and uranyl acetate were added so that the initial concentrations of NH 4   +  and U were 3.726 mM and 12.5 μM, respectively. The first control condition contained bacteria that had been autoclaved, but NH 4 Cl and uranyl acetate were added to these control vials so that they were otherwise identical to the experimental condition. The second control condition contained live bacteria and U, but no NH 4   +  was added to these vials to distinguish the effects of live and active bacteria from live and inactive bacteria. The third control condition contained live bacteria and added NH 4   + , but did not contain any U in order to determine whether the presence of U altered the activity of Acidimicrobiaceae bacteria A6. 
     Fe(II) was measured at intervals of 24 to 48 hours throughout the experiment to gauge Fe-reducing activity of Acidimicrobiaceae bacteria A6. 20 μL of unfiltered samples were deposited in 1 mL of 0.5N HCl. After 15 minutes, Fe(II) was measured using the well-established ferrozine method (Komlos J and Jaffe P R, 2004  Biodegradation  15, 315-325, which is incorporated herein by reference as if fully set forth). Briefly, Fe(II) was measured by adding 30 μL of HCl-extracted sample to 1.5 mL of ferrozine and measuring the absorbance after 30 minutes at a wavelength of 562 nm in a Spectronic Genesys 2 spectrophotometer. Absorbances were converted to molar concentrations of Fe(II) using a standard curve. 
     
       
         
           
               
             
               
                 TABLE 2 
               
             
            
               
                   
               
               
                 Experimental and control conditions in U bioreduction 
               
               
                 experiment with nontronite as Fe source 
               
            
           
           
               
               
               
               
               
            
               
                   
                   
                 Control 1: 
                   
                   
               
               
                   
                   
                 Autoclaved 
                 Control 2: 
                 Control 3: 
               
               
                   
                 Experimental 
                 Bacteria 
                 No NH 4 + 
                 No U 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
            
               
                 NH 4 +, mM 
                 3.726 mM 
                 3.726 mM 
                 0 mM 
                 3.726 mM 
               
               
                 Initial 
                 12.5 ± 2.3 
                 11.8 ± 0.3 
                 12.4 ± 0.5 
                 0 
               
               
                 total U, μM 
               
               
                 Nontronite, 
                 5 
                 5 
                 5 
                 5 
               
               
                 g L −1   
               
               
                 Acidimicrobiaceae 
                 Live 
                 Dead 
                 Live 
                 Live 
               
               
                 bacteria A6 
               
               
                   
               
            
           
         
       
     
