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. 2025 Dec 4;6(1):93–104. doi: 10.1021/acsenvironau.5c00180

Oxygen Isotopic Fractionation of O2 Consumption by Methane and Ammonia Monooxygenases

Carolina F M de Carvalho , Maartje AHJ van Kessel , Arjan Pol , Jakob Zopfi , Moritz F Lehmann , Sarah G Pati †,§,*
PMCID: PMC12828619  PMID: 41583873

Abstract

Understanding stable isotopic fractionation of dissolved O2 in aquatic environments is crucial to constrain and accurately model the processes responsible for biological O2 consumption, which are closely linked to the overall health of an ecosystem. This study aimed to investigate whether O2 consumption by microbial methane and ammonia oxidation may contribute to the observed discrepancy in O2 isotopic fractionation (18ϵ) between heterotrophic O2 respiration in laboratory incubations (−18 to −24 ‰) and in situ measurements of O2 consumption in lakes and oceans (−10 to −18 ‰). To estimate the in vivo 18ϵ values of soluble methane monooxygenase (sMMO), particulate methane monooxygenase (pMMO), and ammonia monooxygenase (AMO), which are the first enzymes required for the oxidation of methane and ammonia, experiments were performed with three methanotrophic bacteria and one comammox (complete-ammonia-oxidizing) bacterium. The resulting 18ϵ values for pMMO and AMO ranged from −18 ± 12 to −24 ± 5 ‰, not significantly different from 18ϵ values typical for heterotrophic respiration. The 18ϵ value determined for sMMO (−22 ± 2 ‰) was in the same range, yet more negative than the previously reported 18ϵ value for the isolated enzyme. Our results provide insights into the potential reaction mechanisms of pMMO and AMO and indicate that O2 consumption by sMMO, pMMO, or AMO cannot explain the observed discrepancy between in situ and laboratory 18ϵ values for “community” O2 consumption in aquatic environments. Instead, the apparent difference may be attributed to aspects involving substrate diffusion limitation.

Keywords: oxygen isotope ratio, biogeochemical O2 cycling, methane oxidation, ammonia oxidation, isotopic fractionation


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1. Introduction

Dissolved oxygen (O2) is the most important oxidizing agent in aquatic ecosystems, and its concentration controls the rate of many biotic and abiotic processes, from cellular metabolism to the biogeochemical cycling of elements. O2 concentrations and the redox state of an aquatic ecosystem represent important parameters that are directly linked to water quality and trophic status. As such, understanding O2 consumption and production dynamics in aquatic environments is imperative to comprehensively assess ecosystem functioning, health, and resilience. By analyzing the stable isotopic composition of dissolved O2 in aquatic environments, quantitative information can be gained on critical ecosystem processes producing or consuming O2, such as primary production and respiration. , Changes in the isotopic composition of dissolved O2 (reported in the common δ18O notation, see eq ) primarily result from the preferential reaction of 16O16O in biological and abiotic processes, leaving the remaining O2 enriched in 16O18O. Changes in δ18O values of O2, referred to as isotopic fractionation, can be quantified with 18ϵ values or apparent 18O kinetic isotope effects (18O-KIEs) according to eq ,

ϵ18=ln(δO18+1δO018+1)ln([O2]/[O2]0)=1OKIE181=1k16/k181 1

where δ18O and δ18O0 indicate the isotopic composition of O2 in a sample at a certain time point and in a reference sample representing initial conditions (t 0), respectively. [O2]/[O2]0 is the fraction of the remaining O2 concentration upon partial consumption since t 0, while 16 k and 18 k refer to the reaction rates of the light 16O16O and heavy 18O16O isotopologues, respectively.

Because 18ϵ values are typically characteristic for different processes causing changes in dissolved O2 concentrations, i.e., respiration, photosynthesis, and gas–water exchange, they can be used to identify, track, and quantify O2-consuming or producing processes in the environment. As such, several studies have applied stable isotope analysis of O2 to study O2 consumption dynamics in oceans and lakes. This approach usually involves determining 18ϵ values for respiration to estimate respiration rates, which then yield information about gross primary production. Typically, 18ϵ values are obtained from laboratory incubation experiments with water from the study site or by measuring the δ18O in situ as a function of depth and/or along other O2 concentration gradients. The “community” 18ϵ values obtained from incubation experiments have been shown to vary from −18 to −24 ‰, ,− similar to the 18ϵ values determined for microbial respiration by the terminal cytochrome c oxidase (−18 to −21 ‰). In contrast, 18ϵ values determined from water column O2 isotope measurements tend to be considerably lower, ranging from −10 to −18 ‰. − , This may suggest that the enzyme-level O isotope effect associated with respiration is suppressed in situ, e.g., due to diffusion limitation. Alternatively, the observed lower water column 18ϵ values may also reflect the combined isotope effects of multiple distinct processes occurring in parallel within the same water mass. It is important to understand which processes modulate the observed water column 18ϵ value and thereby determine what causes the discrepancy between the 18ϵ values observed in incubation experiments versus the 18ϵ values obtained from δ18O and O2 concentration profiles in natural marine or lacustrine water columns. A better insight into this difference is essential for assessing O2-consuming processes and for accurately modeling and estimating O2 consumption dynamics in aquatic environments. So far, this discrepancy has been suggested to occur due to diffusion-limited O2 consumption in sediments, , diffusion-limited respiration by microorganisms in sinking organic matter particles, , mixing processes, or reduced biological O isotopic fractionation during O2 respiration at low temperatures as well as O2 consumption by biologically produced reactive oxygen species (ROS). Recently, we determined that the biological isotopic fractionation of O2 can range from −9 to −53 ‰, depending on the type of O2-consuming enzyme. Although aerobic microbial respiration typically dominates observed biological O2 consumption, other biological O2-consuming processes may also contribute significantly to the observed 18ϵ values, potentially explaining the observed 18ϵ value discrepancies if they impart different O isotope effects.

