Introduction

Since more than 3 decades, reduced organic sulfur compounds have been recognized as substantial biogenic emissions contributing to Earth´s sulfur cycle. The sulfur cycle is highly relevant for the Earth’s climate due to the ability of the sulfur compound’s oxidation products, sulfuric acid (H2SO4) and methane sulfonic acid (MSA, CH3SO3H), to generate new airborne particles that effectively scatter incoming solar radiation and affect the formation of cloud condensation nuclei (CCN)1,2. CCN in turn may have significant influences on the microphysical and radiative properties3 and lifetime4 of clouds.

Globally, the most important organic sulfur compound is dimethyl sulfide (DMS, CH3SCH3) with an annual emission rate of 30 million metric tons of sulfur, followed by methylthiol (MeSH, CH3SH) and, to a lesser extent, dimethyl disulfide (DMDS, CH3SSCH3)5. A large number of experimental and theoretical studies have been conducted to ascertain their atmospheric degradation pathways, especially for DMS6,7,8,9,10,11,12,13,14,15,16,17,18, representing the data base for atmospheric models19,20,21,22. The reaction scheme in Fig. 1 summarises the current knowledge on product formation starting from the methylthiyl (CH3S) and methylsulfonyl radical (CH3SO2), both formed as important intermediates in the gas-phase oxidation of CH3SH, DMS and DMDS. To the best of our knowledge, up to now there is no experimental evidence for the direct gas-phase formation of H2SO4, other than via SO2 oxidation by OH radicals23,24 or Criegee intermediates25,26, although this has been speculated about in the literature for long27,28 and such pathways have already been implemented in models19,20,21,22.

Fig. 1: Reaction scheme of the oxidation of reduced-sulfur emissions, i.e. CH3SH (MeSH, methylthiol), CH3SCH3 (DMS, dimethyl sulfide) and CH3SSCH3 (DMDS, dimethyl disulfide).
figure 1

The scheme focuses on the reaction steps relevant for the formation of H2SO4 and MSA (methane sulfonic acid) starting from CH3S and CH3SO2 and is mainly based on Barnes et al.9. Signals of observed products in the present study are shown in bold. Dashed red arrows indicate complex reactions to the stated intermediates. Only important main products of the individual pathways are displayed.

Here we experimentally demonstrate the direct formation of H2SO4 from the OH radical-initiated gas-phase oxidation of organic sulfur compounds by its direct mass spectrometric detection in two flow systems29,30,31 under atmospheric conditions with residence times of 7.9 and 32 s. Accompanied modelling shows the importance of this direct pathway for the total H2SO4 formation in the atmosphere.

Results and discussion

Detectable products from CH3S oxidation

Product ionization by means of iodide (I-) and nitrate (NO3-) in the mass spectrometric analysis was found as a suitable way to observe product formation, other than SO2, in the oxidation process. Recently, an experimental SO2 yield of 86 ± 18% has been reported for low-NO conditions qualifying SO2 as the predominant product32,33. Figure 2a shows the detected products, other than SO2, from an overview experiment on the oxidation of CH3S initiated by the reaction OH + CH3SH → CH3S + H2O33,34 (Fig. 1). Product ionisation by iodide allowed to follow H2SO4 and MSA, signals consistent with the formation of CH3SO2OONO2 and CH3SO2OOH, which were most likely formed via pathways 12 and 13 (Fig. 1), respectively, and the signal of the intermediate CH3SO2. For the latter, a contribution from CH3SOO cannot be ruled out. It is to be noted here, that H2SO4 formation initiated by OH + SO2 is unimportant under the chosen conditions and, thus, H2SO4 needs to arise from the CH3S oxidation directly, see also Methods. Comparison of the measured product spectra with results from peak fitting of the spectra supports the signal attribution to the five products identified (Fig. 2b and Supplementary Fig. 1). The signals of all closed-shell products steeply increased with rising CH3SH conversion while the CH3SO2 signal levelled off, typical for reactive intermediates. The occurrence of CH3SO2OONO2 and CH3SO2OOH, recently detected from OH + DMS as well14, indicates CH3SO2OO as a significant peroxy species in these reaction systems, which is supported by theoretical calculations35.

Fig. 2: Product detection from CH3S oxidation using ionisation by iodide.
figure 2

Experiments on OH + CH3SH for CH3S production have been conducted in the free-jet flow system, t = 7.9 s, at r.h. = 10%. OH radicals were produced from IPN (isopropyl nitrite) photolysis, i.e. OH radical generation via NO + HO2 → NO2 + OH. Increasing OH radical levels for rising CH3SH conversion were linked by increasing concentrations of NO, NO2 and HO2 due to increasing IPN conversion in the photolysis. Reactant concentrations are stated in Supplementary Table 1. Source data are provided as a Source Data file. a Detected products are given as a function of converted CH3SH. Data for H2SO4 and MSA (methane sulfonic acid) are based on absolute calibration with an uncertainty of 20%. Other concentrations represent lower limits with an uncertainty of a factor of 2. b Measured raw spectrum from 10 min data accumulation compared with calculated signals of iodide adducts with CH3SO2, H2SO4 and MSA from peak fitting.

