Torrefaction Kinetics of Norwegian Biomass Fuels

Torrefaction kinetics of Norwegian biomass fuels, including spruce (softwood) and birch (hardwood) was studied using a thermogravimetric analyser. Small samples of approximately 10 mg and particle size of 63-125 µm were heated at a constant heating rate of 5 °C/min and kept afterwards for 4 hours in...

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Main Authors: Q.V. Bach, R. Khalil, O. Skreiberg, K.Q. Tran
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2014-06-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/5703
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author Q.V. Bach
R. Khalil
O. Skreiberg
K.Q. Tran
author_facet Q.V. Bach
R. Khalil
O. Skreiberg
K.Q. Tran
author_sort Q.V. Bach
collection DOAJ
description Torrefaction kinetics of Norwegian biomass fuels, including spruce (softwood) and birch (hardwood) was studied using a thermogravimetric analyser. Small samples of approximately 10 mg and particle size of 63-125 µm were heated at a constant heating rate of 5 °C/min and kept afterwards for 4 hours in isothermal conditions at different temperatures (230, 240, 250, 260, 270 and 280 °C). A two-step kinetic model was employed to simulate the recorded mass loss curves. The results showed that thedecomposition of the initial biomass in the first step, to form an intermediate solid and volatiles, exhibited a higher conversion rate compared with the second step.
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spelling doaj.art-f730bc1f4f6140e4ae74e31f4c50a0452022-12-21T19:44:14ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162014-06-013710.3303/CET1437009Torrefaction Kinetics of Norwegian Biomass FuelsQ.V. BachR. KhalilO. SkreibergK.Q. TranTorrefaction kinetics of Norwegian biomass fuels, including spruce (softwood) and birch (hardwood) was studied using a thermogravimetric analyser. Small samples of approximately 10 mg and particle size of 63-125 µm were heated at a constant heating rate of 5 °C/min and kept afterwards for 4 hours in isothermal conditions at different temperatures (230, 240, 250, 260, 270 and 280 °C). A two-step kinetic model was employed to simulate the recorded mass loss curves. The results showed that thedecomposition of the initial biomass in the first step, to form an intermediate solid and volatiles, exhibited a higher conversion rate compared with the second step.https://www.cetjournal.it/index.php/cet/article/view/5703
spellingShingle Q.V. Bach
R. Khalil
O. Skreiberg
K.Q. Tran
Torrefaction Kinetics of Norwegian Biomass Fuels
Chemical Engineering Transactions
title Torrefaction Kinetics of Norwegian Biomass Fuels
title_full Torrefaction Kinetics of Norwegian Biomass Fuels
title_fullStr Torrefaction Kinetics of Norwegian Biomass Fuels
title_full_unstemmed Torrefaction Kinetics of Norwegian Biomass Fuels
title_short Torrefaction Kinetics of Norwegian Biomass Fuels
title_sort torrefaction kinetics of norwegian biomass fuels
url https://www.cetjournal.it/index.php/cet/article/view/5703
work_keys_str_mv AT qvbach torrefactionkineticsofnorwegianbiomassfuels
AT rkhalil torrefactionkineticsofnorwegianbiomassfuels
AT oskreiberg torrefactionkineticsofnorwegianbiomassfuels
AT kqtran torrefactionkineticsofnorwegianbiomassfuels