Olive trimmings (OT) were used as feedstock for an in-depth experimental study on the reaction kinetics controlling hydrothermal carbonization (HTC). OT were hydrothermally carbonized for a residence time τ of up to 8 h at temperatures between 180 and 250 ◦ C to systematically investigate the chemical and energy properties changes of hydrochars during HTC. Additional experiments at 120 and 150 ◦ C at τ = 0 h were carried out to analyze the heat-up transient phase required to reach the HTC set-point temperature. Furthermore, an original HTC reaction kinetics model was developed. The HTC reaction pathway was described through a lumped model, in which biomass is converted into solid (distinguished between primary and secondary char), liquid, and gaseous products. The kinetics model, written in MATLAB TM , was used in best fitting routines with HTC experimental data obtained using OT and two other agro-wastes previously tested: grape marc and Opuntia Ficus Indica. The HTC kinetics model effectively predicts carbon distribution among HTC products versus time with the thermal transient phase included; it represents an effective tool for R&D in the HTC field. Importantly, both modeling and experimental data suggest that already during the heat-up phase, biomass greatly carbonizes, in particular at the highest temperature tested of 250 ◦ C.

Hydrothermal carbonization kinetics of lignocellulosic agro-wastes: Experimental data and modeling / Lucian, M.; Volpe, M.; Fiori, L.. - In: ENERGIES. - ISSN 1996-1073. - STAMPA. - 12:3(2019), p. 516. [10.3390/en12030516]

Hydrothermal carbonization kinetics of lignocellulosic agro-wastes: Experimental data and modeling

Lucian M.;Volpe M.;Fiori L.
2019-01-01

Abstract

Olive trimmings (OT) were used as feedstock for an in-depth experimental study on the reaction kinetics controlling hydrothermal carbonization (HTC). OT were hydrothermally carbonized for a residence time τ of up to 8 h at temperatures between 180 and 250 ◦ C to systematically investigate the chemical and energy properties changes of hydrochars during HTC. Additional experiments at 120 and 150 ◦ C at τ = 0 h were carried out to analyze the heat-up transient phase required to reach the HTC set-point temperature. Furthermore, an original HTC reaction kinetics model was developed. The HTC reaction pathway was described through a lumped model, in which biomass is converted into solid (distinguished between primary and secondary char), liquid, and gaseous products. The kinetics model, written in MATLAB TM , was used in best fitting routines with HTC experimental data obtained using OT and two other agro-wastes previously tested: grape marc and Opuntia Ficus Indica. The HTC kinetics model effectively predicts carbon distribution among HTC products versus time with the thermal transient phase included; it represents an effective tool for R&D in the HTC field. Importantly, both modeling and experimental data suggest that already during the heat-up phase, biomass greatly carbonizes, in particular at the highest temperature tested of 250 ◦ C.
2019
3
Lucian, M.; Volpe, M.; Fiori, L.
Hydrothermal carbonization kinetics of lignocellulosic agro-wastes: Experimental data and modeling / Lucian, M.; Volpe, M.; Fiori, L.. - In: ENERGIES. - ISSN 1996-1073. - STAMPA. - 12:3(2019), p. 516. [10.3390/en12030516]
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11572/237797
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