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A single model-free rate expression describing both non-isothermal and isothermal pyrolysis of Norway Spruce
Department of Chemical Engineering and Technology, KTH Royal Institute of Technology, Stockholm, Sweden.ORCID iD: 0000-0002-2068-357X
Department of Chemical Engineering and Technology, KTH Royal Institute of Technology, Stockholm, Sweden.ORCID iD: 0000-0001-7995-3151
Department of Fibre and Polymer Technology, KTH Royal Institute of Technology, Stockholm, Sweden.ORCID iD: 0000-0002-0252-337X
2015 (English)In: Fuel, ISSN 0016-2361, E-ISSN 1873-7153, Vol. 161, p. 59-67Article in journal (Refereed) Published
Abstract [en]

A strictly isoconversional rate expression has been derived for pyrolysis of biomass. This rate expression, derived from non-isothermal thermogravimetric experiments using heating rates 2-10 K/min, can successfully predict the conversion rates of experimental data at heating rates 1-100 K/min and quasiisothermal experiments at 539-650 K. The methodology used is based on an extension of the incremental integral method by Vyazovkin (2001). Being able to derive an intrinsic reaction rate expression from non-isothermal data, without any assumption regarding the chemical processes present, opens up for the possibility to model industrial pyrolysis reactors, with a variety of temperature profiles.

Place, publisher, year, edition, pages
Elsevier, 2015. Vol. 161, p. 59-67
Keywords [en]
Model-free, Isoconversional, Pyrolysis, Biomass, Thermogravimetry, Kinetics
National Category
Energy Engineering Chemical Sciences
Identifiers
URN: urn:nbn:se:his:diva-15875DOI: 10.1016/j.fuel.2015.08.019ISI: 000362304600008Scopus ID: 2-s2.0-84940476206OAI: oai:DiVA.org:his-15875DiVA, id: diva2:1229009
Funder
Swedish Energy Agency
Note

Páscoa Dos Santos Magaia is gratefully acknowledged for developing and performing the proximate analysis on spruce. The authors would also like to thank Elisabet Brännvall and Daniel Tavast for providing the milled spruce and performing the wet analysis characterization on this sample. This work was carried out within the Swedish Gasification Centre consortium. Funding from the Swedish Energy Agency and the academic and industrial partners is gratefully acknowledged. Rosana Moriana acknowledges financial support by the Wallenberg and Lars-Erik Thunholm Foundation. Finally the authors would like to thank the reviewers of this work for their constructive comments.

Available from: 2015-11-17 Created: 2018-06-29 Last updated: 2025-09-29Bibliographically approved

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Moriana, Rosana

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