Besides aerobic microbial respiration, methane and ammonia oxidation are prevalent biological processes in aquatic environments, which may contribute significantly to the total “community” O2 consumption. For example, estimates of global methane oxidation in oceans and freshwaters translate to an annual O2 consumption of approximately 8·1013 g (assuming a 1O2:1CH4 stoichiometry). This value is 7 times larger than estimates of annual O2 consumption by photochemical reactions in marine waters, which is considered to be a major sink of O2 at least in surface waters. Aerobic methane- and ammonia-oxidizing microorganisms are not only widespread in the environment but also play dominant roles in specific environmental niches, where their metabolic activities significantly impact the biogeochemical cycling of carbon and nitrogen, respectively. Aerobic methane oxidation is the process by which methanotrophic bacteria oxidize methane (CH4) to carbon dioxide using O2 in a 2O2:1CH4 stoichiometry (see Figure ). The first step of CH4 oxidation, i.e., to methanol (CH3OH), involves stoichiometric O2 consumption and is catalyzed by a methane monooxygenase (MMO) enzyme, either soluble methane monooxygenase (sMMO) or particulate methane monooxygenase (pMMO). sMMO is a cytosolic iron-dependent O2-consuming enzyme, whereas pMMO is membrane-bound, copper-dependent, and the most prevalent MMO among methanotrophic microorganisms. In aerobic ammonia oxidation, nitrifying microorganisms utilize O2 to oxidize ammonia (NH3) first to nitrite (NO2 ) and subsequently to nitrate (NO3 ). The overall stoichiometries of the consumption of O2 consumption vs NH3 oxidation are 1.5:1 and 2:1 for the oxidation to nitrite and for complete oxidation to nitrate, respectively (see Figure ). The latter can involve two distinct organisms (ammonia-oxidizing bacteria or archaea in conjunction with nitrite-oxidizing bacteria) or a single comammox (complete-ammonia-oxidizing) bacterium. The first step of nitrification, ammonia oxidation to hydroxylamine (NH2OH), concomitant with O2 consumption, is performed by the membrane-bound, copper-dependent enzyme ammonia monooxygenase (AMO). ,

1.

1

Key reaction steps in the oxidation of methane (CH4) by methanotrophic bacteria and ammonia (NH3) by ammonia-oxidizing microorganisms and comammox bacteria. Dashed-lined boxes highlight the reactions and overall stoichiometry of incomplete CH4 oxidation and cell biomass ({CH3O}) formation via methanol (CH3OH) and formaldehyde (CH3O), and NH3 oxidation to nitrite (NO2 ) via hydroxylamine (NH2OH), respectively. Solid-lined boxes highlight the reactions and overall stoichiometries of complete CH4 oxidation to CO2 via formate (HCOO) and NH3 oxidation to nitrate (NO3 ), respectively. Enzymes involved in these reactions are methane monooxygenase (MMO), methanol dehydrogenase (MDH), formaldehyde dehydrogenase (FADH), formate dehydrogenase (FDH), ammonia monooxygenase (AMO), hydroxylamine oxidoreductase (HAO), nitrite oxidoreductase (NXR), and aerobic terminal oxidases. *We note that HAO only catalyzes the reaction of NH2OH to nitric oxide (NO), which is subsequently converted to NO2 .

Notably, pMMO and AMO share many characteristics, including membrane association, copper dependency, substrate specificity, putative subunit compositions, and a similar DNA sequence. ,, Because they are membrane-bound, both enzymes have been proven difficult to purify while maintaining their activity, ,, which has limited our understanding of their structure, mechanism, and the O isotopic fractionation they impart. In contrast, the cytosolic iron-dependent sMMO has been successfully purified with activity, and 18ϵ values between −15 and −17 ‰ have been determined for the isolated sMMO of Methylococcus capsulatus. Despite their prevalence and environmental relevance, 18ϵ values for pMMO or AMO have, to the best of our knowledge, not yet been determined. Other copper-dependent O2-consuming enzymes have been shown to express 18ϵ values between −9 and −22 ‰. An 18ϵ value closer to −9 ‰ for pMMO or AMO could explain the apparent under-expression of the respiration O isotope effect of approximately −20 ‰ in environments where aerobic methane and ammonia oxidation represent important processes. In contrast, an 18ϵ value closer to −22 ‰ for pMMO or AMO would make the O isotope effects for methane and ammonia oxidation indistinguishable from that of respiration, minimizing their potential to suppress the O isotope effect of water column respiration.

In this study, we determined the in vivo 18ϵ values for pMMO, sMMO, and AMO by performing experiments with the pMMO-containing Methylomonas lenta and Methylotetracoccus oryzae, sMMO-containing Methylocella silvestris, and with the AMO-containing Nitrospira inopinata, respectively. While M. lenta possesses the genes for both pMMO and sMMO, when grown in the presence of excess copper (typical culturing conditions), it expresses only pMMO. M. oryzae expresses only pMMO and M. silvestris only sMMO. , By measuring the O2-to-CH4 and O2-to-NH3 consumption stoichiometries, we first determined the contribution of O2 consumption by pMMO, sMMO, and AMO, respectively, to the overall O2 consumption (i.e., relative to terminal respiratory oxidase activity). Second, based on the observed stoichiometries and measured 18ϵ values for total O2 consumption determined for each microorganism, we were able to calculate in vivo 18ϵ values for pMMO, sMMO, and AMO. Additionally, by supplying the methanotrophs with methanol as the substrate, we determined an isolated respiration value by the terminal cytochrome c oxidase. Our work provides novel insights into the previously unexplored O isotopic fractionation associated with the activity of two environmentally relevant O2-consuming enzymes, MMO and AMO. These new insights will be discussed in the context of whether O2 consumption by methane and/or ammonia oxidation in natural environments can explain the previously observed discrepancies in the “community” 18ϵ values for biological O2 consumption in the water column of lakes or oceans.