     Concentrations of Fe(II) measured by the ferrozine method include aqueous Fe(II) and approximately 74% of the Fe(II) sorbed to nontronite surfaces (Zhang G X et al. 2009  Geochim Cosmochim Ac  73, 3523-3538, which is incorporated herein by reference as if fully set forth). Therefore, these measurements were used only in relation to each other to track bacterial Fe(II) production indicating Acidimicrobiaceae bacteria A6 activity. U, NH 4   + , nitrate (NO 3   − ), and nitrite (NO 2   − ) concentrations were measured after 0, 7, and 11 days to determine activity of Acidimicrobiaceae bacteria A6. Total U and U(VI) concentrations were measured by ICP-MS as described above. NH 4   + , NO 3   − , and NO 2   −  concentrations were measured on a Dionex™ Ion Chromatograph ICS3000. Columns used for NH 4   +  were identical to those described above. NO 3   −  and NO 2   −  analysis was carried out with an AS-22 column, an AG-22 guard column, and an ASRS 300 (4 mm) suppressor. It had previously been determined that NH 4   +  could sorb to nontronite, so total NH 4   +  was also measured. Sorbed NH 4   +  was extracted from nontronite by adding 20 μL samples from each vial to 1 mL of 0.5N HCl. After 20 hours, the acid extractions were filtered on 0.2 μm nylon filters and preserved at 4° C. until the NH 4   +  concentrations were measured on a Dionex™ Ion Chromatograph. 
     Purity of bacterial cultures was confirmed after the experiment using DNA isolation and quantitative polymerase chain reaction (qPCR) assay. 1 mL samples of the slurry containing bacteria, growth medium, and nontronite were centrifuged at 1000 rpm for 10 minutes before DNA was extracted from the pellets using the FastDNA® spin kit for soil (MP Biomedicals, USA) as described by the manufacturer. Total bacterial abundance was represented by the number of copies of 16S rRNA genes quantified by qPCR with primers BACT1369F-PROK1492R and the TaqMan probe 1389F (Suzuki M T et al. 2000  Appl Environ Microb  66, 4605-4614, which is incorporated herein as if fully set forth). Acidimicrobiaceae bacteria A6 bacteria were enumerated with the primer set acm342f-439r (Huang S and Jaffe P R 2015  Biogeosciences  12, 769-779, which is incorporated herein by reference as if fully set forth). Several other U-reducing species were also targeted to check the samples for contamination. To investigate the presence of sulfate and Fe reducing bacteria, 6-Proteobacteria was enumerated by qPCR using primer set 361F-685R and the TaqMan probe 1839F (Stults J R et al. 2001  Appl Environ Microb  67, 2781-2789, which is incorporated herein by reference as if fully set forth).  Geobacter , the dominant Fe-reducing microorganisms in sediment environments, was enumerated by qPCR primer set 561F-825R and TaqMan probe Gbc2 (Stults et al. 2001, which is incorporated herein by reference as if fully set forth).  Anaeromyxobacter  spp., a metal-reducing group of bacteria, was enumerated with the 60F-461R primer pair (Petrie L et al. 2003  Appl Environ Microb  69, 7467-7479, which is incorporated herein by reference as if fully set forth). All qPCR experiments were carried out using a StepOnePlus™ Real-Time PCR System (Life Technologies, USA). For DNA quantification, each qPCR mixture (20 μL) was composed of 10 μL of SYBR Premix Ex Taq® II (Takara, Japan), 0.8 μL of 10 μM of each primer, and ˜10 ng DNA template. Each assay contained a set of standards produced by serial dilution of plasmids containing specific target genes, independent triplicate templates for each slurry sample, and triplicate no template controls (NTC). 
     Reduction of Uranium by Acidimicrobiaceae Bacteria A6 with Nontronite as the Iron Source. 
     Measurements of Fe(II) confirm that Acidimicrobiaceae bacteria A6 remain active in the presence of U and nontronite.  FIG. 15  illustrates reduction of Fe in nontronite over 12 days. Values shown are averages of three replicates. Error bars indicate one standard deviation. Referring to  FIG. 15 , Fe(II) production was similar in rate and extent in conditions with and without U, indicating that the addition of 10 μM uranyl acetate is not toxic to Acidimicrobiaceae bacteria A6. In cases with and without added U, Acidimicrobiaceae bacteria A6 were able to use the Fe(III) in nontronite as an electron acceptor for NH 4   +  oxidation. Still referring to  FIG. 15 , in the condition with autoclaved Acidimicrobiaceae bacteria A6, the Fe(II) remained constant throughout the 12-day experiment. This result indicates that there was no abiotic Fe cycling occurring in the vials. 
     Results indicate that Acidimicrobiaceae bacteria A6 can reduce U in addition to Fe.  FIG. 16  illustrates total U and U(VI) concentrations over 11 days. Values shown are averages of three replicates. Error bars indicate one standard deviation. Referring to  FIG. 16 , essentially all of the U(VI) disappeared from solution in 7 days in the condition with live Acidimicrobiaceae bacteria A6, NH 4   + , and U. This change cannot be attributed to activity of other bacteria, as qPCR results indicated that only Acidimicrobiaceae bacteria A6 were present in all vials with live bacteria. Referring to  FIG. 16 , this change in U(VI) also cannot be attributed to sorption of U to nontronite or ingredients of the growth medium because the aqueous U(VI) concentrations remained essentially equivalent to total U concentrations in vials in which Acidimicrobiaceae bacteria A6 had been killed. The similarity between U(VI) and total U in the condition with autoclaved bacteria also demonstrates that no abiotic U reduction occurred. The difference between vials with dead and live Acidimicrobiaceae bacteria A6 indicate that Acidimicrobiaceae bacteria A6 can reduce aqueous U(VI) to U(IV) solids. It has previously been determined that  Shewanella oneidensis  MR-1 are also able to completely reduce U in the presence of nontronite (Zhang G X et al 2009, which is incorporated herein by reference as if fully set forth).  Shewanella oneidensis  MR-1 are only able to reduce U in the presence of AQDS; though this present study did not examine the effect of AQDS on U reduction by Acidimicrobiaceae bacteria A6, it is likely that they similarly require AQDS (Zhang G X et al 2009, which is incorporated). 
     In all vials except one, the total U measured by bicarbonate extraction decreased over 11 days. This change likely resulted from the slow incorporation of U into the structure of nontronite where it would be unaffected by the extraction. 
     Unexpectedly, Fe and U reduction occurred in vials without NH 4   +  for the live Acidimicrobiaceae bacteria A6 to oxidize. In these vials, the Fe(II) increased and U(VI) decreased more slowly and to a lesser extent over 12 days than they did in vials with NH 4   + . These results could indicate that the live Acidimicrobiaceae bacteria A6 area able to use a structural component of the nontronite as an electron donor rather than NH 4   + . Alternatively, biomass turnover and decomposition could provide the remaining live Acidimicrobiaceae bacteria A6 with NH 4   + . In this case, the lower proportion of live bacteria and the lower concentrations of NH 4   +  would explain the slower rates and smaller extent of Fe and U reduction. 
     Example 21. Bioreduction of Cu(II) by Feammox 
       FIGS. 17A-17B  illustrate oxidation of NH 4   +  ( FIG. 17A ) and reduction of Cu (II) ( FIG. 17B ) by Feammox. Around 10 4  cell per ml of pure A6 were incubated in inorganic NH 4   + -Ferric iron liquid medium with 20 ppm Copper (II) chloride (CuCl 2 ) under anaerobic conditions for 40 days. Referring to  FIG. 17B , 64.2% of Cu(II) was reduced and the total dissolved Cu [including Cu(II) and Cu(I)] decreased by 23.1% over the incubation period, while the concentrations of Cu(II) and Cu(I) remained constant for the autoclaved treatment. 
     After the incubation, the samples were aerated to reoxidize the reduced copper. This resulted in full recovery or the initial Cu(II). 
     Example 22. Investigation of Selected Organic Contaminants Biodegradation by Feammox 
     Around 10 4  cell per ml of pure A6 were incubated in inorganic NH 4   + -Ferric iron liquid medium with 1000 ppb Trichloroethylene (TCE)/1000 ppb tetrachloroethylene (PCE)/100 ppb benzene/100 ppb phenanthrene under anaerobic conditions for 40 days. Six 15-mL vials of incubations were conducted for each organic contaminant. The six vials were divided into three groups: two different control conditions and the experimental condition as shown in Table 3. 
     
       
         
           
               
             
               
                 TABLE 3 
               
             
            
               
                   
               
               
                 Experimental and control conditions in selected 
               
               
                 organic contaminants biodegradation by Feammox 
               
            
           
           
               
               
               
               
            
               
                   
                   
                 Control 1: 
                   
               
               
                   
                   
                 Enzyme 
                 Control 3: 
               
               
                   
                 Experimental 
                 Inhibited 
                 No NH 4 + 
               
               
                   
                   
               
            
           
           
               
               
               
               
            
               
                 NH 4 +, mM 
                 2.96 ± 0.12 
                 2.97 ± 0.05 
                 0.02 ± 0.01 
               
               
                 Initial total 
                 1000/1000/ 
                 1000/1000/ 
                 1000/1000/ 
               
               
                 TCE/PCE/benzene/ 
                 100/100/ 
                 100/100/ 
                 100/100/ 
               
               
                 phenathrene, ppb 
               
               
                 Na 2 S, μM 
                 0 
                 50 
                 0 
               
               
                 Acidimicrobiaceae 
                 Live 
                 Live 
                 Live 
               
               
                 bacteria A6 
               
               
                   
               
            
           
         
       
     