Basically, the direct observation of CH3SO2 and other intermediates of the CH3S oxidation for close to atmospheric conditions appears to be very challenging36,37. A spectroscopic study on the product formation of CH3S + O2 in cryogenic matrixes unambiguously identified CH3SOO, CH3SO2 and CH3SO2OO as important intermediates supporting the relevance of the reaction sequence 1/−1, 2 and 11/−11 (Fig. 1) in the CH3S oxidation15. Cryogenic matrix techniques in general represent an useful approach for qualitative studying sulfur oxidation38.

Formation of H2SO4 and MSA in our experiments was also observed by means of nitrate ionisation confirming the findings using iodide ionisation (Supplementary Fig. 2).

MSA formation induced by elevated CH3SH and DMDS concentrations

It is remarkable that H2SO4 and MSA concentrations increased almost uniformly with rising CH3SH conversion, which was accompanied by a rising HO2 radical level for the chosen reaction conditions (Fig. 2a and Supplementary Fig. 2). The competing steps 17 vs. 20 imply a decreasing H2SO4/MSA ratio with rising HO2 concentrations (Fig. 1), which is not visible in the experiments (Supplementary Fig. 3). This means that our experimental findings do not support considerable MSA formation via CH3SO3 + HO2 (pathway 20). Moreover, an increasing H2SO4/MSA ratio with decreasing CH3SH concentration was observed for otherwise nearly constant reaction conditions, including CH3SH consumption by the OH reaction and the prevailing HO2 concentration (Fig. 3). The MSA signal practically disappeared for CH3SH concentrations below a few 1010 molecules cm−3. Thus, the reaction of CH3SO3 with CH3SH (pathway 19), likely via H-abstraction of the labile S-bound H atom, seems to dominate the MSA formation under the present conditions. This also means that the direct H2SO4 formation via CH3SO3 decomposition (pathway 17) is supressed in the presence of sufficiently high CH3SH or other substances serving as H-atom donor. A similar behaviour of the H2SO4/MSA ratio was also observed in OH + DMDS experiments varying the DMDS concentrations (Supplementary Fig. 4). Here, almost exclusive H2SO4 formation can be expected for DMDS concentrations below 1010 molecules cm−3.

Fig. 3: Concentrations of H2SO4 and MSA (methane sulfonic acid), and the MSA/H2SO4 ratio as a function of CH3SH concentration.
figure 3

Experiments on OH + CH3SH were carried out in the free-jet flow system at r.h. = 10% and a reaction time of 7.9 s using IPN (isopropyl nitrite) photolysis for OH radical generation. Reactant concentrations are stated in Supplementary Table 1. The error bars for H2SO4 and MSA depict the uncertainty of 20% based on the uncertainty in the calibration factor. Source data are provided as a Source Data file.

Because atmospheric CH3SH and DMDS concentrations are clearly smaller than 1010 molecules cm−3 (400 ppt), see attached Supplementary Dataset 1 and ref. 5, CH3SO3 decomposition (pathway 17) forming finally the direct H2SO4 most likely dominates the fate of CH3SO3 for atmospheric conditions (Fig. 3 and Supplementary Fig. 4). MSA formation according to CH3SO3 + RH for RH ≡ CH3SH or DMDS (pathway 19) has to be of minor importance. It is speculative whether or not other hydrocarbons RH in the atmosphere could efficiently form MSA via pathway 19.

Formation routes to direct H2SO4

We evaluated the impact of atmospheric trace gases, i.e. ozone, RO2 radicals, NO and NO2, in the process of direct gas-phase H2SO4 formation with separate experiments starting from the OH radical reactions with CH3SH and DMDS (Fig. 4). While OH + CH3SH represents a clean source of CH3S with a reported formation yield of 1.1 ± 0.234, OH + DMDS is expected to form CH3S and CH3SOH39,40, which further reacts with ozone leading mainly to CH3SO2 with a yield close to unity for high enough ozone concentrations32. The OH + DMS reaction was not considered in these experiments because of its complexity9,11, which complicates the investigation of selected pathways. Reaction conditions were chosen in such a way that intermediate concentrations were kept as low as possible in order to suppress unwanted bimolecular steps not relevant in the atmosphere. For this reason, the amount of reacted CH3SH and DMDS was limited to a few 108 molecules cm−3. Gas-phase H2SO4 formation starting from the reaction of SO2 with OH radicals or Criegee intermediates was again small in these measurement series and did not influence the results of direct H2SO4 formation significantly, see also Methods.

Fig. 4: Impact of trace gases on direct H2SO4 formation using ionisation by nitrate.
figure 4

Experiments were conducted either in the free-jet flow system, t = 7.9 s, or in the laminar flow tube (LFT), t = 32 s, at r.h. = 10% (or <0.1%) using tetramethyl ethylene (TME) ozonolysis for OH radical production. Reactant concentrations are given in Supplementary Table 1. Error bars represent the uncertainty of 20% in the absolute calibration. Source data are provided as a Source Data file. a Formation of H2SO4 and SO3 as a function of ozone measured in the LFT. Reacted CH3SH was in the range (7.6–17) × 107 and (2.1–18) × 107 molecules cm−3 for DMDS (dimethyl disulfide). b H2SO4 and MSA (methane sulfonic acid) formation from OH + CH3SH depending on RO2 radical concentrations, CH3C(O)CH2O2 and CH3O2, in the LFT. Rising RO2 levels were achieved by stepwise increase of TME and corresponding CH4 additions keeping reacted CH3SH constant at 7.6 × 107 molecules cm−3. Highest CH3C(O)CH2O2 and CH3O2 concentrations were 1.0 × 109 and 8.8 × 108 molecules cm−3, respectively, calculated from an extended model (Supplementary Table 4). c H2SO4 formation yields as a function of NO addition. d H2SO4 formation yields as a function of NO2 addition.

