Abstract

This contribution combines results of experiments with kinetic modelling to probe the unusual behaviour of carbonyl sulfide (COS), a sulfur species that frequently arises in fuel systems. The experiments identified CO and SO2 as the primary oxidation products, with no formation of CO2. The low ignition temperature (<600 K) of COS observed in prior experiments conflicts with the high activation barrier for the reaction COS + O2 → CO2 + SO of 211.3 kJ mol−1 on the traditional triplet reaction surface. We proposed that, this kinetic barrier prompts the reaction to transfer onto the singlet surface through intersystem crossing that allows the process to surmount lower-energy hurdles. By considering the oxidation of COS as a single step reaction, we fitted the Arrhenius parameter for the reaction COS + O2 → CO + SO2 directly from our experimental measurements. The fitted activation energy of 70.1 kJ∙mol−1 agrees with that of 85.4 ± 20.0 kJ∙mol−1 as calculated in literature at the Hartree-Fock level of theory, indicating the appearance of the intersystem crossing process in the oxidation of COS. The reaction mechanism based on this comportment leads to excellent agreement between the kinetic model and the experimentally measured quantities, such as the onset temperature and the conversion profiles of detected species. The proposed kinetic model for the oxidation of COS provides a tool to design both the SOx mitigation processes and industrial systems for safe handling of sulfur impurities in fossil fuels.

Highlights

  • The presence of sulfur impurities in bio and fossil fuels affects the combustion process, requiring detailed understanding of the oxidation reactions [1] to design air-purification devices to avoid pollution [2,3]

  • Significant quantities of CS2 and carbonyl sulfide (COS) materialise during the thermal-oxidative reaction of sulfur-containing species in presence of hydrocarbons, such as in fuel-rich oxidation of methane seeded with H2S [10,11,12,13] or during the pyrolysis of ethylene doped with SO2 [14,15,16,17]

  • The jet-stirred reactor approximates well the ideal continuous stirred tank reactor (CSTR), with CSTR named as the perfectly-stirred reactor (PSR) in the combustion literature [46]

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Summary

Introduction

The presence of sulfur impurities in bio and fossil fuels affects the combustion process, requiring detailed understanding of the oxidation reactions [1] to design air-purification devices to avoid pollution [2,3]. The crossing-over between the triplet (ground state) and singlet (excited state) reaction surfaces prevails in oxidation of reduced sulfur species, including the reactions of 1H2S + 3O2 [41], 2SH + 2SH [42], 1CS2 + 3O2 [36], 1CS + 3O2 [26], 1COS + 3O2 [40], 3S + 3O2 [43] and 3SO + 3O2 [26]. Our measurements of the oxidation of CS2 in the jet-stirred reactor required a higher rate for Reaction R1 (where we explicitly denote the triplet species by a digit “3′′ written in the superscript) in the subset mechanism of COS/O2 to match the faster conversion and a lower accumulation of COS as observed in the experiments. We validate the updated mechanism against the experimental measurements of other researchers and discuss the influ­ ence of moisture in the oxidation of COS

Methodology
Experimental results for oxidation of COS
Kinetic modelling of oxidation of COS
Validation of updated mechanism with literature data
Conclusions
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