     Subsamples were taken on day 0, 12, 22, 30 and 37 under anoxic conditions. Samples for NH 4   +  analysis were filtered using 0.2 um nylon filters and stored at 4° C. until they were analyzed using a Dionex™ Ion Chromatograph ICS3000 with a CS-16 column, a CS-16 guard column, and a CERS 500 (4 mm) suppressor. TCE, PCE, benzene or phenathrene were measured with a Thermo Scientific Vanquish UHPLC system.  FIGS. 18A-18D  illustrate an effect of biodegradation of trichloroethylene (TCE) ( FIG. 18A ), tetrachloroethylene (PCE) ( FIG. 18B ), benzene ( FIG. 18C ) and phenanthrene ( FIG. 18D ) by Feammox. Around 10 4  cell per ml of pure A6 were incubated in inorganic NH 4   + -Ferric iron liquid medium with 1000 ppb Trichloroethylene (TCE) ( FIG. 18A ), 1000 ppb tetrachloroethylene (PCE) ( FIG. 18B ), 100 ppb benzene ( FIG. 18C ), 100 ppb phenanthrene ( FIG. 18D ) under anaerobic conditions for 40 days. 
     Referring to  FIGS. 18A-18B , TCE, PCE, benzene and phenanthrene degradation were found in all Feammox active samples, but not in the samples that included Feammox enzyme inhibitor (sodium bisulfide) and samples without NH 4   + . It was observed that 36% of TCE, 28% of PCE, 20% of benzene and 8.8% of phenanthrene was degraded over an incubation period of approximately one month. NH 4   +  oxidation was not seen in any of the control conditions, which suggests that Acidimicrobiaceae bacteria A6 were not active in these conditions that also did not result in the degradation of the organics. 
     It should be noticed that all of the above are extremely recalcitrant compounds, especially in anaerobic environments. Higher degradation rates can be achieved by having larger bacterial numbers. The bacterial numbers for higher degradation may be 10 6 , 10 8  or 10 10  cells per ml of pure A6. 
     Example 23. Characteristics of Feammox Acidimicrobiaceae Bacterium A6 and Enzyme Identification 
     Feammox bacteria were isolated in inorganic NH 4   + -Ferric iron solid medium from wetland soils collected in New Jersey as described in Examples 2-17. The bacteria were cultured in liquid and solid media. 
     Inorganic NH 4   + -Ferric iron liquid medium contained the following components per liter: 177 mg NH 4 Cl, 77.9 mg (NH 4 ) 2 SO 4 , 19.8 mg NaHCO 3 , 71.0 mg KHCO 3 , 9.00 mg KH 2 PO 4 , 100 mg MgSO 4 .7H 2 O, and 60.0 mg CaCl 2 .2H 2 O. 3.37 g ferrihydrite, 18.42 mg antraquinone-2,6-disulfonate (AQDS) and 1 mL trace element solution and vitamin (ATCC®). Inorganic NH 4   + -Ferric iron solid medium was prepared with liquid medium and 0.8% agar, 0.2 mL 3.37 g L −1  ferrihydrite was spread on the surface. 
       FIGS. 19A-19D  illustrate A6 bacterial cultures and cells.  FIG. 19A  illustrates growth of the A6 bacterium in the liquid medium. Cultures of A6 became increasingly turbid and black-colored (due to accumulation of ferrous iron) during incubation. Culture doubling times of the A6 isolate were 10.2 days.  FIG. 19B  illustrates A6 growth on the solid inorganic NH 4   + -ferric iron medium. Colonies of A6 are displayed with black spot (iron-encrusted) on the solid medium.  FIGS. 19C-19D  show rod-shaped A6 cells. The cells were 1.5-3 mm long by 0.5 mm wide. The A6 bacteria are gram-positive bacteria. On the solid medium, colonies with black spot (accumulation of ferrous iron) were collected and transferred to inorganic NH 4   + -Ferric iron liquid medium. Their Feammox activity was verified by the NH 4   +  oxidation and iron reduction rates. A strain of Actinobacteria was isolated and identified as Feammox bacteria, and named Feammox Acidimicrobiaceae bacterium A6. The pH optimum for growth of A6 was 4.5, but reasonable activity was detected from pH 2 to 7. Its temperature optimum was 25° C., and a doubling time of 10.2 days. A  13 C labeled CO 2  amendment was conducted, and the  13 C in cells of A6 increased from 1.80% to 10.3% after 14 days incubation. In a separate incubation,  15 NH 4 Cl was added with a final concentration of 0.5 mmol L −1 , and 0.133 mmol L −1  of  15 NO 2   −  was detected, while no  15 NO 3   −  was produced. 
     The genome size and guanine-cytosine content of A6 are 3.3 mega base pairs (Mb) and 52%. The Feammox ammonium Monooxygenase (FMO) gene (SEQ ID NO: 8), was identified. FMO is considered to be the functional gene coding ammonium oxidation coupled to ferric iron reduction in A6. 
     Isolation, Purification and Cultivation of Bacteria: Continuous Flow Membrane Feammox Enrichment Reactor 
     Soil samples from wetland soils collected in New Jersey were inoculated into a continuous flow membrane reactor, which was operated under anaerobic conditions by constantly purging N 2  trough the reactor&#39;s headspace at a room temperature (25° C.), and with a 48 hour hydraulic retention time.  FIG. 11  illustrates a scheme of a membrane reactor for NH 4   +  oxidation via Feammox. Referring to this figure, 1 refers to the feed solution, 2 refers to the feed pump, 3 refers to the membrane module, 4 refers to the floater connected to an electrical on/off switch, 5 refers to the ceramic diffuser, 6 refers to the N 2  supplier, 7 refers to the water bath, 8 refers to outflow, and 9 refers to the outflow pump. Inorganic NH 4   + -Ferric iron liquid medium contained the following components per liter: 177 mg NH 4 Cl, 77.9 mg (NH 4 ) 2 SO 4 , 19.8 mg NaHCO 3 , 71.0 mg KHCO 3 , 9.00 mg KH 2 PO 4 , 100 mg MgSO 4 .7H 2 O, and 60.0 mg CaCl 2 .2H 2 O. 3.37 g ferrihydrite, 18.42 mg AQDS and 1 mL trace element solution and vitamin (ATCC®). pH was controlled at around 4-5, and dissolve oxygen was &lt;0.10 mg/L. Samples form the outflow were collected every two days, and sludge samples from reactor were collected and kept at −20° C. for molecular biology analysis. 
     454 pyrosequencing was performed with samples collected from the membrane reactor after 150 days of reactor operation with Domain-specific primers, targeting the V3-V5 region of the 16S rDNA of bacteria were amplified following methods suggested by Pinto et al. 2012, PLoS One 7: 43093, which is incorporated herein by reference as if fully set forth. And the results were compared with samples from previous incubation on days 0, 30, 90, 160. Acidimicrobiaceae bacterium A6, which belongs to the Actinobacteria phylum, was the dominant species in the incubation experiments after 180 days of incubation (14.8% in terms of cell numbers) and increased in the membrane reactor after 150 days of operation (40.2% in terms of cell numbers). 
     Growth on Solid Media: 
     Inorganic NH 4   + -Ferric iron solid media was prepared with liquid media and 0.8% agar, 0.2 mL 3.37 g L −1  ferrihydrite was spread on the surface. 
     On the solid medium, colonies with black spot (accumulation of ferrous iron) were collected and transferred to inorganic NH 4   + -Ferric iron liquid media.  FIG. 20  illustrates anaerobic oxidation of ammonium by the A6 isolate. Referring to  FIG. 20 , bacterial cells were incubated for 20 days on the inorganic, NH 4   + -ferric iron media, pH 4.5. The A6 concentration was 10 5  copies per mL. 0.738 mM of NH 4   +  was oxidized and 0.710 mM of NO 2   −  was produced. Still referring to  FIG. 20 , the Feammox activity of the bacterial cells was verified by the NH 4   +  oxidation and iron reduction rates. A strain of Actinobacteria was isolated and identified as Feammox bacteria, and named Feammox Acidimicrobiaceae bacterium A6. Referring to  FIGS. 19C-19D , microscopic examination showed that cells were rod-shaped, 1.5-3 mm long by 0.5 mm wide, gram-positive. 
     Growth on Liquid Media: 
     In ferric iron-containing liquid media, cultures of A6 became increasingly turbid and black-coloured (due to the accumulation of ferrous iron) during incubation. Microscopic examination showed that endospores were produced. The pH optimum for growth of isolate A6 were 4.5, and its temperature optimum was 25° C. Under optimum conditions of pH and temperature, culture doubling times of isolate A6 were 10.2 days. 
     Anaerobic Oxidation of Ammonium—Ammonium Oxidation Rates 
     The A6 isolate was incubated for 20 days on the inorganic, NH 4   + -Ferric iron media, at a pH 4.5. The A6 bacterial concentration was 10 5  copies per mL.  FIG. 20  illustrates concentrations of NH 4   +  and NO 2   −  during anaerobic oxidation of ammonium. After incubation, 0.738 mM of NH 4   +  was oxidized and 0.710 mM of NO 2   −  was produced. 
     Effect of NH 4   +  Concentration on Feammox. 
       FIG. 21  illustrates an effect of NH 4   +  concentration on its consumption by A6. Referring to this figure, the isolate A6 was incubated for 20 days in the inorganic NH 4   + -Ferric iron media, pH4.5. A6 included 10 5  copies per mL. 10 mM ferrihydrite and three different amounts (10 mM, 5 mM, 1 mM) of NH 4   +  were added initially. Higher NH 4   +  consumption rates by Feammox were found for higher NH 4   +  concentration incubation. 
       15 N Isotope Incubation 
       15 NH 4 Cl was added with a final concentration of 0.5 mmol L −1  and 0.133 mmol L −1  of  15 NO 2   −  was detected after 7 days incubation, while no  15 NO 3   −  was produced. The data was summarized in Table 4. 
     