Ozone: No significant H2SO4 formation from OH + CH3SH was observed for ozone concentrations of up to 2 × 1012 molecules cm−3 (80 ppb) in the free-jet flow system with the short reaction time of 7.9 s. H2SO4 became detectable in the laminar flow tube (LFT) with a reaction time of 32 s indicating a relatively slow process of direct H2SO4 formation (Fig. 4a). Big differences in the H2SO4 yields of more than an order of magnitude were measured using either OH + CH3SH for CH3S generation or OH + DMDS forming CH3S and most likely CH3SO2 with high yields. Considering CH3SO2 as the needed intermediate for direct H2SO4 formation (Fig. 1), CH3S´s oxidation obviously proceeds only with a small share via CH3SO2, e.g. ≤ 9% for an ozone concentration of 5.7 × 1011 molecules cm−3 (Fig. 4a) taking OH + DMDS with a CH3SO2 yield of unity as the reference. Moreover, OH + CH3SH experiments with heavy ozone (18O3) revealed the absence of H2SO4 containing three 18O atoms (Supplementary Fig. 5) as expected from the reaction sequence 3, 6b and 9 (Fig. 1). We largely measured H2SO4 with one 18O atom consistent with the reaction sequence 1/−1, 2 and 9. The findings imply the dominance of pathway 6a over 6b or in fact the irrelevance of pathway 6b, allowing for the importance of ozone reactions in the CH3S oxidation8,34,41. This can be explained by the high exothermicity of the CH3SO + O3 reaction forming the chemically excited CH3SO2* that rapidly decomposes to SO2 and CH3 before it is thermalised42.

The small H2SO4 yields < 1% for atmospheric ozone concentrations, even under conditions of the preferred CH3SO2 generation from OH + DMDS, support the efficient decomposition of CH3SO2 (pathway 8), which is in line with the high SO2 yields reported recently32,33. SO3 yields measured under dry conditions, r.h. < 0.1%, were in very good agreement with the H2SO4 yields at r.h. = 10% (Fig. 4a) confirming SO3 as the precursor of H2SO4 (pathways 17 and 18 in Fig. 1).

An ozone concentration of 5.7 × 1011 molecules cm−3 (23 ppb) was chosen in the following experiments, which stands for an average concentration over pristine oceans43, making our findings applicable to the atmospheric reaction system.

RO2 radicals: We detected a distinct impact of RO2 radicals on the formation of H2SO4 and MSA (Fig. 4b). Main RO2 radicals in the reaction system are CH3C(O)CH2O2, formed in the course of OH radical generation via TME ozonolysis44,45, and CH3O2 as the by-product of SO2 in the oxidation of CH3SH and DMDS32,33 as well as from OH + CH4 in the case of CH4 additions. In the OH + CH3SH reaction, we increased in a two-step process the concentrations of CH3C(O)CH2O2 and CH3O2 radicals, first by a factor of 10, i.e. from 6.2 × 107 to 5.7 × 108 and from 4.0 × 107 to 4.4 × 108 molecules cm−3, respectively, leading to enhanced H2SO4 formation by a factor of 3.5 for constant CH3SH conversion (Fig. 4b). Further doubling of the RO2 concentrations led to further rise in H2SO4 productions. The MSA formation, however, increased stronger than that of H2SO4, which became more visible from a similar experiment on OH + DMDS (Supplementary Fig. 6). Furthermore, we observed predominate MSA formation in a reaction system with HO-C6H12O2 along with CH3C(O)CH2O2 as the main RO2 radicals (Supplementary Fig. 7). It can be speculated that most likely CH3SO2OO reacted with RO2 radicals either via the alkoxy channel (pathway 15 in Fig. 1), forming finally H2SO4, or via the dismutation channel (pathway 16 in Fig. 1), similar to the well-known chemistry of carbon-centred RO2 radicals46, leading to MSA. The branching ratio of pathways 15 vs. 16 appears to be dependent on the structure of the reacting RO2 radical. Other RO2 driven pathways, influencing the product formation, cannot be ruled out.

Nitrogen oxide (NO): Addition of NO substantially accelerated the H2SO4 formation in all experiments (Fig. 4c) supporting the potential importance of CH3SO2OO for H2SO4 formation, here via pathway 14 (Fig. 1). An increase in the H2SO4 production by a factor of 4 (Supplementary Fig. 8) was measured using a NO concentration of 1 × 109 molecules cm−3 similar to the behaviour observed for elevated RO2 concentrations (Fig. 4b and Supplementary Fig. 6). This indicates rate coefficients k14 and k15 for the reaction of CH3SO2OO with NO and RO2, respectively, being in the same range. Comparison of results for relatively low NO concentrations of < 1010 molecules cm−3 in the LFT showed more than one order of magnitude higher H2SO4 yields from the oxidation of DMDS relative to CH3SH, in line with the findings from the pure ozone-driven reaction (Fig. 4a). For elevated NO levels, other NO reactions presumably disturbed the CH3SO2 formation from OH + DMDS and inhibited further rise of the H2SO4 yield. Further NO reactions in the CH3S oxidation could also negatively impact the H2SO4 formation, such as CH3S + NO → CH3SNO10 or CH3SOO + NO → CH3SO + NO210 (pathway 5) resulting finally in SO2 formation via pathway 6a (Fig. 1). The higher H2SO4 yields from OH + CH3SH measured in the LFT at t = 32 s point again to a slow process of H2SO4 formation that is far away from completeness for the reaction time of 7.9 s in the free-jet flow system.

