2025 Volume 40 Issue 4 Article ID: ME25066
This study investigated the effects of elevated hydrostatic pressure on methane production and gene expression in a hydrogenotrophic methanogen isolated from subseafloor sediments at biogenic gas hydrate sites, with a focus on the implications of CO2 availability. Using high-pressure cultivation, the methane production rate decreased by 15% at 25 MPa, while a transcriptomic analysis revealed the marked up-regulation of methyl-coenzyme M reductase and ATP synthase. These results suggest that methanogens compensate for pressure-driven constraints on CO2 utilization by increasing the expression of key methanogenic enzymes, underscoring the overlooked role of CO2 in deep biosphere microbial processes.
Deep marine sediments harbor a large fraction of the Earth’s microbial biomass (Magnabosco et al., 2018) and constitute the largest methane reservoir on Earth (Milkov, 2004). Geochemical evidence indicates that methane stored as gas hydrates beneath deep ocean basins is mainly generated by methanogenic archaea (Kvenvolden, 1995; Milkov, 2005). Therefore, identifying the environmental factors controlling methanogenesis in subseafloor settings is fundamental to understanding global biogeochemical cycles.
A distinctive feature of deep marine sediments is elevated hydrostatic pressure, which enhances the solubility of the gaseous methanogenic substrates, H2 and CO2. Regarding H2, higher solubility under elevated pressure has been shown to promote the growth of hyperthermophilic methanogens by improving access to the substrate (Bernhardt et al., 1988b; Miller et al., 1988; Takai et al., 2008). In contrast, greater CO2 solubility decreases culture medium pH, thereby suppressing methanogenic activity (Bernhardt et al., 1988a). Dissolved CO2 is also hydrated and ionized to HCO3–, a process that is promoted under elevated pressure (Abe and Horikoshi, 1998). These pressure-driven changes in CO2 speciation may reduce its availability for methanogenesis in deep subseafloor sediments. However, this effect has yet to be investigated, partly because of the opposing impacts of H2 and CO2 solubilities.
To assess the effects of CO2 availability under elevated pressure on methanogenic activity, we used formate as an alternative substrate to H2/CO2 and employed Good’s buffer (HEPES) instead of bicarbonate buffering systems in the culture medium. Periodic sampling from a high-pressure cultivation system (Fig. 1) enabled measurements of formate concentrations, from which methane production was calculated stoichiometrically. Experiments focused on Methanocalculus sp. strain 1H1Hc7 (JCM 39199), the predominant hydrogenotrophic methanogen isolated from sediments in the biogenic gas hydrate area of the eastern Nakai Trough (Katayama et al., 2022).

Schematic diagram (a) and photographs (b, c, and d) of the high-pressure cultivation system. A vial was set to a syringe needle connected with the outlet port to harvest the culture that was subsequently used for the quantification of formate concentrations (c and d).
Strain 1H1Hc7 exhibits optimal methane production at 45°C (Katayama et al., 2022), corresponding to in situ conditions at ~2,500 m below sea level, given a sediment geothermal gradient of 0.03°C m–1 (Kanno et al., 2014). To simulate these conditions, we cultured the strain under 0.1 MPa (atmospheric), 13 MPa, and 25 MPa (Supplementary Methods). The formate consumption rate at 25 MPa was approximately 15% lower than that at atmospheric pressure, whereas no decrease was observed at 13 MPa (Fig. 2). Despite this difference, the final cumulative methane stoichiometrically produced reached nearly the same level (~5.7 mM) under all conditions (Fig. 2). Cell densities were also similar between 0.1 MPa (8.4×107±3.5×107 [mean±s.d.] gene copy numbers mL–1) and 25 MPa (6.8×107±4.0×107 mL–1) after cultivation. These results indicate that a high pressure primarily imposed a kinetic limitation rather than a yield limitation on methanogenesis.