       
         
           
               
             
               
                 TABLE 4 
               
               
                   
               
               
                 Summary of  15 N isotope incubation 
               
               
                   
               
             
            
               
                   
               
            
           
           
               
               
               
               
            
               
                   
                   
                   14 N 
                   15 N 
               
               
                   
                   
               
               
                   
                 D1-NH 4 + 
                 0.892 
                 0.108 
               
               
                   
                 D1-NO 2 − 
                 0.995 
                 0.005 
               
               
                   
                 D1-NO 3 − 
                 0.995 
                 0.005 
               
               
                   
                 D7-NH 4 + 
                 0.847 
                 0.153 
               
               
                   
                 D7-NO 2 − 
                 0.757 
                 0.243 
               
               
                   
                 D7-NO 3 − 
                 0.992 
                 0.008 
               
               
                   
                   
               
            
           
           
               
               
               
               
            
               
                   
                   
                 D1 
                 D7 
               
               
                   
                   
               
               
                   
                 15N-NH4+ 
                 0.5192 
                 0.3862 
               
               
                   
                 15N-NO2− 
                 0.0001 
                 0.1330 
               
               
                   
                 15N-NO3− 
                 0.0001 
                 0.0001 
               
               
                   
                   
               
            
           
         
       
     
     The data confirmed that NO 2   −  is the main product of NH 4   +  oxidation in Feammox reaction. 
     Reduction of Ferric Iron Reduction Rates: 
       FIG. 22  illustrates iron reduction rates. The A6 cells were incubated for 20 days on the inorganic, NH 4   + -ferric iron medium, pH 4.5. The A6 concentration was 10 5  copies per mL. After incubation, 4.330 mM of NH 4   +  was oxidized, and 4.317 mM of Fe(II) was produced. 
     Effect of Iron Concentration on Feammox: 
       FIG. 23  illustrates an effect of iron concentration on Feammox. Referring to  FIG. 23 , the isolate A6 was incubated for 20 days in the inorganic NH 4   + -Ferric iron media, at pH4.5. A6 included 10 5  copies per mL. 2 mM NH 4   +  and three different amounts (20 mM, 10 mM, 2 mM) of ferrihydrite were added initially. No significant different of NH 4   +  consumption by Feammox with different ferrihydrite amended during incubation was found. As long as there was sufficient iron included in the media, no effect of iron concentration on Feammox was observed. 
     Determination of pH and Temperature Optima: 
     Isolate A6 incubation for 20 Days under different pH gradient in inorganic, NH 4   + -Ferric iron media. A6 is 105 copies per mL. pH adjust to 2, 4.5, 6.5, 8.0 by HCl and NaOH.  FIGS. 25A-25B  illustrate determination of the effect of pH on NH 4   +  consumption ( FIG. 25A ) and bacterial growth ( FIG. 25B ). pH=2 results are reported in the far left bar of each of days 0, 5, 10, 15 and 20 panels. pH=4.5 results are reported in the left middle bar of each of days 0, 5, 10, 15 and 20 panels. pH=6.5 results are reported in the right middle bar of each of days 0, 5, 10, 15 and 20 panels. pH=8 results are reported in the far right bar of each of days 0, 5, 10, 15 and 20 panels. The pH optimum for growth of A6 was 4.5, but reasonable activity was detected from pH 2 to 7. 
     Temperature Gradient: 
       FIG. 24  illustrates the relative ammonium removal rate constants (k) by Acidimicrobiaceae-bacteria A6 at 15° C., 20° C. and 35° C. Referring to this figure, the highest rate was measured at 20° C., k=0.03 hr −1 , followed by 35° C., k=0.019 hr −1 , and 15° C., k=0.01 hr −1 . 
     Utilization of Organic Substrates: 
     Growth yields of isolate A6 have no growth difference in media containing glycerol, citric acid and glutamic acid with in control cultures NaHCO 3  added. The data shows that A6 is an autotroph utilizing inorganic carbon but the presence of different organic carbons does not affect its growth. 
     It was observed that culturing of the isolate A6 in yeast extract media required one or more additional growth factors. 
     Heavy Metal Tolerance: 
     This gram-positive isolate was able to grow in media containing elevated concentrations of the heavy metals tested. The A6 isolate was tested for the ability to grow in the media supplemented with 100 μM-100 mM of copper, 10-200 mM of zinc, 20-100 μM of uranium, 10-200 mM of ferric iron or 10-200 mM of ferrous iron. It was observed that the isolate A6 grew in 260 mM on ferric iron. However, addition of ferrous iron did not inhibit the bacterial growth. Growth also occurred in the presence of 100 mM, but not 200 mM, copper. It was also observed that 50 mM zinc inhibited growth. The A6 bacteria was growing in the presence of the tested concentrations of uranium but it was found that uranium was toxic to the bacterial cells at 200 μM. 
     Autotrophic growth and CO2 fixation—assimilation of CO 2  in cultures of isolate A6: A6 was able to grow in organic carbon-free liquid media. A  13 C labeled CO 2  amendment was conducted with a Thermo MAT 253™ stable isotope ratio mass spectrometer, and the  13 C in cells of A6 increased from 1.80% to 10.3% after 14 days incubation. 
     
