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Hydrogen sulfide (H2S) is produced in a wide range of anoxic environments where sulfate (SO42−) reduction is coupled to decomposition of organic matter. In the same environments, methane (CH4) is the end product of an anaerobic food chain and both H2S and CH4 diffuse upwards into oxic zones where aerobic microorganisms can utilize these gases. Methane-oxidizing bacteria are known to oxidize a major part of the produced CH4 in these ecosystems, mitigating the emissions of this potent greenhouse gas to the atmosphere. However, how methanotrophy is affected by toxic H2S is largely unexplored. Here, we show that a single microorganism can oxidize CH4 and H2S simultaneously. By oxidizing H2S, the thermoacidophilic methanotroph Methylacidiphilum fumariolicum SolV can alleviate the inhibitory effects on CH4 oxidation. In response to H2S, strain SolV upregulated a type III sulfide:quinone oxidoreductase (SQR) and a sulfide-insensitive ba3-type terminal oxidase to dissipate the reducing equivalents derived from H2S oxidation. Through extensive chemostat cultivation of M. fumariolicum SolV we demonstrate that it converts high loads of H2S to elemental sulfur (S0). Moreover, we show chemolithoautotrophy by tracing 13CO2 fixation into new biomass by using H2S as sole energy source. Molecular surveys revealed several putative SQR sequences in a range of proteobacterial methanotrophs from various environments, suggesting that H2S detoxification is much more widespread in methanotrophs than previously assumed, enabling them to connect carbon and sulfur cycles in new ways.

Acid-tolerant ammonia-oxidizing bacteria (AOB) can open the door to new applications, such as partial nitritation at low pH. However, they can also be problematic because chemical nitrite oxidation occurs at low pH, leading to the release of harmful nitrogen oxide gases. In this publication, the role of acid-tolerant AOB in urine treatment was explored. On the one hand, the technical feasibility of ammonia oxidation under acidic conditions for source-separated urine with total nitrogen concentrations up to 3.5 g-N L−1 was investigated. On the other hand, the abundance and growth of acid-tolerant AOB at more neutral pH was explored. Under acidic conditions (pH of 5), ammonia oxidation rates of 500 mg-N L−1 d−1 and 10 g-N g-VSS-1 d-1 were observed, despite high concentrations of 15 mg-N L−1 of the AOB-inhibiting compound nitrous acid and low concentration of 0.04 mg-N L−1 of the substrate ammonia. However, ammonia oxidation under acidic conditions was very sensitive to process disturbances. Even short periods of less than 12 h without oxygen or without influent resulted in a complete cessation of ammonia oxidation with a recovery time of up to two months, which is a problem for low maintenance applications such as decentralized treatment. Furthermore, undesirable nitrogen losses of about 10% were observed. Under acidic conditions, a novel AOB strain was enriched with a relative abundance of up to 80%, for which the name “Candidatus (Ca.) Nitrosacidococcus urinae” is proposed. While Nitrosacidococcus members were present only to a small extent (0.004%) in urine nitrification reactors operated at pH values between 5.8 and 7, acid-tolerant AOB were always enriched during long periods without influent, resulting in an uncontrolled drop in pH to as low as 2.5. Long-term experiments at different pH values showed that the activity of “Ca. Nitrosacidococcus urinae” decreased strongly at a pH of 7, where they were also outcompeted by the acid-sensitive AOB Nitrosomonas halophila. The experiment results showed that the decreased activity of “Ca. Nitrosacidococcus urinae” correlated with the limited availability of dissolved iron at neutral pH., Water Research X, 17, ISSN:2589-9147