2. Materials and Methods

2.1. Bacterial Cultures

Pure cultures of M. lenta (LMG26260) and M. oryzae were grown in 60 to 150 mL serum vials, containing 15 to 60 mL of dilute nitrate mineral salt solution (dNMS: 0.2 g L–1 MgSO4·7H2O, 0.006 g L–1 CaCl2·2H2O, 0.2 g L–1 NaNO3), supplemented with 5 mM phosphate buffer (pH 7.0), 0.1% (v/v) trace element solution I (10 g L–1 trisodium nitrilotriacetate and 5 g L–1 FeSO4·7H2O), and II (0.43 g L–1 ZnSO4·7H2O, 0.24 g L–1 CoCl2·6H2O, 0.99 g L–1 MnCl2·4H2O, 0.25 g L–1 CuSO4·5H2O, 0.22 g L–1 NaMoO4·2H2O, 0.19 g L–1 NiCl2·6H2O, 0.21 g L–1 NaSeO4·10H2O, 0.14 g L–1 H3BO4, and 0.24 g L–1 CeCl·6H2O), and a headspace of 20% CH4 in air. , Cells were grown at 22 °C, with shaking at 150 rpm for 1 to 2 weeks. M. silvestris (DSMZ 15510) was cultured under similar conditions but at pH 5.8 and 26 °C. A pure culture of N. inopinata was grown aerobically in 1000 mL Schott bottles containing 200 mL of mineral medium (0.05 g L–1 KH2PO4, 0.075 g L–1 KCl, 0.05 g L–1 MgSO4·7H2O, 0.584 g L–1 NaCl) supplemented with 4 mM HEPES (pH 7.8) and 0.1% (v/v) of trace metal solutions (see composition above), at 37 °C, in the dark, without shaking. The pH was maintained by the addition of Na2CO3. All experiments were performed with actively growing batch cultures.

2.2. O2 Consumption Experiments with Methanotrophs

2.2.1. Experiments with Methane as the Substrate

To determine the 18ϵ values of O2 consumption by different methanotrophs during CH4 oxiation, experiments were conducted in duplicate for all three methanotrophic species in a 60 mL incubation chamber that housed a membrane-inlet mass spectrometer (MIMS) probe following previously described procedures. , The probe (3 mm in diameter with 4–16 perforated holes of 1 mm diameter each) was covered by silicon tubing and connected to the mass spectrometer, which was operated at a 40 μA emission current, via a 1/8- or 1/16-in. stainless-steel tube.

To monitor dissolved O2 concentrations the incubation chamber was equipped with an optical O2 sensor spot read by a FireStingO2 pro meter (PyroScience GmbH) with automated pressure, humidity, and temperature correction. A calibration point for 100% dissolved O2 was achieved by purging the water-filled chamber with air until stable readings (i.e., equilibrium concentrations) were obtained at the set experimental temperatures (268 and 260 μM at 25 and 28 °C, respectively; salinity 0 ppm). 0% dissolved O2 was assigned to stable low-level readings achieved after biological O2 consumption with excess substrate.

The chamber was placed on a magnetic stirring plate, and temperature was regulated by an external water bath connected to the chamber’s water jacket. Experiments with M. lenta and M. oryzae were conducted at 28 °C, experiments with M. silvestris at 25 °C. Liquid and gas could be introduced into the chamber via a central hole in the piston (0.8 mm diameter), using metal capillaries or gastight syringes. Any gas headspace was eliminated before the start of the measurement. The central piston hole was sealed with a 1/16-in. PEEK tube (0.76 mm inner diameter) Luer-locked to a stainless-steel needle (0.41 mm o.d.), through which samples were obtained by lowering the piston. When taking a sample, the first mL of solution was always discarded, then the PEEK tube-attached needle was injected into a 12 mL Exetainer (Labco Limited), and 3 to 7 mL of the sample was transferred by lowering the piston. Prior to starting an experiment, Exetainers were closed with chlorobutyl septa and screw caps, purged with He gas for 1 h, and amended with 200 μL of 3.2 M HCl to inactivate the bacteria upon sample transfer. To ensure equal headspace pressure in the Exetainers with different sample volumes, Exetainer septa were pierced with a stainless-steel needle (0.45 mm o.d.) connected with a T-piece to a slow He flow, and an open outlet submerged under 10 cm of water during sample injection, as described in de Carvalho et al. Procedural blanks were prepared by filling the incubation chamber with N2-purged (<0.1% O2) water and transferring 3 to 7 mL of this O2-free water to He-purged Exetainers containing HCl, as described above. After injection, Exetainers containing samples or procedural blanks were mixed gently and stored upside down in the dark, with the lid submerged under water, until isotope analysis was performed within 16 days after sample/blank collection (see Section ). We experimentally verified that within this time frame isotopic fractionation of O2 consumption can be determined reliably.

CH4 concentrations were determined from the MIMS mass-to-charge (m/z) signal at m/z 15 (i.e., CH3 +, a fragment formed in the ion source). m/z 15 was selected over m/z 16 due to lower background signals. A calibration was performed by sequentially injecting two 1 mL aliquots of CH4-saturated water (1.5 mM CH4) into the water-filled, initially CH4-free chamber while continuously recording a signal. This procedure resulted in three calibration points at 0, 30, and 60 μM dissolved CH4. The CH4-saturated water was prepared at room temperature in a sealed bottle under a known pressure (1.10–1.14 bar) of pure CH4. Accuracy at higher CH4 concentrations was verified by equilibrating the liquid filled chamber with 30% CH4 in air, resulting in a dissolved CH4 concentration of 450 μM.