       
         
           
               
             
               
                 TABLE 5 
               
             
            
               
                   
               
               
                 Summary of assimilation of CO 2   
               
            
           
           
               
               
               
               
               
            
               
                   
                 Cell (with methanol wash) 
                   
                 DNA 
                   
               
            
           
           
               
               
               
               
               
            
               
                   
                   12 C 
                   13 C 
                   12 C 
                   13 C 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
               
            
               
                   
                 Day 0 
                 98.2% 
                 1.80% 
                 98.9% 
                 1.10% 
               
               
                   
                 Day 14 
                 89.7% 
                 10.3% 
                 82.0% 
                 18.0% 
               
               
                   
                   
               
            
           
         
       
     
     Screening of RuBisCo (Ribulose-1,5-Bisphosphate Carboxylase/Oxygenase) Genes: 
     RuBisCO genes were amplified from cell lysates of A6. Both cbbL and cbbM genes were successfully amplified. 
     Full Sequencing and Functional Gene-Single-Copy Gene Analysis: 
       FIG. 26  illustrates a schematic representation of the genome of the Acidimicrobiaceae Feammox bacterium A6. The genome size and guanine-cytosine content of A6 are 3.3 mega base pairs (Mb) and 52%. Genotypic traits are summarized in Table 6. 
     
       
         
           
               
             
               
                 TABLE 6 
               
             
            
               
                   
               
               
                 Genotypic traits 
               
            
           
           
               
               
               
            
               
                   
                 Attribute 
                 Value 
               
               
                   
                   
               
            
           
           
               
               
               
            
               
                   
                 Genome size (bp) 
                 3,106,468 
               
               
                   
                 Plasmid size (bp) 
                 106,011 
               
               
                   
                 DNA Coding region (bp) 
                 2,991,461 
               
               
                   
                 DNA G + C content (bp) 
                 1,709,039 
               
               
                   
                 RNA genes 
                 42 
               
               
                   
                 rRNA operons 
                 2 
               
               
                   
                 Protein-coding genes 
                 2032 
               
               
                   
                 Pseudo genes 
                 58 
               
               
                   
                 Genes with function prediction 
                 1579 
               
               
                   
                 Genes assigned to COGs 
                 1392 
               
               
                   
                 Genes assigned Pfam domains 
                 1497 
               
               
                   
                 Genes with transmembrane 
                 538 
               
               
                   
                 helices 
               
               
                   
                   
               
            
           
         
       
     
     Functional Gene: 
     The gene encoding Feammox ammonium Monooxygenase (FMO) having a sequence of SEQ ID NO: 12 was identified. The gene was located in the bacterial plasmid. The FMO is considered to be the functional gene coding ammonium oxidation coupling to ferric iron reduction in A6. 
     FMO Activity. 
       FIG. 27  illustrates the FMO activity. Referring to  FIG. 27 , isolate A6 was incubated for 20 days under pH 4.5, in inorganic NH 4   + -Ferric iron media. Copy number of Feammox gene, FMO-a, was analyzed during the incubation which showed active Feammox reaction. It was observed that that FMO activity increased as total microbial as well as Acidimicrobiaceae Feammox bacterium A6 activity increased. 
       FIG. 28  illustrates oxidation of NH 4   +  by Acidimicrobiaceae bacterium A6 and the FMO activity in the presence (without FMO-a) and absence (with FMO-a) of a broad enzyme inhibitor (NaS). Referring to  FIG. 28 , it was observed that the NH 4   +  oxidation rate decreased in the samples without FMO-a. 
     Phylogenetic Analysis: 
     According to the phylogenetic analysis, Acidimicrobiaceae bacterium A6), belonging to the Acidimicrobiaceae family, whose closest cultivated relative is  Ferrimicrobium acidiphilum  (with 92% identity) and  Acidimicrobium ferrooxidans  (with 90% identity). 
     Example 24. Feammox Applications 
     Feammox process could be applied for waste water treatment for ammonium removal without the need to supply oxygen. Oxygen supply is the highest energy cost in waste treatment plants. The process may also be used in the design of engineered wetlands for nitrogen removal. That would be important in the agricultural and livestock industry. There might be many other applications. 
     Ammonium oxidation requires oxygen. Anammox process works with nitrite, but it requires high temperatures (around 82° F.). Since the bacterium was isolated at a New Jersey wetland, it is reasonable that it will function at lower temperatures. This is important for waste treatment, since in the winter waste water temperatures are around 40° F. Feammox may be applied for developing more temperature robust treatment processes that do not need aeration. Means to recycle iron and/or use scrap grounded up iron may be developed to be supplied for Feammox. The process similar to the one tested in incubation experiments will be utilized in a simple prototype reactor. Table 6 describes NH 4   +  removal using the reactor illustrated in  FIG. 11  contrast Anammox and Feammox. 
     