Nitrogen dioxide (NO2): Addition of NO2 featured a similar effect for the rise of H2SO4 yields (Fig. 4d) as observed for NO (Fig. 4c), albeit the NO2 impact was less pronounced. It is supposed in the literature that NO2 reacts with CH3SO2 forming CH3SO3 (pathway 10) which finally leads to H2SO4 analogous to the ozone-mediated route (pathway 9)9. This set of experiments confirmed again the much higher potential of H2SO4 formation starting from OH + DMDS regarding OH + CH3SH, as well as the slow formation rate of the direct H2SO4 production. H2SO4 production almost doubled as the result of a NO2 addition of 6.7 × 109 molecules cm−3 in the LFT experiments (Fig. 4d), indicating nearly the same reaction rate in the reaction of CH3SO2 with ozone and NO2 (pathways 9 and 10 in Fig. 1), [O3] = 5.7 × 1011 molecules cm−3. This leads to k9/k10 1/85 being in good agreement with the rate coefficient ratio currently used in models21,22. The experiments with NO2 addition did not allow any conclusions regarding the relative importance of the product channels 7a and 7b from CH3SO + NO2.

In summary, the experiments provided evidence for the promoting effect of each of the four important trace gases for the direct H2SO4 formation. The relatively strong impact caused by RO2 radicals and NO (Fig. 4b and 4c) was surprising, which further highlights CH3SO2OO radicals as important intermediates.

Application to the atmosphere

Adjustments in the H2SO4 yields were needed in order to apply the laboratory findings for atmospheric conditions. The incompleteness of the CH3SO3 conversion due to the short reaction times led to a correcting factor of 1.6 for the H2SO4 yields in the LFT using k17 = 0.076 s−1 at 295 ± 2 K, see Methods. Relatively high CH3SH and DMDS concentrations in the experiments, not present in the atmosphere, necessitated further adjustment by a factor of 1.5 to allow for the suppression of H2SO4 formation in their competing reaction with CH3SO3 forming MSA (pathway 19 in Fig. 1), see Fig. 3 and Supplementary Fig. 4. Adjusted H2SO4 yields for low-NOx conditions and [O3] = 5.7 × 1011 molecules cm−3 were estimated to be 0.074 ± 0.015% per formed CH3S and 0.82 ± 0.02% per formed CH3SO2 (Fig. 4a) assuming a CH3SO2 yield of unity from OH + DMDS. The yields increased to 0.11 ± 0.02% (CH3S) and 1.2 ± 0.2% (CH3SO2) incorporating the “RO2 effect” (Fig. 4b) for total RO2 radical concentrations of 3 × 108 molecules cm−3, that represents an average RO2 level during main CH3S and CH3SO2 production at noon (Supplementary Fig. 9). The ratio k8/(k9×[O3]) 120 (k8/k9 7 × 1013 molecules cm−3) followed from the ozone-driven experiments on OH + DMDS with a H2SO4 yield of 0.82%, that strongly favours SO2 formation from CH3SO2 (pathway 8) being consistent with the high SO2 yields measured32,33. This k8/k9 ratio, however, is in contrast to the implementation in latest atmospheric models, k8/k9 = 9.5 × 1011 molecules cm−321,22, leading to severe overestimation of the modelled CH3SO3 production.

Atmospheric impact

Process model simulations were performed with a complex multiphase chemistry mechanism MCM/CAPRAM47,48 for six different scenarios (Methods and Supplementary Table 2) to assess the importance of the direct gas-phase formation pathway of H2SO4 from DMS and CH3SH oxidation relative to the OH + SO2 reaction under pristine marine conditions. Oxidation of DMDS was neglected because of its relatively small emission5. The model is able to simulate typical DMS and SO2 mixing ratios (see Supplementary Figs. 10 and 11) as measured under marine conditions (Fig. 5a and attached Supplementary Dataset 1) independent of NOx levels assumed in the simulations (Supplementary Fig. 12). The modelled CH3S and CH3SO2 formation rates are provided in Supplementary Table 3 for all six simulations. It can be seen that NOx can likely affect the CH3S formation, but it is less important for CH3SO2 formation. The strongest impact on CH3SO2 production has the HA applied. The modelled CH3S and CH3SO2 formation rates together with the experimental H2SO4 yields of 0.11% (CH3S), 1.2% (CH3SO2) and 100% (SO2) were used to calculate the gas-phase H2SO4 formation rates from the different oxidation pathways and their relative contributions (Fig. 5b). For more clarity, the simulations with higher NOx are not depicted, because of the modelled low effect on CH3S and CH3SO2 formation rates in comparison with the simulation using the smaller NO emission. The data in Supplementary Table 3 reveal that the modelled CH3S and CH3SO2 formation rates are only weakly affected by ten times higher NOx emissions, whereas the considered uptake parameters are the most important influencing factors. As the result, the direct gas-phase formation of H2SO4 arises mainly from the DMS addition channel and can contribute up to 50% to the overall gas-phase H2SO4 production. This emphasises the importance of the direct gas-phase formation route for marine conditions. Fully neglecting the share from the DMS addition channel because of inconsistent CH3SO2 yields currently in the literature9,19,49, still a fraction of up to 12% remains (Fig. 5b). It should be noted, that total direct gas-phase H2SO4 formation rates exclusively simulated by the model (Supplementary Fig. 13) exceeded those from the combined experiment/model approach (Fig. 5b) by about two orders of magnitude. A main reason for that is the inappropriate description of CH3SO2´s fate in the latest models21,22.