For each experiment, the chamber was filled with 52–57 mL of dNMS medium. The medium was purged with air to obtain air-saturated O2 concentrations. CH4 gas was introduced into a 1 to 2 mL headspace to achieve an initial dissolved CH4 concentration between 250 and 450 μM. The generation of a CH4 headspace led to a decrease of the dissolved O2 concentrations to 184 to 214 μM. Once the desired experimental starting conditions were achieved, the CH4 headspace was removed, and 0.1 to 1 mL of a bacterial suspension (obtained by centrifugation of 30 to 120 mL of active culture at 4000 rpm and subsequent resuspension in fresh medium) was added to start the reaction. Experiments were stirred at 500 rpm, except when adding bacterial suspensions. The first sample (3 mL) was taken immediately after adding bacterial suspension at a dissolved O2 concentration of 193 ± 8 μM. Four additional samples (3–7 mL) were taken at decreasing O2 concentrations down to 53 ± 2 μM.

2.2.2. Experiments with Methanol as the Substrate

To determine 18ϵ values representative for O2 consumption by methanotrophic respiration alone (i.e., excluding O2 consumption by pMMO or sMMO), methanol was used as the substrate. Additionally, to assess the potential impact of background O2 consumption by the MIMS probe (up to 5%) on the measured δ18O values, replicate experiments were conducted in two distinct setups: (1) in the 60 mL incubation chamber with an active MIMS probe, and (2) in a 50 mL gastight glass syringe, where background O2 consumption by the MIMS probe was absent.

Experiments were conducted in both the incubation chamber with the MIMS probe, as described above, but with 2.3 mM methanol instead of CH4, and in the gastight glass syringe, containing a stir bar and optical sensor spots for measuring O2 concentrations and temperature (PyroScience GmbH), at room temperature as described in de Carvalho et al. In brief, the syringe was filled with 50 mL of air-saturated dNMS medium containing 0.1 to 1 mL of concentrated bacterial biomass. A 100 μL gastight glass syringe was used to add an aqueous solution of methanol (for a final concentration of 2.3 mM) through the Luer-tip opening of the syringe to initiate the reaction. Immediately after methanol addition, a stainless-steel needle (0.8 mm o.d.) was attached to the Luer-Lock tip of the syringe and pushed into a 12 mm thick chlorobutyl stopper to limit O2 exchange with the atmosphere. Six samples of 3–7 mL were taken from this syringe reactor and transferred to He-purged Exetainers as described in Section . Residual O2 concentration in the samples typically ranged from 200 to 50 μM. A control sample was prepared by transferring 3 mL of remaining assay solution without methanol with a 10 mL gastight glass syringe into a He-purged Exetainer containing 200 μL of 3.2 M HCl. These control samples were assumed to be representative of the initial O2 concentration (270 ± 5 μM) and isotopic composition. Blanks were prepared by transferring 3 to 7 mL of N2-purged water with a 50 mL gastight glass syringe from closed serum bottles into He-purged Exetainers. Exetainers containing samples and blanks were stored as described above.

2.3. O2 Consumption Experiments with N. inopinata

To determine the 18ϵ values of O2 consumption by the comammox bacterium N. inopinata during NH3 oxidation, experiments were conducted in a 50 mL gastight glass syringe, as described in Section . The assay solution was prepared by adding 15 mL of ammonium (NH4 +)-free mineral medium supplemented with 20 mM HEPES (pH 7.8) to 45 mL of an active N. inopinata culture. The syringe was filled headspace-free and placed onto a stirring plate (500 rpm) inside an incubator (37 °C). The assay solution contained approximately 100 μM NH4 +, but an additional 500 μM NH4 + was introduced through the Luer-lock tip of the syringe at the start of the reaction. Six 2 mL samples were taken for NH3, NO3 , and NO2 concentration measurements, and six additional samples (3–7 mL) were taken for O2 isotope analysis. Samples for NH3, NO3 , and NO2 concentration measurements, collected in 2 mL Eppendorf tubes, were always taken directly before the samples for isotope analysis. The latter were collected into 12 mL He-purged Exetainers as described in Section , containing 50 μL saturated HgCl2 solution. Adding HCl did not completely stop the reaction; instead, it led to additional O2 consumption likely due to the reaction with nitrous acid. All handling of HgCl2 was performed with appropriate caution, and all solutions were disposed of as hazardous waste. The first samples were taken immediately (i.e., approximately 30 s) after the NH4 + addition, representing the initial O2, (NH4 + + NH3), NO3 , and NO2 concentrations and δ18O values of O2. The remaining five samples were collected at O2 concentrations of approximately 150, 120, 90, 70, and 50 μM. Samples collected for the dissolved inorganic nitrogen species were immediately passed through a sterile membrane filter (Sarsted, Filtropur, 0.2 μM pore size). Concentrations of (NH4 + + NH3) were determined by Hach Lange ammonium tests (0.2 to 2 mg L–1 NH4 + + NH3, HACH). NO2 was determined colorimetrically using sulfanilamide and N-(1-Naphthyl)­ethylenediamine according to Hansen and Koroleff. NO x (i.e., NO2 + NO3 ) was determined using an NO x TELEDYNE T200 Analyzer (TELEDYNE API, CA, USA) involving the reduction of NO x with hot acidic Vanadium­(III) solution to NO gas and subsequent chemiluminescence detection.

2.4. Stable Isotope Analysis

The δ18O values of O2 were measured in the headspace of the 12 mL Exetainers using a GasBench II coupled via a Conflo IV to a Delta V Plus isotope ratio mass spectrometer (Thermo Fisher Scientific) as described by de Carvalho et al. and reported in permil (‰ ± one standard deviation) relative to the international measurement standard Vienna Standard Mean Ocean Water (VSMOW), according to eq .