       
         
           
               
             
               
                 TABLE 7 
               
             
            
               
                   
               
               
                 Comparison of Feammmox and Anammox reactors 
               
            
           
           
               
               
               
               
            
               
                   
                 Feammox reactor 
                 Anammox reactor 
                 Conditions 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
               
            
               
                 Temperature 
                 20-25° 
                 C. 
                 28-35° 
                 C. 
                 Feammox con work 
               
               
                   
                   
                   
                   
                   
                 if T~15° C. 
               
            
           
           
               
               
               
               
            
               
                 pH 
                 4.5-6 
                 cirumneutral 
                 Feammox can work 
               
               
                   
                   
                   
                 if pH~2 
               
            
           
           
               
               
               
               
               
            
               
                 Aeration time 
                 0 
                 h/day 
                 Non or 1.5 h/day 
                 Feammox require 
               
               
                   
                   
                   
                   
                 Fe(III) 
               
            
           
           
               
               
               
               
               
               
            
               
                 Doubling time 
                 8-12 
                 days 
                 10-12 
                 days 
                 Both are slow 
               
               
                   
                   
                   
                   
                   
                 growing bacteria 
               
            
           
           
               
               
               
               
            
               
                 NH 4 + removal 
                 85% 
                 41% (no aeration)   
                 NH 4 + inflow 
               
               
                   
                   
                 72% (with aeration) 
                 concentration 5 mM; 
               
               
                   
                   
                   
                 Retention Time 48 h 
               
               
                   
               
            
           
         
       
     
     It was shown that the Feammox reactor is as efficient if not more than the anammox reactor. Finally, sludge was mixed from the Feammox and Anammox reactors, showing that a combined Feammox/Anammox mode is feasible and does not require partial aeration, which is required by Anammox to convert some NH 4   +  to NO2-, which in the combined process is done by Feammox. Operating conditions were different for the Feammox/Anammox reactor. 
     A combined Feammox/Anammox process results in less iron demand than a pure Feammox process. Anammox with 20% Feammox sludge may result in 70% NH 4 + removal without aeration. 
     Example 25. Feammox in Electrogenic Microbial Reactors 
     Electrogenic microbial reactors such as Microbial Fuel Cells (MFCs) and Microbial Electrolysis cells (MECs) are bioelectrochemical systems that extract energy from a substrate (Call and Logan 2011  Biosen. Bioelectron.  26(11): 4526-4531, which is incorporated herein by reference as if fully set forth). This process harvests electrons biologically, which are then transferred to the anode that functions as the terminal electron acceptor for the microorganisms in the system, and H 2  is produced at the anode.  FIG. 29  illustrates a scheme of the electrogenic microbial reactor. Referring to  FIG. 29 , the reactor includes a vial, a graphite anode connected via titanium wire to the positive terminal of the power supply, a stainless steel catode connected via stainless steel wire to the negative terminal of the power supply. MECs require a small potential applied from an external power source (E AP &gt;0.25 V), resulting in H 2  production at the anode (Logan, Hamelers et al. 2006  Environ. Sci. Technol.  40(17):5181-5192; Call and Logan 2008  Environ. Sci. Technol.  42(9):3401-3406; Call and Logan 2011, all of which e incorporated by reference as if fully set forth). When the anode in a MFC or MEC works in place of a finite electron acceptor (i.e., Fe(III)), the bacterial growth is no longer limited by the consumption of that electron acceptor. 
     Some electrogenic iron reducing microorganisms; e.g.,  Geobacter  sp., are capable of transferring the electrons to an anode instead of Fe(III) and grow in MECs (Logan 2009, which is incorporated herein by reference as if fully set forth). Thus, we have tested A6&#39;s ability to grow in small MECs has been tested. It was found that under constant mixing, and with a voltage input of 0.7V, MECs seeded with a pure culture of A6 to which 5 mM ammonium was added produced a current density (I) that increased from 0.02 A/m 3  to up to ˜36 A/m 3 , while the autoclaved control increased to only 1.3 A/m 3  (Call and Logan 2011, which is incorporated herein by reference as if fully set forth). The A6 biomass increased from 10 4  copies of DNA/ml to 9×10 5  over 14 days of operation. An electron shuttling compound, AQDS (Anthraquinone-2,6-disulfonate) had to be added to the solution, since unlike  Geobacter , A6 does not seem to colonize the anode. When an electron shuttling compound like AQDS is added, the electron will be transferred from NH 4   +  to AQDS in solution and then to the anode. Hence, MECs and MFCs may be the ideal Feammox reactor configuration for NH 4   +  removal from wastewater via Feammox that solves the Fe(III) supply problem. Other configurations and materials can also be used to construct MECs as well as MFCs. 
     Although the equation in  FIG. 29  shows that the solution pH should decrease while NH 4   +  is being oxidized, it was observed that pH increases. Our hypothesis is that this is due to the CO 2  consumption by A6, which is an autotroph. Hence, CO 2  control may be for the growth of a pure A6 culture. CO 2  addition should not be needed when organics are degraded simultaneously since CO 2  is produced during the biodegradation of organics. 
     Example 26. Addition of Elemental Sulfur Stimulates Feammox Activity 
     Standard Feammox incubations were conducted with the addition of S(0). It was shown that by adding S(0) to the medium the growth rate of Acidimicrobiaceae bacterium A6 was increased, as well as the removal of ammonium, and the production of Feammox related enzymes (Accession numbers AF5136601-AF5136621). SEQ ID NOS of amino acid and nucleic acid sequences Feammox related enzymes ERCFMO_0001-FERCFMO_0021 (correspond to AF5136601-AF5136621) are listed in Table 8 below. 
     
       
         
           
               
             
               
                 TABLE 8 
               
             
            
               
                   
               
               
                 SEQ ID NOS of FMO Related Enzymes and Genes 
               
            
           
           
               
               
               
               
            
               
                   
                   
                 SEQ ID NO 
                 SEQ ID NO 
               
               
                   
                 FMO clone* 
                 (Gene) 
                 (Enzyme) 
               
               
                   
                   
               
            
           
           
               
               
               
               
            
               
                   
                 ERCFMO_0001 
                 8 
                 29 
               
               
                   
                 ERCFMO_0002 
                 9 
                 30 
               
               
                   
                 ERCFMO_0003 
                 10 
                 31 
               
               
                   
                 ERCFMO_0004 
                 11 
                 32 
               
               
                   
                 ERCFMO_0005 
                 12 
                 33 
               
               
                   
                 ERCFMO_0006 
                 13 
                 34 
               
               
                   
                 ERCFMO_0007 
                 14 
                 35 
               
               
                   
                 ERCFMO_0008 
                 15 
                 36 
               
               
                   
