4.7 Article

Oxidation of H2S and CH3SH in a jet-stirred reactor: Experiments and kinetic modeling

期刊

FUEL
卷 283, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2020.119258

关键词

H2S; CH3SH; Oxidation; JSR; Kinetic modeling

资金

  1. Aragon Government [T22_17R]
  2. FEDER 2014-2020 Construyendo Europa desde Aragon
  3. MINECO [CTQ2015-65226, BES-2016-076610]
  4. FEDER [CTQ2015-65226]
  5. Australian Research Council
  6. College of Engineering at The United Arab Emirates University, UAEU [31N421]

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This contribution presents experimental measurements of H2S and CH3SH oxidation, updates a kinetic model to simulate the data, and demonstrates high agreement between experimental and model results. The oxidation of CH3SH mainly proceeds through an intersystem crossing process, forming sulfine and eventually decomposing into CO + H2S and COS + H2. The results have potential applications in sour gas treatment and energy production.
This contribution reports experimental measurements of the oxidation of H2S and CH3SH, under atmospheric pressure in a jet-stirred reactor (JSR), in the temperature range of 600-1100 K and for stoichiometric and oxidizing conditions. We update a recent kinetic model, originally developed based on the measurements of oxidation of H2S and CH3SH in a tubular flow-reactor and apply it to simulate the experimental data. The CH3SH subset of the kinetic model features new reactions based on a recent theoretical work and the rate parameters proposed in the present investigation. The oxidation of CH3SH proceeds mainly through an intersystem crossing process that leads to the formation of sulfine (CH2SO). The unimolecular decomposition of CH2SO in two competing reactions produces CO + H2S and COS + H-2. The results from the model concur well with the experimental measurements, both from the present work and from the literature. We demonstrate that, both H2S and CH3S exhibit a similar ignition temperature, due to the initiation step that involves the abstraction of H initially bonded to sulfur. It is expected that, the results from the present investigation find application in processing of sour gas, including shale gas, especially in the direct combustion of the gas (i.e., without purification) for energy production.

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