Fig. 5: Measured DMS (dimethyl sulfide) and SO2 data and the contribution of different pathways to H2SO4 formation.
figure 5

Source data are provided as a Source Data file. a Measured average DMS concentrations (colour coded) worldwide with corresponding SO2/DMS ratios (numbers), if available. The map plot was created with R68 using the ggplot2 package (map_data(“world”)). b Calculated H2SO4 formation rates from different pathways combining the modelled CH3S and CH3SO2 formation rates with experimentally determined H2SO4 yields. The “Cloud” scenario represents simulations with cloud passages leading to lower SO2 concentrations due to its uptake and oxidation in clouds. The simulations with “lower HA” represent model runs using lower Henry constants HA of DMS oxidation products (see Supplementary Table 1). c Reproduction of measured SO2 (black line with squares) and DMS (red line with dots) concentrations as well as its SO2/DMS ratio (blues crosses) from observations at Baring Head, New Zealand50. Purple and yellow bars illustrate the calculated relative contributions of DMS (direct route) and SO2 oxidation to total H2SO4 formation at daytime. The contributions are calculated based on results from “no Cloud” simulation.

The simulations indicate that the concentration ratio of SO2 relative to the reduced-sulfur compounds, mainly DMS, is a critical parameter for the importance of the direct gas-phase H2SO4 formation. This becomes apparent using data from a field campaign at Baring Head, New Zealand50, with an air mass change from anthropogenically influenced, SO2/DMS > 10, to the clean pristine ocean regime, SO2/DMS < 0.1 (Fig. 5c). Significant relevance of the direct gas-phase H2SO4 route only exists for SO2/DMS ≤ 0.3. Thus, the direct gas-phase route could be important especially in the Southern Hemisphere, due to low SO2/DMS ratios existing there (Fig. 5a), and in the outflow of convective marine clouds where SO2 is reduced by scavenging and cloud chemistry.

Field studies often indicated new particle formation in the direct vicinity above marine clouds51,52 most likely connected to the high OH radical53 and H2SO4 concentrations54 observed at such locations. Updrafts of clouds can inject DMS into the free troposphere. There, we suggest that the direct gas-phase H2SO4 formation DMS → H2SO4, as identified in the present study, play an important role for gas-phase H2SO4 production in cloud outflows, because of the expected low SO2/DMS ratio immediately after cloud passage and the slow overall process DMS → SO2 → H2SO4. This implies that directly formed gas-phase H2SO4 from DMS oxidation is likely substantial for the observed new particle formation in cloud outflows, thereby affecting or even controlling the amounts of CCN available51,52,55. Therefore, this study provides the impetus for further developments to incorporate and study such processes in regional and global atmospheric chemistry transport as well as climate models.

In conclusion, we experimentally demonstrated the direct formation of H2SO4 in the course of atmospheric gas-phase oxidation of reduced-sulfur compounds. We found strong indications for the reactions CH3SO2 + O3 (pathway 9) and CH3SO2OO + RO2 (pathway 15) being the rate limiting steps for H2SO4 production under low-NOx conditions. The strong increase of H2SO4 production in the presence of NO emphasises the role of CH3SO2OO radicals in this reaction system. Our findings do not support considerable MSA formation via the CH3SO3 + HO2 pathway.

Although the direct H2SO4 formation yields appear to be pretty small, for concentration ratios SO2/DMS ≤ 0.3, i.e. for conditions as encountered especially over the oceans in the Southern Hemisphere, and/or in the outflows of clouds, the direct route could be competitive with the established OH + SO2 path of H2SO4 generation.

All in all, we herewith suggest direct gas-phase formation of H2SO4 from reduced-sulfur compounds, such as DMS, to be an atmospherically relevant process for the production of H2SO4, and consequently for the formation of new particles, under, e.g. the pristine marine conditions in the Southern Hemisphere.

Methods

Experimental setup

The investigations were carried out in two flow systems, i.e. in the free-jet flow system30,31 and the laminar flow tube (LFT)29 at 1 bar of air and a temperature of 295 ± 2 K. The flow tubes worked with different residence times, 7.9 and 32 s, respectively, that allowed to draw a conclusion regarding the rate of relatively slow processes, here on the thermal decomposition of CH3SO3.

