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CO 2 Gasification Reactivity and Syngas Production of Greek Lignite Coal and Ex-Situ Produced Chars under Non-Isothermal and Isothermal Conditions: Structure-Performance Relationships

Author

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  • Athanasios Lampropoulos

    (Department of Mechanical Engineering, University of Western Macedonia, 50100 Kozani, Greece)

  • Vassilios D. Binas

    (Institute of Electronic Structure and Laser, Foundation for Research and Technology-Hellas, 70013 Heraklion, Greece)

  • Leila Zouridi

    (Institute of Electronic Structure and Laser, Foundation for Research and Technology-Hellas, 70013 Heraklion, Greece
    Department of Material Science & Technology, University of Crete, 70013 Heraklion, Greece)

  • Costas Athanasiou

    (Department of Environmental Engineering, Democritus University of Thrace, 67132 Xanthi, Greece)

  • Miguel A. Montes-Morán

    (Instituto de Ciencia y Tecnología del Carbono (INCAR-CSIC), 33010 Oviedo, Spain)

  • J. Angel Menéndez

    (Instituto de Ciencia y Tecnología del Carbono (INCAR-CSIC), 33010 Oviedo, Spain)

  • Michalis Konsolakis

    (School of Production Engineering and Management, Technical University of Crete, 73100 Chania, Greece)

  • George E. Marnellos

    (Department of Mechanical Engineering, University of Western Macedonia, 50100 Kozani, Greece
    Centre for Research & Technology Hellas, Chemical Process & Energy Resources Institute, 57001 Thessaloniki, Greece)

Abstract

The presented work explores the structural properties, gasification reactivity, and syngas production of Greek lignite fuel (LG) and ex-situ produced chars during CO 2 gasification. Three different slow pyrolysis protocols were employed for char production involving torrefaction at 300 °C (LG300), mild-carbonization at 500 °C (LG500), and carbonization at 800 °C (LG800). Physicochemical characterization studies, including proximate and ultimate analysis, X-ray Diffraction (XRD), and Raman spectroscopy, revealed that the thermal treatment under inert atmospheres leads to chars with increased fixed carbon content and less ordered surface structures. The CO 2 gasification reactivity of pristine LG and as-produced chars was examined by thermogravimetric (TG) analysis and in batch mode gasification tests under both isothermal and non-isothermal conditions. The key parameters affecting the devolatilization and gasification steps in the overall process toward CO-rich gas mixtures were thoroughly explored. The gasification performance of the examined fuels in terms of carbon conversion, instant CO production rate, and syngas generation revealed an opposite reactivity order during each stage. TG analysis demonstrated that raw lignite (LG) was more reactive during the thermal devolatilization phase at low and intermediate temperatures (da/dt max,devol. = 0.022 min −1 ). By contrast, LG800 exhibited superior gasification reactivity at high temperatures (da/dt max,gas. = 0.1 min −1 ). The latter is additionally corroborated by the enhanced CO formation of LG800 samples under both non-isothermal (5.2 mmol) and isothermal (28 mmol) conditions, compared to 4.1 mmol and 13.8 mmol over the LG sample, respectively. The pronounced CO 2 gasification performance of LG800 was attributed to its higher fixed carbon content and disordered surface structure compared to LG, LG300, and LG500 samples.

Suggested Citation

  • Athanasios Lampropoulos & Vassilios D. Binas & Leila Zouridi & Costas Athanasiou & Miguel A. Montes-Morán & J. Angel Menéndez & Michalis Konsolakis & George E. Marnellos, 2022. "CO 2 Gasification Reactivity and Syngas Production of Greek Lignite Coal and Ex-Situ Produced Chars under Non-Isothermal and Isothermal Conditions: Structure-Performance Relationships," Energies, MDPI, vol. 15(3), pages 1-19, January.
  • Handle: RePEc:gam:jeners:v:15:y:2022:i:3:p:679-:d:727152
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    References listed on IDEAS

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