Effects of hydrostatic pressure on formate consumption and methane production in Methanocalculus sp. strain 1H1Hc7. Data are presented as the means and standard deviations (error bars) of quadruplicate experiments. The figure also shows methane production rates, with means and standard deviations, relative to those observed under atmospheric pressure conditions, and the final amounts of methane produced (mM, in parentheses) calculated based on the chemical formula representing the conversion of a quarter mole of methane from formate.
The transcriptome analysis compared cultures at 0.1 and 25 MPa, using a two-fold change in expression and a P-value of 0.05 as cut-offs. Of the 2,327 genes encoded in the 1H1Hc7 genome, 79 were significantly up-regulated and 100 were down-regulated at 25 MPa (Supplementary Table S1). Under high-pressure conditions, genes involved in methanogenesis were markedly up-regulated, particularly those encoding methyl-coenzyme M reductase (MCR, 1.7–4.0 fold) and ATP synthase (ATPase, 1.8–22 fold) (Table 1). In contrast, genes associated with transcription and protein synthesis were down-regulated at 25 MPa (Supplementary Table S2).
List of genes significantly up-regulated under high pressure conditions. Expression levels of Methanocalculus sp. strain 1H1Hc7 genes in three replicates are shown as RPKM values, which were further normalized to the median expression level of all genes with mapped transcripts (N. RPKM).
| Locus | Function | N. RPKM in 0.1 MPa | N. RPKM in 25 MPa | P-value | |||
|---|---|---|---|---|---|---|---|
| A.V. | S.D. | A.V. | S.D. | ||||
| 1H1ca_00514 | Aquaporin AqpM | 2.17 | 0.31 | 9.19 | 1.14 | 0.009 | |
| 1H1ca_00394 | ATP-dependent DNA helicase Rep | 0.57 | 0.04 | 1.17 | 0.17 | 0.029 | |
| 1H1ca_01282 | Cell wall-active antibiotics response protein | 0.65 | 0.12 | 1.33 | 0.13 | 0.008 | |
| 1H1ca_01239 | Coenzyme F390 synthetase | 0.74 | 0.08 | 1.7 | 0.08 | 0.001 | |
| 1H1ca_01924 | D-inositol-3-phosphate glycosyltransferase | 0.6 | 0.07 | 1.24 | 0.17 | 0.026 | |
| 1H1ca_00994 | Deoxyribodipyrimidine photo-lyase | 0.31 | 0.02 | 0.63 | 0.07 | 0.017 | |
| 1H1ca_02150 | indole-3-glycerol phosphate synthase | 2.98 | 0.21 | 6.12 | 0.33 | 0.001 | |
| 1H1ca_01754 | Methyl-coenzyme M reductase subunit alpha | 26.27 | 2.7 | 63.83 | 13.59 | 0.042 | |
| 1H1ca_01750 | Methyl-coenzyme M reductase subunit beta | 41.91 | 4.75 | 124.18 | 23.68 | 0.028 | |
| 1H1ca_01753 | Methyl-coenzyme M reductase subunit gamma | 23.65 | 3.03 | 55.04 | 11.79 | 0.047 | |
| 1H1ca_01752 | Methyl-coenzyme M reductase operon protein C | 23.81 | 0.34 | 74.87 | 15.93 | 0.031 | |
| 1H1ca_01751 | Methyl-coenzyme M reductase operon protein D | 30.19 | 3.89 | 84.78 | 16 | 0.029 | |
| 1H1ca_02149 | N-(5′-phosphoribosyl)anthranilate isomerase | 3.67 | 0.25 | 8.6 | 0.62 | 0.006 | |
| 1H1ca_00992 | Phosphate uptake regulator, PhoU | 2.25 | 0.26 | 5.98 | 1.24 | 0.036 | |
| 1H1ca_00326 | Potassium-transporting ATPase ATP-binding subunit | 0.64 | 0.04 | 1.41 | 0.2 | 0.023 | |
| 1H1ca_01032 | Putative aminoacrylate hydrolase RutD | 0.66 | 0.17 | 1.46 | 0.29 | 0.026 | |
| 1H1ca_02280 | Sensor histidine kinase | 1.21 | 0.06 | 3.04 | 0.71 | 0.047 | |
| 1H1ca_01311 | Small archaeal modifier protein 3 | 3.14 | 0.33 | 7.96 | 0.98 | 0.015 | |
| 1H1ca_00896 | tRNA(fMet)-specific endonuclease VapC | 2.8 | 0.49 | 6.8 | 1.2 | 0.033 | |
