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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Ahrenfeldt, Jesper
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Topics
Publications (11/11 displayed)
- 2023Influence of wood pellets properties on their grinding performancecitations
- 2019From wood chips to pellets to milled pellets: The mechanical processing pathway of Austrian pine and European beechcitations
- 2017Full-scale Milling Tests of Wood Pellets for Combustion in a Suspension-Fired Power Plant Boiler
- 2017Changes imposed by pyrolysis, thermal gasification and incineration on composition and phosphorus fertilizer quality of municipal sewage sludgecitations
- 2016Closing the Loop - Utilization of Secondary Resources by Low Temperature Thermal Gasification
- 2014Kinetic model for torrefaction of wood chips in a pilot-scale continuous reactorcitations
- 2012Fuel Pellets from Wheat Straw: The Effect of Lignin Glass Transition and Surface Waxes on Pelletizing Propertiescitations
- 2012Changes of chemical and mechanical behavior of torrefied wheat strawcitations
- 2012Quality effects caused by torrefaction of pellets made from Scots pinecitations
- 2011Pelletizing properties of torrefied sprucecitations
- 2007High temperature electrolyte supported Ni-GDC/YSZ/LSM SOFC operation on two-stage Viking gasifier product gascitations
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article
Kinetic model for torrefaction of wood chips in a pilot-scale continuous reactor
Abstract
Torrefaction is a mild thermal treatment (200-300 °C) in an inert atmosphere, known to increase the energy density of biomass by evaporation of water and a proportion of the volatiles. In this work a "two-step reaction in series" model was used to describe the thermal degradation kinetics of pine wood. The kinetic parameters were determined using a thermogravimetric analyzer (TGA) and the mass loss during the initial heating period was taken into account when deriving the kinetic parameters. It was shown that the experimental results at different heating rates (10-50 °C min-1) are in good accordance with the model data. In an additional step a continuous, pilot scale reactor was built to produce torrefied wood chips in large quantities. The "two-step reaction in series" model was applied to predict the mass yield of the torrefaction reaction. Parameters used for the calculation were the temperature along the reactor and the biomass feeding rate in combination with the kinetic parameters obtained from the tests in the TGA. Together with results from a laboratory scale, batch torrefaction reactor that was used to determine the higher heating value (HHV) and mass loss (y) of the same material at different torrefaction temperatures, it was possible to predict the HHV of torrefied wood chips from the pilot reactor. The results from this study and the presented modeling approach can be used to predict the product quality from pilot scale torrefaction reactors based on small scale experiments and could be used to improve the homogeneity of torrefied products, which still is a problem for most operational torrefaction pilot plants today. © 2014 Elsevier B.V.