The free-jet flow system consists of an outer tube (length: 200 cm, inner diameter: 16 cm) and a moveable inner tube (outer diameter: 9.5 mm) connected with a nozzle of 3 mm inner diameter. The first reactant (isopropyl nitrite (IPN) or ozone) premixed with air (5 litre min−1, STP) was injected through the inner tube into the main gas stream (95 litre min−1, STP), which contained the second reactant (CH3SH and/or tetramethyl ethylene (TME) along with additions if needed) diluted in air. Downstream the nozzle, large differences of the gas velocities at the nozzle outflow (nozzle: 15.9 m s−1; main flow: 0.13 m s−1) and the nozzle geometry ensured rapid turbulent reactant mixing56. The reaction time was 7.9 s, experimentally obtained by a “chemical clock”. This set-up allows to carry out investigations under atmospheric conditions in absence of wall effects. IPN photolysis57 for continuous OH radical generation in the flow system was conducted downstream the mixing point of the reactants by means of 8 NARVA 36 W Blacklight Blue lamps emitting in the range 350–400 nm. The photolysis of IPN produces NO and i-C3H7O radicals, which rapidly formed acetone and HO2 radicals in the reaction with O2. OH radical generation finally took place via HO2 + NO → OH + NO2. Ozonolysis of TME44 served as non-photolytic OH radical source under low-NOx conditions.

The laminar flow tube (LFT) (i.d. 8 cm; total length 425 cm) consists of a first section (56 cm) containing the gas inlet system, a second middle section (344 cm) representing the reaction zone and an end section (25 cm) incorporating the sampling devices. Here, TME ozonolysis was exclusively used for OH radical formation. Ozone was injected through a nozzle system into the gas mixture, containing TME, reduced-sulfur compounds and additives if needed, just before entering the middle section. The total flow was set at 30 litre min−1 (STP) resulting in a residence time of 32 s in the reaction zone.

Humidified air in both setups was supplied by flushing a part of the air flow through three water saturators filled with water from an ultrapure water system (Barnstead, resistivity: 17.4 MΩ cm). The relative humidity of the reaction gas was continuously controlled at the outflow by a humidity sensor (Hygrosense HYTE). Ozone was monitored by a gas monitor (Thermo Scientific iQ 49) and the concentration of organic compounds by a proton transfer reaction - mass spectrometer (Ionicon, high sensitivity PTR-MS)58. The “crude” air was taken from a pressure swing adsorption unit with further purification by means of absorber units filled with charcoal, a hopcalite (CuMnOx) catalyst59 and different activated 4 Å and 10 Å molecular sieves.

Reactant concentrations and conversion and the importance of OH + SO2 and Criegee intermediate + SO2

Initial reactant concentrations are either given in Supplementary Table 1 for the experiments described in the main text, Figs. 24, or in the figure captions. The amount of reacted CH3SH in the IPN photolysis experiment (Fig. 2a) was measured in an additional run in the presence of SO2 (for otherwise identical reaction conditions) by monitoring H2SO4 formation. The SO2 concentration, 7.5 × 1011 molecules cm−3, was chosen to such an extent that only 2% of formed OH radicals reacted with SO2 and, thus, the product formation of the OH + CH3SH reaction was not disturbed12. Reacted CH3SH is available from the measured H2SO4 (after correction of the fraction arising from CH3SH oxidation) considering the OH reactivity in the parallel reactions OH + CH3SH and OH + SO2. In the case of TME ozonolysis for OH production, the amount of reacted CH3SH or DMDS was calculated based on a detailed reaction scheme (Supplementary Table 4). Modelling calculations, including the IPN photolysis experiment, confirmed that H2SO4 production starting from the reaction of SO2 with OH radicals or Criegee intermediates did not significantly influence the results of direct H2SO4 formation from the organic sulfur compounds.

Mass spectrometric analysis

Detection of H2SO4, CH3SO3H and other oxidation products was carried out using a CI-APi-TOF (chemical ionisation - atmospheric pressure interface - time-of-flight) mass spectrometer with a resolving power > 3000 Th/Th (Tofwerk) connected to a Boulder-type inlet system (Airmodus) operating with iodide (I-) and nitrate (NO3-) as the reagent ions at atmospheric pressure12,31.

In the case of ionisation by iodide, tert-butyl iodide premixed in a flask was added to a 35 litre min−1 (STP) sheath flow of purified nitrogen leading to a tert-butyl iodide concentration of 4.8 × 1011 molecules cm−3. Produced ions after ionisation with a 241Am source were I- and to a lesser amount I(H2O)-. The ions from the sheath flow were guided into the sample flow by an electric field without mixing of both gas streams. In the case of ionisation by nitrate, an HNO3 containing vial was connected to the 35 litre min−1 (STP) flow without overflowing the HNO3 sample. HNO3 diffusion from the vial was found to be sufficient to form the reagent ions (HNO3)xNO3-, x = 0, 1, 2, after ionisation.

Absolute signal calibration was used in the measurements of H2SO4 applying iodide and nitrate ionisation as well as in the determination of SO3, which was detected as the adduct (SO3)NO3- and SO4-60,61 using nitrate ionisation. H2SO4 and SO3 production in the calibration experiments for wet (r.h. = 10%) and dry (r.h. <0.1%) conditions, respectively, was carried out via TME ozonolysis in the presence of SO262. The calibration factors obtained for H2SO4 were also taken for CH3SO3H. In the case of CH3SO2, CH3SO2OOH and CH3SO2OONO2, a calculated calibration factor of 2 × 109 molecules cm−3 was taken, resulting in lower limit concentrations for these products with an uncertainty of a factor of two31,45.