                 ERCFMO_0009 
                 16 
                 37 
               
               
                   
                 ERCFMO_0010 
                 17 
                 38 
               
               
                   
                 ERCFMO_0011 
                 18 
                 39 
               
               
                   
                 ERCFMO_0012 
                 19 
                 40 
               
               
                   
                 ERCFMO_0013 
                 20 
                 41 
               
               
                   
                 ERCFMO_0014 
                 21 
                 42 
               
               
                   
                 ERCFMO_0015 
                 22 
                 43 
               
               
                   
                 ERCFMO_0016 
                 23 
                 44 
               
               
                   
                 ERCFMO_0017 
                 24 
                 45 
               
               
                   
                 ERCFMO_0018 
                 25 
                 46 
               
               
                   
                 ERCFMO_0019 
                 26 
                 47 
               
               
                   
                 ERCFMO_0020 
                 27 
                 48 
               
               
                   
                 ERCFMO_0021 
                 28 
                 49 
               
               
                   
                   
               
               
                   
                 *Clone refers to the clone of uncultured bacterium particulate methane monooxygenase/ammonia monooxygenase subunit A, partial cds, also referred to as the FMO. 
               
            
           
         
       
     
     Based on the findings that Feammox can degrade TCE/PCE and PAHs, it was investigated whether one or a contortion of these enzymes are involved in these reactions. 
     Table 9 describes an increase in copy numbers of the genes encoding clones of the FMO enzyme in response to the addition of S(0). 
     
       
         
           
               
             
               
                 TABLE 9 
               
             
            
               
                   
               
               
                 Increase in Copy Numbers of the Genes Encoding Clones of the FMO Enzyme in Response to Addition of S(0) 
               
            
           
           
               
               
               
            
               
                   
                 Number of A6 cells (×10 4 )/mL of culture 
                 Gene copy number (×10 4 )/mL of culture 
               
            
           
           
               
               
               
               
               
               
               
               
               
            
               
                 Gene Encoding 
                   
                   
                 after 20 days 
                 after 20 days 
                 with 
                 after 20 days 
                 after 20 days 
                 with 
               
               
                 Clone of the 
                 Origin of 
                   
                 incubation 
                 incubation 
                 S(0)/without 
                 incubation 
                 incubation 
                 S(0)/without 
               
               
                 FMO Enzyme 
                 the Clone 
                 initial 
                 with S(0) 
                 without S(0) 
                 S(0) 
                 with S(0) 
                 without S(0) 
                 S(0) 
               
               
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
            
               
                 ERCFMO_0001 
                 Pure* 
                 23.00 
                 121.77 
                 48.88 
                 2.49 
                 258.00 
                 38.91 
                 6.631 
               
               
                 ERCFMO_0002 
                 Pure* 
                 41.79 
                 253.49 
                 210.48 
                 1.20 
                 138.00 
                 72.59 
                 1.901 
               
               
                 ERCFMO_0003 
                 Enrichment ** 
                 294.98 
                 113.65 
                 75.53 
                 1.50 
                 162.00 
                 73.54 
                 2.203 
               
               
                 ERCFMO_0004 
                 Enrichment ** 
                 22.81 
                 215.65 
                 183.08 
                 1.18 
                 212.00 
                 31.71 
                 6.686 
               
               
                 ERCFMO_0005 
                 Pure* 
                 59.30 
                 75.09 
                 21.85 
                 3.44 
                 78.00 
                 25.13 
                 3.104 
               
               
                 ERCFMO_0006 
                 Enrichment ** 
                 226.56 
                 275.09 
                 236.90 
                 1.16 
                 261.00 
                 20.52 
                 12.718 
               
               
                 ERCFMO_0007 
                 Pure* 
                 65.38 
                 146.68 
                 29.33 
                 5.00 
                 137.00 
                 16.84 
                 8.135 
               
               
                 ERCFMO_0008 
                 Enrichment ** 
                 199.70 
                 196.86 
                 155.78 
                 1.26 
                 308.00 
                 133.40 
                 2.309 
               
               
                 ERCFMO_0009 
                 Enrichment ** 
                 93.68 
                 312.54 
                 236.33 
                 1.32 
                 237.00 
                 215.13 
                 1.102 
               
               
                 ERCFMO_0010 
                 Enrichment ** 
                 80.59 
                 217.89 
                 120.70 
                 1.81 
                 259.00 
                 129.07 
                 2.007 
               
               
                 ERCFMO_0011 
                 Pure* 
                 51.70 
                 70.82 
                 77.63 
                 0.91 
                 70.00 
                 25.65 
                 2.729 
               
               
                 ERCFMO_0012 
                 Enrichment ** 
                 24.33 
                 76.92 
                 98.05 
                 0.78 
                 308.00 
                 111.97 
                 2.751 
               
               
                 ERCFMO_0013 
                 Enrichment ** 
                 439.43 
                 504.46 
                 388.55 
                 1.30 
                 329.00 
                 225.75 
                 1.457 
               
               
                 ERCFMO_0014 
                 Enrichment ** 
                 15.21 
                 80.67 
                 38.05 
                 2.12 
                 234.00 
                 125.65 
                 1.862 
               
               
                 ERCFMO_0015 
                 Pure* 
                 15.21 
                 133.99 
                 62.73 
                 2.14 
                 132.00 
                 32.71 
                 4.036 
               
               
                 ERCFMO_0016 
                 Enrichment ** 
                 316.27 
                 372.08 
                 413.23 
                 0.90 
                 541.00 
                 407.03 
                 1.329 
               
               
                 ERCFMO_0017 
                 Pure* 
                 28.09 
                 141.41 
                 74.44 
                 1.90 
                 159.00 
                 82.74 
                 1.922 
               
               
                 ERCFMO_0018 
                 Enrichment ** 
                 482.01 
                 574.22 
                 423.33 
                 1.36 
                 560.00 
                 180 
                 3.111 
               
               
                 ERCFMO_0019 
                 Enrichment ** 
                 206.79 
                 226.83 
                 250.00 
                 0.91 
                 410.00 
                 120 
                 3.417 
               
               
                 ERCFMO_0020 
                 Enrichment ** 
                 428.79 
                 537.18 
                 341.00 
                 1.58 
                 323.23 
                 134.00 
                 2.412 
               
               
                 ERCFMO_0021 
                 Pure* 
                 13.68 
                 102.00 
                 26.67 
                 3.83 
                 120.00 
                 23.00 
                 5.217 
               
               
                   
               
               
