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. 2021 Dec;600(7890):670-674.
doi: 10.1038/s41586-021-04153-3. Epub 2021 Dec 22.

Rapid microbial methanogenesis during CO2 storage in hydrocarbon reservoirs

Affiliations

Rapid microbial methanogenesis during CO2 storage in hydrocarbon reservoirs

R L Tyne et al. Nature. 2021 Dec.

Abstract

Carbon capture and storage (CCS) is a key technology to mitigate the environmental impact of carbon dioxide (CO2) emissions. An understanding of the potential trapping and storage mechanisms is required to provide confidence in safe and secure CO2 geological sequestration1,2. Depleted hydrocarbon reservoirs have substantial CO2 storage potential1,3, and numerous hydrocarbon reservoirs have undergone CO2 injection as a means of enhanced oil recovery (CO2-EOR), providing an opportunity to evaluate the (bio)geochemical behaviour of injected carbon. Here we present noble gas, stable isotope, clumped isotope and gene-sequencing analyses from a CO2-EOR project in the Olla Field (Louisiana, USA). We show that microbial methanogenesis converted as much as 13-19% of the injected CO2 to methane (CH4) and up to an additional 74% of CO2 was dissolved in the groundwater. We calculate an in situ microbial methanogenesis rate from within a natural system of 73-109 millimoles of CH4 per cubic metre (standard temperature and pressure) per year for the Olla Field. Similar geochemical trends in both injected and natural CO2 fields suggest that microbial methanogenesis may be an important subsurface sink of CO2 globally. For CO2 sequestration sites within the environmental window for microbial methanogenesis, conversion to CH4 should be considered in site selection.

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Conflict of interest statement

M.F. and B.S. are employed by/an employee of ExxonMobil Upstream Integrated Solutions Company. Z.M.S. is employed by/an employee of ExxonMobil Research and Engineering Company. When the manuscript was first submitted, M.L. was employed by/an employee of ExxonMobil Upstream Integrated Solutions Company. M.L. is now employed by/an employee of Aker BP. The views expressed are those of the author(s) and not necessarily those of ExxonMobil Upstream Integrated Solutions Company, ExxonMobil Research and Engineering Company, or Aker BP.