Kinetic data analysis

H2SO4 and MSA wall loss in the LFT:

The rate law for H2SO4 is given by

$$\frac{d\left[{{H}_{2}{SO}}_{4}\right]}{{dt}}=\,{P}_{{{H}_{2}{SO}}_{4}}-{k}_{{loss}}\, \times \,[{{H}_{2}{SO}}_{4}]$$
(1)

assuming a time-independent production term of H2SO4, \({P}_{{{H}_{2}{SO}}_{4}}\). This assumption is justified because of constant OH radical production during the whole reaction time and practically constant reactant concentrations due to reactant conversions clearly smaller than 1% in each case. Integration of Eq. (1) with \({[{{H}_{2}{SO}}_{4}]}_{t=0}\) = 0 yields:

$${[{{H}_{2}{SO}}_{4}]}_{t}=\frac{{P}_{{{H}_{2}{SO}}_{4}}}{{k}_{{loss}}}\,\left(1-\exp \left({-k}_{{loss}}\,{{\times }}\,t\right)\right)$$
(2)

\({[{{H}_{2}{SO}}_{4}]}_{t}={P}_{{{H}_{2}{SO}}_{4}}{\times }{t}\) follows for the wall-loss free H2SO4 concentration. Consequently, the relative H2SO4 loss in the tube is given by:

$${{H}_{2}{SO}}_{4}\,{loss}=1-\frac{1}{{k}_{{loss}}\,{{\times }}\,t}\left(1-\exp \left({-k}_{{loss}}\,{{\times }}\,t\right)\right)$$
(3)

The value of \({k}_{{loss}}\) can be described by the diffusion-controlled wall-loss term \(\frac{3.65{x\;D}}{{r}^{2}}\) using an experimentally obtained H2SO4 diffusion coefficient D = 0.08 cm2 s−163 leading to \({k}_{{loss}}\) = 0.018 s−1. Based on that and for the reaction time of 32 s in the LFT, a H2SO4 loss of 24% was calculated using Eq. (3). Thus, the measured H2SO4 concentration was multiplied with 1.315 to consider the wall loss. The same was applied for MSA.

Determination of k17 describing CH3SO3 → SO3 + CH3:

Assuming dominant loss of CH3SO3 via its decomposition into SO3 and CH3 and a time-independent production term of CH3SO3, \({P}_{{{{CH}}_{3}{SO}}_{3}}\), due to practically constant reactant conditions, the rate law of CH3SO3 is given by:

$$\frac{d\left[{{{CH}}_{3}{SO}}_{3}\right]}{{dt}}=\,{P}_{{{{CH}}_{3}{SO}}_{3}}-{k}_{17}\, \times \,[{{{CH}}_{3}{SO}}_{3}]$$
(4)

Integration of Eq. (4) with \({[{{{CH}}_{3}{SO}}_{3}]}_{t=0}\) = 0 yields:

$${[{{{CH}}_{3}{SO}}_{3}]}_{t}=\frac{{P}_{{{{CH}}_{3}{SO}}_{3}}}{{k}_{17}}\,\left(1-\exp \left({-k}_{17}\,{{\times }}\,t\right)\right)$$
(5)

The rate law of SO3 formation is

$$\frac{d[S{O}_{3}]}{dt} ={k}_{17}{\times }[C{H}_{3}S{O}_{3}]\\ ={P}_{C{H}_{3}S{O}_{3}}{\times }(1-\exp (-{k}_{17}{\times }t))$$
(6)

leading after integration with \({[{{SO}}_{3}]}_{t=0}\) = 0 to:

$$\frac{{[{{SO}}_{3}]}_{t}}{{P}_{{{{CH}}_{3}{SO}}_{3}}}=t-\,\frac{1}{{k}_{17}}\,\left(1-\exp \left({-k}_{17}\,{{\times }}\,t\right)\right)$$
(7)

Because of immediate SO3 conversion to H2SO4 under humid conditions, Eq. (7) can be written in the following way:

$$\frac{{[{{H}_{2}{SO}}_{4}]}_{t}}{{P}_{{{{CH}}_{3}{SO}}_{3}}}=t-\,\frac{1}{{k}_{17}}\,\left(1-\exp \left({-k}_{17}\,{{\times }}\,t\right)\right)$$
(8)

Equation (8) was used to determine \({k}_{17}\) based on measured H2SO4 concentrations from OH + CH3SH depending on NO2 additions in both flow systems, i.e. in the free-jet flow system with t = 7.9 s and in the LFT with t = 32 s for otherwise similar conditions (Supplementary Fig. 14 and Fig. 4d). The ratio \({[{{{{{{{\rm{H}}}}}}}_{2}{{{{{\rm{SO}}}}}}}_{4}]}_{32{{{{{\rm{s}}}}}}}\)/\({[{{{{{{{\rm{H}}}}}}}_{2}{{{{{\rm{SO}}}}}}}_{4}]}_{7.9{{{{{\rm{s}}}}}}}\) was found to be 4.5 ± 0.6 with a corresponding ratio of the CH3SO3 production rates \({P}_{{{{CH}}_{3}{SO}}_{3}}\) of 1/2.27, that considered the different reactant concentrations in the experiments and the fraction of OH radicals reacting with CH3SH. For the mean H2SO4 ratio of 4.5, \({k}_{17}\) = 0.076 s−1 was calculated leading to \({0.076}_{-0.025}^{+0.034}\) s−1 that involves the bounds of the H2SO4 ratio.