δO18=(O18/O16)sample(O18/O16)VSMOW1 2

where (18O/16O)sample and (18O/16O)VSMOW are the ratios of heavy to light isotopes in O2 in a sample and in VSMOW, respectively. In brief, seven 100 μL injections were made from each Exetainer headspace onto a 60 m Rt-Molsieve 5 Å PLOT column (Restek from BGB Analytik, 0.32 mm ID, 30 μm film thickness) maintained at 25 °C. Each GC/IRMS measurement sequence comprised 7–16 experimental samples, 10–15 procedural blanks, five water standards, and three air standards. Air standards were evenly distributed across the sequence and consisted of 150 μL of ambient air in 12 mL of He. Air standards were used to verify the absence of any instrument drift and to perform a one-point calibration of the δ18O values on the VSMOW scale. In recent work, we could demonstrate that the error introduced when using a one-point calibration with air is negligible for δ18O values of O2. The δ18O value of O2 in air was assumed to be 23.8 ‰. Procedural blanks were used to correct the measured δ18O values for blank contributions. Water standards (Exetainers containing different amounts of air-saturated water) were used to correct δ18O values for instrument linearity (change in δ values with signal size).

2.5. Data Analysis

18ϵ values were determined from the slope obtained through the linear regression fit according to eq and are expressed in permil (‰). For experiments conducted in the 60 mL incubation chamber (Section ), the consumption rates of O2 and CH4 were corrected for background consumption by the MIMS probe. The O2-to-CH4 and O2-to-NH3 consumption stoichiometries were determined based on the measured concentrations of O2 versus CH4 or NH3, respectively. All linear regressions were performed with R version 4.3.1 and the lm and confint functions. Unless noted otherwise, errors are reported as 95% confidence intervals.

3. Results and Discussion

3.1. Isotopic Fractionation Associated with O2 Consumption by Methanotrophs

During O2 consumption experiments with methanotrophs when using CH4 as the substrate, the δ18O values of the unreacted dissolved O2 increased with progressing O2 consumption, consistent with the Rayleigh-type dynamics predicted by eq . As an example, Figure shows data from one experiment with M. lenta, including the measured O2 and CH4 concentrations (Figure A) and the changes in δ18O of the remaining O2 over time (Figure C). An O2:CH4 consumption stoichiometry of 1.49 ± 0.01 was determined based on the slope of the linear regression between O2 and CH4 concentrations (see Figure B). The fact that this stoichiometry is between 1 and 2 indicates that both complete CH4 oxidation to CO2 (for energy generation) and incomplete CH4 oxidation in combination with cell biomass formation (see Figure ) occurred during this experiment. In addition, Figure D shows the linearized isotope and concentration data, from which an 18ϵbulk value of −23 ± 3 ‰ was calculated. 18ϵbulk values, which represent bulk O isotopic fractionation of total O2 consumption, were between −20 ± 1 ‰ and −23 ± 3 ‰ for all experiments with methanotrophs using CH4 as the substrate (see upper-row panels in Figure and Table ). 18ϵresp values determined in experiments with methanotrophs using methanol as the substrate ranged between −19.0 ± 0.7 ‰ and −22 ± 3 ‰ (see bottom-row panels in Figure and Table ), in agreement with previous studies on terminal respiration in microbial cultures and pure enzymes. ,,,, The 18ϵresp value determined for M. lenta in the presence of the MIMS probe (−22 ± 3 ‰, n = 1; Figure , red circles) was identical within error to the 18ϵresp value determined in the syringe reactor (−20 ± 1 ‰, n = 2; Figure , orange and green circles), confirming that O2 consumption by the MIMS probe (up 5% of the observed O2 consumption rate) did not significantly affect the measured isotopic fractionation of O2. For further considerations, average 18ϵresp values per species were used (see Table ).

2.

2

O2 and CH4 consumption and isotopic fractionation of O2 during a single experiment with M. lenta. (A) Change in concentrations of dissolved O2 (dashed line) and CH4 (solid line) over time. The dip in CH4 concentration between 5 and 10 min was due to a measurement artifact when stirring was paused to add bacterial biomass to start the reaction. (B) O2 versus CH4 concentrations from panel A. The black line indicates a linear regression fit with a slope of 1.49 ± 0.01 representing the O2:CH4 consumption stoichiometry. (C) δ18O values of unreacted O2 measured in discrete samples over time. (D) Linearized and normalized data (δ18O vs [O2]) from panels A and C, where [O2]0 and δ18O0 represent the concentration and δ18O value, respectively, of O2 at the beginning of the experiment. The solid line shows a linear regression fit according to eq , from which an 18ϵ value of −23 ± 3 ‰ was obtained.

3.

3

Log-normalized change in δ18O values vs log-normalized concentrations of O2 ([O2]) from experiments with different methanotrophs, where [O2]0 and δ18O0 are the concentration and δ18O value of O2 at the beginning of an experiment. The upper-row panels show results from experiments performed with CH4 as the substrate. The bottom-row panels show results from experiments performed with methanol as the substrate. Replicate experiments are colored green, orange, and red. Experiments with CH4 and one replicate experiment with methanol and M. lenta (red circles) were performed in the incubation chamber with the MIMs probe. All other experiments with methanol were performed in a syringe reactor (see Section for details). The slopes of the linear regressions are reported for each experiment in ‰ as 18ϵbulk (upper row) and 18ϵresp (lower row). All linear regressions were significant (p < 0.001) and had adjusted R 2 values ≥ 0.99.