Figures

Fig. 1
Fig. 1. Map of study area showing locations of the Olla and Nebo-Hemphill oil fields as well as the Black Lake Oil Field, from which the injected CO2 was sourced.
Only the Olla Oil Field contains injected CO2. The inset on the right shows an expanded view with individual sample locations (nearby urban areas are denoted by stars) and a stratigraphic column showing the relevant lithologic units.
Fig. 2
Fig. 2. The δ13C of CO2 in the Olla (CO2 injected field) samples.
a, The δ13C of CO2 as a function of the CO2/3He ratio. The dashed lines show endmember methanogenesis and dissolution (pH 7) fractionation trajectories. The tick marks represent the total amount of CO2 trapping within the system, relative to sample O5. The shaded region represents trapping by the combination of both microbial methanogenesis and dissolution. The upper and lower methanogenesis:dissolution ratios (M:D) are 0.33 and 0.19, respectively, showing that dissolution accounts for approximately three times more CO2 removal (M:D = 0.26) than microbial methanogenesis. The lines labelled ‘consumption’ show the portion of original injected CO2 that has been removed by net microbial methanogenesis. b, The δ13C of CO2 as a function of the δ13C of CH4. The shaded region represents the CO2 isotopic composition of the injectate from the Black Lake Oil Field into the Olla system. The Olla data are consistent with thermal re-equilibration with both reservoir temperatures (solid lines) and microbial methanogenesis (dotted lines). The 1σ level of uncertainty is within the symbol size.
Fig. 3
Fig. 3. Δ12CH2D2 versus Δ13CH3D of the measured Olla and Nebo-Hemphill samples.
The clumped isotopologue space illustrates whether measured CH4 is at internal thermodynamic equilibrium (black line) or not. The thermodynamic equilibrium curve is calculated following ref. . The shaded cross represents thermal equilibration to current reservoir temperatures in each isotopologue. The arrows represent the theoretical trends for methanogenesis (dark grey) and AOM (light grey) . The 1σ level of uncertainty is shown on the measured samples.
Extended Data Fig. 1
Extended Data Fig. 1. Relationship between noble gas isotopic ratios in the Olla (blue circles) and Nebo-Hemphill (orange triangles) oil fields.
Both fields show a resolvable mantle component that is significantly greater in the Olla Oil Field. One standard deviation error bars are within symbol size. a, He isotopic ratios versus 4He/20Ne ratio. Air-corrected He isotopes are reported relative to air (RA = 1.38 × 10−6 (ref. )). All samples are in excess of typical radiogenic production (0.02RA), requiring a mantle contribution. High 4He/20Ne indicates negligible air contamination in the samples. b, Three neon isotope plot. The crustal production line reflects the observed trend in typical crustal fluids. The mantle-air line represents mixing between air and a MORB-like endmember. Data are consistent with mixing between air and a mantle-rich component. In both He and Ne isotopes, the mantle signal is stronger in the Olla Oil Field. Source data
Extended Data Fig. 2
Extended Data Fig. 2. CO2/3He variation vs.
a, b, 4He (a) and 20Ne (b) abundances in the Olla (blue circles) and Nebo-Hemphill (orange triangles) oil fields. 1σ level of uncertainty is shown on the measured samples. A negative correlation between 4He, which accumulates in formation waters as a function of time and 20Ne (which is groundwater derived) and CO2/3He, has been interpreted in other CO2-rich natural gas fields to support the importance of the formation water in controlling CO2 removal. Source data
Extended Data Fig. 3
Extended Data Fig. 3. Hydrocarbon isotopic composition in the Olla (blue circles) and Nebo-Hemphill (orange triangles) oil fields.
a, Comparison of δ13C-CH4 and δD-CH4, with typical CH4 provenances after Whiticar. One standard deviation error bars are within symbol size. In isolation, the Olla samples (blue circles, this study; unfilled circles, from ref. ) are consistent with a mainly thermogenic origin, whereas Nebo-Hemphill (orange triangles, this study; unfilled triangles, from ref. ) appears to be a microbial-thermogenic mix. Clumped isotopologues nevertheless provide clear evidence that the Olla CH4 is microbial in origin (Fig. 3). b, Plot of δ13C of Cn versus 1/Cn variation in natural gases. One standard deviation error bars are within symbol size. Both the Olla (blue circles) and Nebo-Hemphill (orange triangles) fields show an enrichment in their isotopic signature especially in propane; however, this is most pronounced within the Olla Oil Field. Source data
Extended Data Fig. 4
Extended Data Fig. 4. Schematic of the processes occurring within the Olla Oil Field and resulting changes in the isotopic composition within the field.
The first panel shows CO2 injection into the 2,800-ft sandstone (sst) and subsequent lateral and vertical migration (yellow arrows) to all the producing formations within the field. The middle panel demonstrate the different processes (microbial methangonesis, AOM and dissolution), which are occurring in the field and their effects on the isotopic composition. Yellow circles represent CO2 dissolution and green circles are the net CH4 production from microbial activity. Hydrogen for microbial methanogenesis is sourced from the hydrocarbons and water. The final panel shows the current state of the reservoir.
Extended Data Fig. 5
Extended Data Fig. 5
Microbial community analysis of most abundant taxa from the SSU rRNA gene-sequence region. Bar charts represent the most resolved taxa from amplicon sequence variants generated in QIIME 2,, for archaeal primers (a) and bacterial primers (b). Hydrogenotrophic methanogenesis-capable taxa are represented with bold red font. Source data
Extended Data Fig. 6
Extended Data Fig. 6. Carbon isotopic composition of the Olla samples as a function of CO2 concentration for data from this study (dark blue circles) and those collected without 3He analysis (unfilled circles).
One standard deviation error bars are within symbol size. Dashed lines show endmember methanogenesis and dissolution fractionation (at pH 7) trajectories. Tick marks represent the total amount of CO2 trapping within the system, relative to sample O5. The shaded region represents trapping by the combination of both microbial methanogenesis and dissolution. The same combination of dissolution and microbial methanogenesis has been modelled (grey region, cf. Fig. 2). Lines labelled ‘consumption’ at 5%, 13% and 19 % show the proportion of original CO2 that has been removed by net microbial methanogenesis. One sample from ref. has a CO2 concentration greater than our ‘most pristine’ CO2/3He sample (O5). This illustrates that by using sample O5 as our least altered composition we calculate a conservative (minimum) amount of CO2 consumption, and that initial CO2 concentrations were probably greater. Source data
Extended Data Fig. 7
Extended Data Fig. 7. Carbon composition of the Pannonian Basin samples.
a, Szegholm South, (red circles), Szegholm North, (purple triangles), Ebes, (blue diamonds) and Hajduszoboszlo, (grey squares) gas field samples as a function of their CO2 concentrations and CO2/3He. Dashed lines represent the projection of CO2 trapping in the fields. b, The Szegholm South field had multiple CO2 isotope data and this field has been used to investigate the processes controlling this pattern using the carbon isotopic composition as a function of CO2/3He. Dashed lines show endmember methanogenesis and dissolution fractionation (at pH 7) trajectories. Tick marks represent the total amount of CO2 trapping within the system. The shaded region represents trapping by the combination of both microbial methanogenesis and dissolution. The upper and lower methanogenesis:dissolution ratios (M:D) are 0.050 and 0.060, respectively, showing dissolution accounts for approximately 16 times (M:D = 0.055) more CO2 removal than microbial methanogenesis. Lines labelled ‘consumption’ show the proportion of original CO2 that has been removed by net microbial methanogenesis.

References

    1. Leung DYC, Caramanna G, Maroto-Valer MM. An overview of current status of carbon dioxide capture and storage technologies. Renew. Sustain. Energy Rev. 2014;39:426–443.
    1. Bui M, et al. Carbon capture and storage (CCS): the way forward. Energy Environ. Sci. 2018;11:1062–1176.
    1. Stewart, R. J. & Haszeldine, R. S. Carbon Accounting for Carbon Dioxide Enhanced Oil Recovery (Scottish Carbon Capture & Storage, 2014); https://www.sccs.org.uk/images/expertise/misc/SCCS-CO2-EOR-JIP-Carbon-Ba...
    1. Gilfillan SMV, et al. Solubility trapping in formation water as dominant CO2 sink in natural gas fields. Nature. 2009;458:614–618. - PubMed
    1. Matter JM, et al. Rapid carbon mineralization for permanent disposal of anthropogenic carbon dioxide emissions. Science. 2016;352:1312–1314. - PubMed

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