4.7 Article

Combustion chemistry of COS and occurrence of intersystem crossing

期刊

FUEL
卷 283, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2020.119257

关键词

Carbonyl sulfide; Inter-system crossing (ISC); Jet-stirred reactor (JSR); Kinetic modelling; Combustion of reduced sulfur species

资金

  1. Australian Research Council (ARC)
  2. College of Engineering at The United Arab Emirates University, UAEU [31N421]

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This study combines experiments with kinetic modelling to investigate the unconventional behavior of carbonyl sulfide (COS) oxidation. By measuring and modeling, it was found that an intersystem crossing process occurs during the reaction of COS, providing a new way to design SOx mitigation processes and handle sulfur impurities in fuels.
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 + O-2 -> 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 + O-2 -> 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.

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