1. O2:CH4 Consumption Stoichiometries (Δ­[O2]/Δ­[CH4]), the Fraction of O2 Consumed by MMO (f MMO), 18 ϵ Values Determined with CH4 (18 ϵ bulk) and Methanol (18 ϵ resp) as the Substrate, and the Calculated O Isotope Effects Imparted by Methane Monooxygenase (as 18 ϵ MMO and Average Apparent 18O-KIE, see eq ) for Three Methanotrophic Bacteria.

species Δ[O2]/Δ[CH4] (−) f MMO (−) 18ϵbulk (‰) 18ϵresp (‰) 18ϵMMO (‰) 18O-KIE (−)
M. lenta 1.358 ± 0.009 0.736 ± 0.005 –21 ± 2 –20.1 ± 0.9 –22 ± 3 1.023 ± 0.004
1.49 ± 0.01 0.670 ± 0.005 –23 ± 3 –24 ± 5
M. oryzae 1.266 ± 0.007 0.790 ± 0.004 –21.9 ± 0.3 –19.0 ± 0.7 –23 ± 1 1.023 ± 0.002
1.323 ± 0.009 0.756 ± 0.005 –21 ± 1 –22 ± 2
M. silvestris 1.49 ± 0.02 0.673 ± 0.007 –21.2 ± 0.5 –19.9 ± 0.5 –22 ± 3 1.022 ± 0.002
1.341 ± 0.008 0.746 ± 0.004 –20 ± 1 –21 ± 1

As stated above, 18ϵbulk values represent the bulk O isotopic fractionation of total O2 consumption, which integrates the O isotopic fractionation associated with both MMO activity (18ϵMMO) and terminal respiration (18ϵresp). In M. lenta and M. oryzae, MMO activity is ascribed to pMMO, while in M. silvestris, it is ascribed to sMMO. Using the observed O2:CH4 consumption stoichiometry, we estimated the relative contribution of the two O2 consuming processes (i.e., the fractional contribution of MMO, f MMO, versus respiration, f resp) to total O2 consumption, which was then used to calculate 18ϵMMO from 18ϵbulk and 18ϵresp as outlined in eq .

ϵbulk18=fMMO·ϵMMO18+fresp·ϵresp18=fMMO·ϵMMO18+(1fMMO)·ϵresp18 3

We considered the plausible stoichiometries for CH4 oxidation to range from 1CH4:2O2, during complete oxidation of CH4 to CO2, to 1CH4:1O2, for incomplete oxidation of CH4 and cell biomass formation (see Figure ). The O2:CH4 consumption stoichiometries, determined in this study, ranged from 1.266 ± 0.007 to 1.49 ± 0.02 (see Table ), indicating a mix of complete and incomplete CH4 oxidation, consistent with previous studies. , We can use these stoichiometries as a direct proxy for the fraction of O2 consumption by MMO (see eq ) because based on the reactions shown in Figure , the amount of CH4 consumed (Δ­[CH4]) is equal to the amount of O2 consumed by MMO (Δ­[O2]MMO) and the amount of total O2 consumed (Δ­[O2]) is equal to the sum of O2 consumed by respiration (Δ­[O2]resp) and MMO.

Δ[O2]Δ[CH4]=Δ[O2]MMO+Δ[O2]respΔ[O2]MMO=1fMMO 4

We can thus calculate O isotopic fractionation associated with O2 consumption by MMO for the three methanotrophs with eqs and and the measured parameters O2:CH4 stoichiometry, 18ϵbulk and 18ϵresp. The resulting average 18ϵMMO values were −22 ± 2 ‰ for M. silvestris, −23 ± 2 ‰ for M. oryzae, and −23 ± 4 ‰ for M. lenta (see Table ). While not significantly different, there is a slight difference in isotopic fractionation between pMMO (18ϵMMO = −23 ± 3 ‰) and sMMO (18ϵMMO = −22 ± 2 ‰).

3.2. Isotopic Fractionation Associated with O2 Consumption by N. inopinata

18ϵbulk values associated with O2 consumption by the complete-ammonia oxidizer N. inopinata were determined in experiments analogously to those with methanotrophs, except that NH3 consumption was determined from NH4 + concentrations in discrete samples at different time points. The O2:NH3 consumption stoichiometries were 1.7 ± 0.5 and 1.5 ± 0.7, respectively, and the corresponding 18ϵbulk values were −19 ± 2 ‰ and −19.1 ± 0.7 ‰ (see Figure and Table ), similar to the 18ϵbulk for methanotrophic O2 consumption. The fact that average NO2 (62 ± 54 μM) and NO x production (56 ± 103 μM) were both comparable to average NH3 consumption (96 ± 43 μM) together with an average O2:NH3 stoichiometry of 1.6 suggests that the majority of NH3 was oxidized only to NO2 (partial nitrification) during the course of the experiments (see Figure ). Note that the poor precision of the N-species concentration measurements are due to the fact that initial concentrations of NH4 +, NO2 , and NO3 (approximately 0.6, 1.3, and 3.9 mM, respectively) were high relative to the changes measured in these concentrations.

4.

4

(A) O2 vs (NH4 + + NH3) concentrations in two replicate experiments with N. inopinata. The NH4 + concentrations were determined from duplicate measurements at different time points of the reaction (error bars represent standard deviations). The solid lines show a linear regression fit of the data in each experiment, with the slopes representing the respective O2:NH3 consumption stoichiometries. (B) Log-normalized change in δ18O values vs log-normalized concentration of O2 for experiments with N. inopinata. The solid lines show a linear regression fit according to eq , with slopes indicating 18ϵbulk values.

2. O2:NH3 Consumption Stoichiometries (Δ­[O2]/Δ­[NH3]), the Fraction of O2 Consumed by AMO (f AMO), 18 ϵ Values Determined In Vivo (18 ϵ bulk), and the Calculated O Isotope Effects Imparted by Ammonia Monooxygenase (as 18 ϵ AMO and Average Apparent 18O-KIE, see eq ) for N. inopinata .

species Δ[O2]/Δ[NH3] (−) f AMO (−) 18ϵbulk (‰) 18ϵAMO (‰) 18O-KIE (−)
N. inopinata 1.5 ± 0.7 0.7 ± 0.3 –19.1 ± 0.7 –19 ± 14 1.019 ± 0.014
1.7 ± 0.5 0.6 ± 0.2 –19 ± 2 –18 ± 12