Based on Eq. (9), which corresponds to Eq. (3) for H2SO4 loss,

$${{{CH}}_{3}{SO}}_{3}\,{decomposition}=1-\frac{1}{{k}_{17}\,{{\times }}\,t}\left(1-\exp \left({-k}_{17}\,{{\times }}\,t\right)\right)$$
(9)

it was possible to calculate with \({k}_{17}\) = 0.076 s−1, that 62% of formed CH3SO3 decomposed in the LFT (t = 32 s) making a correction factor of 1.6 necessary in order to account for total removal via pathway 17. It is to be noted, that the reaction of CH3SH with CH3SO3, pathway 19, does not influence this result as long as the contribution of this pathway (same CH3SH concentration) is identical in both flow experiments.

Atmospheric modelling

Complex multiphase chemistry simulations were performed using the SPectral Aerosol Cloud Chemistry Interaction Model (SPACCIM)64 to study the contributions of different reaction pathways from DMS, SO2 and CH3SH leading to sulfuric acid or its precursors under pristine marine conditions. It should be noted, that the applied model is not designed to simulate new particle formation. Thus, nucleation driven by gas-phase H2SO4 and resulting effects cannot be investigated. Therefore, we only focus on the chemical gas-phase H2SO4 formation in the present study.

In the model, the multiphase chemistry is described by combining the near-explicit gas-phase mechanism MCMv3.265,66 and detailed aqueous-phase chemistry mechanism CAPRAM4.0 (Chemical Aqueous Phase RAdical Mechanism version 4.0)47, respectively. This mechanism system describes the formation of gas-phase H2SO4 and aqueous sulfate in a very detailed manner. The representation of the specific multiphase chemistry of reactive halogen species and dimethyl sulfide, important for the marine atmosphere, is achieved through two additional reaction modules, CAPRAM–HM3.048 and CAPRAM–DM1.021. With these two additional modules, CAPRAM4.0 includes almost all known sulfate formation pathways in the atmospheric aqueous phase, such as S(IV) oxidation by H2O2, O3, HNO4, reactive halogen species (X2- radical or HOX, with X = Cl, Br or I) or transition metal ions.

Due to the intended foci of the simulations, the complex multiphase DMS chemistry scheme of CAPRAM-DM1.0 has been upgraded with recent mechanism updates and an oxidation scheme for CH3SH was implemented (Supplementary Table 5). The mechanistic updates comprise the formation of the hydroperoxymethyl thioformate (HPMTF) and its further oxidation in the gas phase. The gas-phase HPMTF oxidation follows mainly the proposed routes described by Wu et al. (2015)11, considering SO2 or OCS formation, only. Thus, HPMTF cannot contribute to the direct gas-phase formation of H2SO4 in this mechanism. Phase transfer and subsequent aqueous-phase processing of HPMTF, not included yet because of the current high uncertainties, do not change this. Briefly, the revised mechanism scheme contains 128 gas-phase reactions, 5 phase transfer processes and 50 aqueous-phase reactions.

In the process simulations, an aerosol particle spectrum representative for pristine marine conditions is included67. The whole model setup (emission, deposition, initialisation of the gas-phase and particle-phase composition) is the same as applied in previous DMS chemistry studies21,48. An exception is the newly included emission of CH3SH (emission rate: 3.18 × 103 molecules cm−3 s−1), which is a factor of ten lower compared to that of DMS. This difference is in line with field measurements, see attached Supplementary Dataset 1.

In total, six simulations were performed, separated into (i) three with (“Cloud”) and (ii) three without (“no Cloud”) cloud processing along the air parcel trajectory. The total simulation time is 108-hours but only day 2 to 4 were considered for data analysis to avoid spin-up effects. Runs are performed for summer conditions, with a boundary layer temperature and relative humidity of 280 K and 70% during non-cloud periods. In the simulations with cloud interactions, eight non-permanent clouds are considered. Every cloud exists for about two hours and occurs around noon and midnight, respectively. Cloud formation is achieved through adiabatic cooling of the air parcel 15 minutes before 11 a.m. and p.m., and the cloud evaporation is realised by adiabatic warming 15 minutes after 1 p.m. and a.m., respectively. Besides the two microphysical scenarios (“Cloud”, “no Cloud”), simulations were run with Henry’s Law constants implemented in the base mechanism21 and with lower Henry’s Law constants for DMSO (HA,298K = 2.43 × 105 mol atm−1), DMSO2 (HA,298K = 1.18 × 106 mol atm−1), and MSIA (HA,298K = 1.69 × 106 mol atm−1) calculated by COSMOtherm22. The two uptake cases were performed to consider the potential uncertainty in the Henry’s Law constants and to study their impact of the sulfuric acid formation. In addition, simulations with an increased NO emission by a factor of ten were run using Henry’s Law constants implemented in the base mechanism. All simulation scenarios together with their individual configurations are outlined in Supplementary Table 2.

For the six different simulations, averaged net rates (in molecules cm−3 s−1) for the daytime oxidation of DMS, CH3SH and SO2 between the second to the fourth model day were calculated as well as primary daytime production rates of CH3S and CH3SO2. For the oxidation of DMS, we distinguish between rates of the addition and abstraction pathways. All calculated rates are given in Supplementary Table 3.