| 1H1ca_02147 | Tryptophan synthase alpha chain | 2.95 | 0.3 | 6.35 | 0.8 | 0.02 | |
| 1H1ca_02148 | Tryptophan synthase beta chain | 3.3 | 0.37 | 8.14 | 0.61 | 0.001 | |
| 1H1ca_01312 | Tungsten-containing aldehyde ferredoxin oxidoreductase | 5.25 | 0.81 | 11.2 | 1.19 | 0.006 | |
| 1H1ca_00037 | V-type ATP synthase alpha chain | 0.41 | 0.03 | 1.01 | 0.21 | 0.04 | |
| 1H1ca_02292 | V-type ATP synthase alpha chain | 0.79 | 0.13 | 6.58 | 1.87 | 0.033 | |
| 1H1ca_02293 | V-type ATP synthase beta chain | 0.8 | 0.08 | 5.37 | 1.41 | 0.03 | |
| 1H1ca_02290 | V-type ATP synthase subunit C | 1.27 | 0.31 | 13.64 | 3.22 | 0.022 | |
| 1H1ca_02294 | V-type ATP synthase subunit D | 2.06 | 0.39 | 6.49 | 0.47 | 0.001 | |
| 1H1ca_02291 | V-type ATP synthase subunit F | 0.66 | 0.14 | 6.29 | 1.46 | 0.022 | |
| 1H1ca_02286 | V-type ATP synthase subunit G | 4.99 | 1.1 | 31.93 | 3.26 | 0.005 | |
| 1H1ca_02287 | V-type ATP synthase subunit I | 2.46 | 0.61 | 12.26 | 1.69 | 0.011 | |
| 1H1ca_02289 | V-type ATP synthase subunit E | 1.64 | 0.48 | 19.88 | 4.32 | 0.018 | |
| 1H1ca_02288 | V-type ATP synthase subunit K | 1.57 | 0.34 | 19.28 | 4.44 | 0.02 | |
These results suggest that strain 1H1Hc7 responded to the change in the chemical equilibrium of CO2 under high pressure. During methanogenesis, formate is initially oxidized to CO2, and this is followed by its reduction to CH4 (Supplementary Fig. S1). However, under elevated pressure, the CO2 produced may be rapidly converted into HCO3– (Abe and Horikoshi, 1998), thereby reducing the pool of CO2 directly available for methanogenesis (Vorholt and Thauer, 1997). Based on calculations using the equation by Millero (Millero, 1995), the CO2 concentration available for methanogenesis is 29.96 mM under atmospheric pressure, but only 0.71 mM under 25 MPa, representing more than a 40-fold decrease. Under bicarbonate-free, HEPES-buffered conditions, formate provides the only carbon input for methane formation, and the stoichiometric mass balance (4HCOOH → CH4+3CO2+2H2O) holds throughout the incubation, reflecting a nearly identical amount of final cumulative methane between 0.1 and 25 MPa. Under these CO2-limited conditions, the up-regulation of the MCR complex may play a key role in maintaining the balance of methyl-group intermediates within the terminal steps of methanogenesis. The reaction catalyzed by methyl-H4MPT:HS-CoM methyltransferase (Mtr), which transfers the methyl group from CH3–H4MPT to HS–CoM, is coupled to Na+ translocation across the membrane and, thus, constitutes an energy-conserving step of the pathway (Gottschalk and Thauer, 2001) (Supplementary Fig. S1). When CO2 availability is restricted, the supply of CH3–H4MPT to the Mtr–MCR module decreases, potentially lowering both methyl flux and Na+-motive energy conservation. By increasing MCR abundance, cells may more effectively consume CH3–S–CoM, keeping its intracellular concentration low and thereby pulling Mtr-coupled methyl transfer forwards. This enhanced flux coupling between Mtr and MCR helps sustain the Na+ motive force and overall energy conservation under kinetically unfavorable, CO2-limited conditions. The concomitant up-regulation of ATPase under pressure further supports this adaptive mechanism by facilitating ion translocation and energy conservation associated with the downstream methyl-transfer reaction or may represent a broader cellular response to pressure stress beyond methanogenesis.