Similar to O2 consumption by methanotrophs, the average 18ϵbulk value for O2 consumption by N. inopinata reflects the combined O isotopic fractionation imparted by both AMO and respiration. As with methanotrophs, where experiments with methanol were used to isolate the respiratory 18ϵresp value by excluding MMO-driven O2 consumption, a similar approach could theoretically be applied to N. inopinata by using hydroxylamine as an intermediate substrate to bypass AMO activity. However, due to the reactivity of hydroxylamine, an isolated respiration 18ϵresp value for N. inopinata could not be determined. Nevertheless, 18ϵresp for N. inopinata can be reasonably approximated based on known properties of its respiratory machinery. Notably, N. inopinata lacks the canonical terminal copper-heme-dependent cytochrome c oxidase, and instead expresses a heme-dependent cytochrome bd-like oxidase. , Stolper et al. demonstrated that the 18ϵresp values obtained for Escherichia coli mutant strains containing either only cytochrome c oxidase, only cytochrome bd-I oxidase, or only cytochrome bd-II oxidase, were indistinguishable within error, ranging from −14.9 to −15.5 ‰. Although these 18ϵresp values are lower than those typically reported for isolated cytochrome c oxidase, or microbial respiration more broadly, ,,, they nevertheless suggest that the cytochrome bd-like oxidase in N. inopinata may impart 18ϵresp values similar to those of more common respiratory terminal oxidases found in most bacteria (i.e., approximately −20 ‰).

Similar to the approach used for the methanotrophs in this study, the O2:NH3 consumption stoichiometry was employed to calculate the relative contributions of AMO activity versus respiration to total O2 consumption and, in turn, to calculate 18ϵAMO from the observed 18ϵbulk values and an assumed 18ϵresp of −20 ‰ with eq .

ϵbulk18=fAMO·ϵAMO18+fresp·ϵresp18=Δ[NH3]Δ[O2]·ϵAMO18+(1Δ[NH3]Δ[O2])·ϵresp18 5

We note that the calculated average 18ϵAMO value of −19 ± 13 ‰ (Table ) is contingent on the assumed 18ϵresp, which was not independently determined (unlike in our methanotroph experiments) but instead derived from the existing literature. Nevertheless, varying the assumed 18ϵresp value by ±5 ‰ still yields 18ϵAMO estimates (−15 to −22 ‰) that fall within the typical range reported for terminal aerobic respiration (18ϵresp). The high uncertainty of the 18ϵAMO estimate is due to the elevated 95% confidence intervals of the O2:NH3 stoichiometries (Table ), and thus it is a consequence of the errors associated with NH3 concentration measurements.

3.3. Kinetic Isotope Effects and O2 Activation Mechanisms of Enzymes Involved in Methane and Ammonia Oxidation

The in vivo 18ϵMMO, 18ϵAMO, and 18ϵresp values determined in this study can be converted into average apparent 18O-KIEs of 1.023 ± 0.003, 1.022 ± 0.002, 1.019 ± 0.014, and 1.020 ± 0.001 (Tables and ) for the reduction of O2 by pMMO, sMMO, AMO, and terminal oxidase, respectively. 18O-KIEs can be used as mechanistic probes to assess the rate-limiting steps in O2-consuming enzymatic reactions and thus shed light on the catalytic cycle of such enzymes. This is of particular interest for pMMO and AMO, whose catalytic cycles have not been well studied. Because pMMO, sMMO, AMO, and terminal oxidase represent three different classes of O2-consuming enzymes with distinct active-site structures, it is surprising to see their respective 18O-KIEs fall within error of each other. To better link these values with the potentially rate-limiting reaction steps, a closer look at these enzyme’s catalytic cycles is required.

Cytochrome c oxidase, the most prevalent terminal oxidase, is a well-studied heme-copper-dependent enzyme, in which the heme a3 subunit initially binds O2 reversibly, forming an iron-superoxo intermediate (see Figure a). In the subsequent step, which is suggested to be rate-limiting, a hydrogen atom abstraction from an adjacent tyrosine residue by this iron-superoxo species, concomitant with O–O bond cleavage, leads to the formation of an iron-oxo and a copper-hydroxo species. The measured 18O-KIE of 1.020 ± 0.001 for terminal oxidases is in agreement with such a rate-limiting hydrogen atom abstraction step by a metal-superoxo intermediate as well as with a rate-limiting iron-oxo species formation. ,

5.

5

Key steps in the O2 activation mechanisms of (a) cytochrome c oxidase (adapted from ref , copyright 2015 American Chemical Society), (b) soluble methane monooxygenase (sMMO, adapted from ref , copyright 2024 American Chemical Society, and with permission under a Creative Commons CC-BY 4.0 license from ref , copyright 2001 ASBMB), and (c) particulate methane monooxygenase (pMMO, adapted from ref , copyright 2024 American Chemical Society and with permission under a Creative Commons CC-BY 4.0 license from ref , copyright 2024 P.E.M. Siegbahn). Potentially rate-limiting steps according to measured 18O kinetic isotope effects are marked with an asterisk (*).

The 18O-KIE determined for the diiron enzyme sMMO in this study with M. silvestris (1.022 ± 0.002) is larger than previously reported values for the isolated enzyme from M. capsulatus (1.015–1.017). While natural variability in isotope effects for a given enzyme is not uncommon, it is also possible that the isolated enzyme exhibits a different 18O-KIE outside its cellular environment, compared to in its in vivo state. In sMMO, it is proposed that O2 activation is initiated with a reversible O2 binding to one of the active-site iron atoms, followed by the formation of a diiron-bridged peroxo species (3 in Figure b). One of the O atoms is subsequently released from the active site as H2O, while the other O atom may form a high-valent diiron-bridged oxo species (4 in Figure b). The final steps in the catalytic cycle of sMMO involve hydrogen atom abstraction from CH4 by 4, rebound of the methyl radical, release of methanol, and reduction of the active-site iron atoms (see Figure b). While Stahl et al. suggested the formation of a diiron-bridged peroxo species (3) to be the rate-limiting step based on their 18O-KIEs of 1.015–1.017, the value measured in this study (1.022 ± 0.002) is in better agreement with a rate-limiting formation of an iron-bound oxo species (4). A common rate-limiting iron-oxo species formation would also be compatible with the identical 18O-KIEs of sMMO and the terminal oxidase measured in this study. Further studies should focus to elucidate whether the difference in isotope effects of sMMO is due to experimental variables (in vitro vs in vivo) or the different bacterial species (M. silvestris vs M. capsulatus).