                 *Pure bacterial culture (10 5 /mL Acidimicrobiaceae bacterium A6 only, in series of 20 mL vials) 
               
               
                 ** Enriched bacterial culture (10 6-7 /mL Acidimicrobiaceae bacterium A6; include ~ 35%-45% of the total bacteria number) 
               
            
           
         
       
     
     It was observed that incubation of the bacterium A6 with S(0) resulted in increase in the number of A6 cells and the number of the copies of the genes encoding clones ERCFMO_0001, ERCFMO_0002, ERCFMO_0005, ERCFMO_0007, ERCFMO_0011, ERCFMO_0015, ERCFMO_0017, and ERCFMO_0021 of the FMO enzyme. Elemental sulfur S(0) was added to the cultures in the amount between 0.5 mM to 20 mM. However, no difference was observed between the amount of sulfur and the reaction rate in the cultures. It was observed that the small amount of sulfur added at the beginning resulted in short time of the reaction. However, more sulfur added over time prolonged the reaction time. The solubility of sulfur is 1.9(±0.6)×10 −8  mole S 8 ·kg −1 . Therefore, the cumulative amount of sulfur added needs to be in excess of 0.05 mM/L to affect the reaction if added once. The maximum sulfur that can be added is believed to depend on the density of sulfur (=2 kg/L). Sulfur can be added in the amount between 1 mg/L and 2 kg/L. 
     The references cited throughout this application are incorporated for all purposes apparent herein and in the references themselves as if each reference was fully set forth. For the sake of presentation, specific ones of these references are cited at particular locations herein. A citation of a reference at a particular location indicates a manner(s) in which the teachings of the reference are incorporated. However, a citation of a reference at a particular location does not limit the manner in which all of the teachings of the cited reference are incorporated for all purposes. 
     Example 27—Oxidant Enhanced Feammox Activity 
     Batch Incubations with Elemental Sulfur, S(0). 
     To set up the incubations, 30 ml of inorganic Fe(III)-NH 4   +  enrichment medium (iFeN) was added into 50 mL sealed serum vials. The composition of the iFeN medium (pH 4.5, which was adjusted by adding dropwise HCl) consisted of 69.55 mg/l NH 4 Cl, 77.9 mg/l (NH 4 ) 2 SO 4 , 19.8 mg/l NaHCO 3 , 71.0 mg/l KHCO 3 , 9.00 mg/l KH 2 PO 4 , 100 mg/l MgSO 4 .7H 2 O, and 60.0 mg/l CaCl 2 .2H 2 O, in addition to 1 mg/l of a trace element solution and 1 mg/l of a vitamin solution (ATCC® MD-VS™). The cultures were also supplemented with 6-line ferrihydrite (Fe 2 O 3 .0.5H 2 O; prepared according to Cornell and Schwertmann, 1990), to obtain a final amount of 10 mmol/1 of Fe(III). 200 mg elemental sulfur [S(0)] was then added to these 30 ml iFeN media. After inoculating the iFeN media with about 10 5 /ml of Acidimicrobiaceae sp. A6, or with enrichment Feammox cultures containing similar numbers of Acidimicrobiaceae sp. A6, the headspace of each incubation vial was vacuumed and then flushed with a N 2 /CO 2  (80:20) mixture, which was repeated three times. The enrichment cultures were then kept in dark at 25° C. and incubated under anaerobic conditions. Three sets of control samples were prepared, 1) autoclaved control, 2) no S(0) added control, 3) no Fe(III) added control. Extra 3.0 mM of NH 4 Cl was add to the second incubation experiments of enrichment cultures. Anaerobic incubations were performed for 20 days, and concentrations of Fe(III) and NH 4   +  were analyzed daily. 
     Results 
     Results of the Feammox batch incubations showing the effect of S(0) addition on ammonium removal and iron reduction with the pure culture of Acidimicrobiaceae sp. A6 are shown in  FIGS. 30 and 31 , and with the Acidimicrobiaceae sp. A6 enrichment culture (two separate experiments) in  FIGS. 32 through 35 . As illustrated in these figures, rates of ammonium removal and iron reduction in the presence of S(0) were significantly enhanced relative to the control compositions. The effect of adding S(0) on the abundance of Acidimicrobiaceae sp. A6 during the incubation with the pure culture are shown in  FIG. 36 . As evidenced in  FIG. 36 , the abundance of Acidimicrobiaceae sp. A6 was substantially enhanced by the presence of elemental sulfur relative to the various control compositions. Increases in the Acidimicrobiaceae sp. A6 population can also increase removal rates of ammonium and/or other contaminants. 
     Example 28—Continuous Flow Membrane Feammox Reactor Employing Elemental Sulfur, S(0) 
     A 2 L continuous flow membrane Feammox reactor (Huang and Jaffe, 2015), was operated under anaerobic conditions by constantly purging N 2  trough the reactor&#39;s headspace at a room temperature (25° C.), and with a 48-hour hydraulic retention time. A 35.5˜40.2% NH 4   +  removal, between inflow and outflow was achieved in the membrane reactor during a one-year operation. The medium in the inflow contained the following components per liter: 177 mg NH 4 Cl, 77.9 mg (NH 4 ) 2 SO 4 , 19.8 mg NaHCO 3 , 71.0 mg KHCO 3 , 9.00 mg KH 2 PO 4 , 100 mg MgSO 4 .7H 2 O, and 60.0 mg CaCl 2 .2H 2 O, and 1 mL trace element solution (Van de Graaf et al., 1996). 10.0 mmol/l of ferrihydrite were added once every week directly to the reactor. To aid in maintaining anaerobic conditions, 0.10-0.20 mmolL −1  sodium citrate was feed to the reactor about twice per month. pH was controlled at around 4˜5, and the dissolve oxygen was maintained at 0.10-0.30 mg/l. 
     After the reactor was running under stable conditions, 200 mg of S(0) was added to the reactor and set up day 0, twice 64 mg of S(0) were added on day 14 and 32. Samples form the inflow and outflow were collected and analyzed every day, and sludge samples from reactor were collected and kept at −20° C. for molecular biology analysis. 
     As illustrated in  FIG. 37 , after adding S(0), the ammonium removal rate between inflow and outflow increased by greater than 10 percent. 
     Various embodiments of the invention have been described in fulfillment of the various objects of the invention. It should be recognized that these embodiments are merely illustrative of the principles of the present invention. Numerous modifications and adaptations thereof will be readily apparent to those skilled in the art without departing from the spirit and scope of the invention.