The expression profiles of other methanogenic enzymes support this interpretation. Upstream C1-transfer enzymes—formate dehydrogenase (Fdh), formylmethanofuran dehydrogenase (Fwd), formylmethanofuran-tetrahydromethanopterin formyltransferase (Ftr), methenyl-H4MPT cyclohydrolase (Mch), methylene-H4MPT dehydrogenase (Mtd), methylene-H4MPT reductase (Mer), and Mtr—were not significantly up-regulated (Supplementary Table S1). Since these reactions are near-equilibrium steps with small Gibbs free-energy changes (Thauer, 1998), increasing their enzyme abundance may not contribute to overcoming CO2-limited conditions. In contrast, MCR catalyzes the exergonic step of methanogenesis, allowing it to drive metabolic flux even under thermodynamically constrained conditions.
Carbonic anhydrase is a key enzyme in the CO2-concentrating mechanism, providing an efficient strategy for carbon acquisition in photosynthetic microorganisms under CO2-limited conditions (Aizawa and Miyachi, 1986). Although a gene encoding a putative carbonic anhydrase (1H1ca_01525) was identified in the 1H1Hc7 genome, its expression was similar between 0.1 and 25 MPa, suggesting that strain 1H1Hc7 did not rely on this mechanism under the conditions tested herein. In methanogens, carbonic anhydrase is proposed to catalyze cytoplasmic CO2 conversion to HCO3– during acetoclastic methanogenesis (Alber and Ferry, 1994); however, its physiological function in hydrogenotrophic methanogens remains unclear.
Our in vitro observations have implications for deep subseafloor sediments where the majority of CO2 is converted to HCO3–. In these environments, formate, rather than H2, may serve as an important CO2 sink, favoring hydrogenotrophic methanogenesis. In support of this, four of the six strains of hydrogenotrophic methanogens, including strain 1H1Hc7, which were previously isolated from subseafloor sediments in the Nankai Trough (Katayama et al., 2022), produced methane from formate as the sole substrate (Supplementary Table S3). In addition, 16S rRNA gene amplicon sequencing data indicate that formate-utilizing methanogens are more abundant than non-formate-utilizing methanogens (Supplementary Table S3). Consistently, formate-utilizing methanogenesis has been shown to dominate over H2-utilizing methanogenesis in hyperalkaline environments with extremely limited CO2 availability (Fones et al., 2021). The present results underscore the previously underestimated role of CO2 availability in affecting methanogenic activity and gene expression in the deep biosphere.
Katayama, T., Yoshioka, H., and Nobu, M. K. (2025) High-pressure Methanogenesis Reveals Metabolic Adaptation to Dissolved CO2 Limitation. Microbes Environ 40: ME25066.
https://doi.org/10.1264/jsme2.ME25066
This study was part of the Research Consortium for Methane Hydrate Resources in Japan (MH21) and MH21-S R&D consortium (MH21-S) funded by the Ministry of Economy, Trade and Industry of Japan. The authors thank Than Tin Aung, Toshinori Imai, Miki Amo, Kazuya Naito, and Naoyuki Shimoda in the Japan Organization for Metals and Energy Security (JOGMEC) for their valuable discussions. The authors also thank Ryuji Ohtsuki, Mayumi Takuma, Misa Takenouchi, Sanae Yamaoka, and Rieko Iwanami for their assistance with high-pressure cultivation experiments and molecular analyses.
Conflicts of interestThe authors declare that there are no conflicts of interest.