The 18O-KIEs determined for pMMO (1.023 ± 0.003) and AMO (1.019 ± 0.014) in this study align with the upper range of values previously reported for copper-dependent O2-consuming enzymes. Generally, O2 activation by copper-dependent enzymes with apparent 18O-KIEs between 1.017 and 1.022 is associated with a rate-limiting hydrogen atom abstraction, leading to the formation of a copper-hydroperoxo species. ,, Given the similarities in substrate specificity, subunit compositions, and DNA sequences of pMMO and AMO, a common O2 activation mechanism is plausible. A complete catalytic cycle has not been resolved for either of the two enzymes, but experimental and computational evidence from studies with pMMO can be used, together with the measured 18O-KIEs, to suggest two possible O2 activation mechanism (see Figure C). While there is still debate regarding the exact location of the active site in pMMO, current evidence suggests a mononuclear copper center to be the active site (7 in Figure c). In analogy to O2 activation mechanisms of other mononuclear copper enzymes with similar 18O-KIEs, the first step of the catalytic cycle likely involves reversible O2 binding and formation of a copper-superoxo intermediate (8 in Figure c). This could be followed by a rate-limiting hydrogen atom abstraction by 8 directly at the substrate (CH4) and thus result in a Cu-hydroperoxo intermediate and a methyl radical (9 in Figure c). The catalytic cycle can then be completed through a radical rebound step and the release of the products methanol and H2O. Computational studies, however, suggest that direct hydrogen atom abstraction from CH4, achieved enzymatically only by MMO and AMO, requires a more reactive intermediate, such as Cu­(II)-(hydr)­oxo or Cu­(III)-oxo species (12a12c in Figure c). These species could form through a rate-limiting O–O bond cleavage step from a Cu-hydroperoxo intermediate (11 in Figure c). While a Cu­(III)-oxo species has not yet been detected in enzymes, the analogous intermediate in iron-dependent enzymes (an Fe­(IV)-oxo species formed in a rate-limiting O–O bond cleavage step) is associated with a 18O-KIE of 1.022, similar to pMMO and AMO here. Similar to the mechanism mentioned above, this second possible catalytic cycle of pMMO (and AMO) is concluded with hydrogen atom abstraction from CH4, radical rebound, and release of the products methanol and H2O (see Figure c). The key difference between the two proposed mechanisms (89107 vs 8111213147 in Figure ) is the timing of hydrogen atom abstraction from CH4 relative to the first irreversible step of O2 activation. In the former pathway, hydrogen atom abstraction occurs during the first irreversible step, whereas in the latter, it occurs after the first irreversible step of the O2 activation. The nature of the rate-limiting step of pMMO could potentially be determined by comparing 18O-KIEs using protiated and deuterated substrates (CH4 or CD4). Deuteration of the substrate would alter the 18O-KIE onyl if hydrogen atom abstraction occurs during the first irreversible step of O2 activation. However, this analysis was beyond the scope of the current study. Nonetheless, the 18O-KIEs determined here for the first time for O2 activation by pMMO and AMO provide important evidence to better refine the catalytic cycle of these environmentally relevant enzymes.

4. Conclusions

The in vivo 18ϵ values for pMMO, sMMO, and AMO determined in this study ranged from −18 ± 12 ‰ to −24 ± 5 ‰. These values are not significantly different from the in vivo 18ϵresp values we report here for methanotrophs (−19.0 ± 0.7 ‰ to −22 ± 3 ‰) or from typical aquatic respiration 18ϵ values reported in previous studies (−18 to −24 ‰). ,,, This apparent similarity implies that O2 consumption by the widespread enzymes pMMO or AMO cannot account for the discrepancy observed between in situ and laboratory-derived 18ϵ values for O2 consumption in aquatic environments. Consequently, the 18ϵ values estimated for aerobic CH4 or NH3 oxidation indicate that these processes cannot be uniquely identified or quantified solely on the basis of O2 isotope analysis in the environment. Nevertheless, it would be interesting to conduct further experiments, particularly with other ammonia-oxidizers or mixed cultures, to test the robustness of the 18ϵ values determined in this study. We consider it unlikely that other biological (i.e., beyond respiration and CH4 or NH3 oxidation) or abiotic O2-consuming processes, such as H2S or Fe­(II) oxidation, ,, which are characterized by low 18ϵ values, are pervasive enough in natural aquatic environments to significantly mask the isotopic imprint of heterotrophic O2 respiration at the ecosystem scale. And while photochemical reactions can have a significant impact on the isotopic fractionation of O2 consumption in surface waters, , these processes unlikely mask the isotopic imprint of heterotrophic O2 respiration in lower parts of the water column, where in situ isotopic fractionation of O2 consumption is typically determined. Hence, the observed discrepancy between “community” in situ and laboratory 18ϵ values for O2 consumption is most plausibly explained by diffusion limitation at different spatial scales in natural environments or O2 consumption via biological ROS formation, as previously proposed.

Acknowledgments

This work was supported by the Swiss National Science Foundation (Grant no. PZ00P2_186083).

The data underlying this study are openly available at 10.5281/zenodo.17415999.

The authors declare no competing financial interest.

Published as part of ACS Environmental Au special issue “2025 Rising Stars in Environmental Research”.

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Associated Data

This section collects any data citations, data availability statements, or supplementary materials included in this article.

Data Availability Statement

The data underlying this study are openly available at 10.5281/zenodo.17415999.


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