Biomass torrefaction: Modeling of reaction thermochemistry

Based on the evolution of volatile and solid products predicted by a previous model for willow torrefaction (Bates and Ghoniem, 2012) a thermochemical model has been developed to describe their thermal, chemical, and physical properties as well as the rates of heat release. The first stage of torref...

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Bibliographic Details
Main Authors: Bates, Richard B (Contributor), Ghoniem, Ahmed F (Contributor)
Other Authors: Massachusetts Institute of Technology. Department of Mechanical Engineering (Contributor)
Format: Article
Language:English
Published: Elsevier, 2016-11-21T22:01:05Z.
Subjects:
Online Access:Get fulltext
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100 1 0 |a Bates, Richard B  |e author 
100 1 0 |a Massachusetts Institute of Technology. Department of Mechanical Engineering  |e contributor 
100 1 0 |a Bates, Richard B  |e contributor 
100 1 0 |a Ghoniem, Ahmed F  |e contributor 
700 1 0 |a Ghoniem, Ahmed F  |e author 
245 0 0 |a Biomass torrefaction: Modeling of reaction thermochemistry 
260 |b Elsevier,   |c 2016-11-21T22:01:05Z. 
856 |z Get fulltext  |u http://hdl.handle.net/1721.1/105394 
520 |a Based on the evolution of volatile and solid products predicted by a previous model for willow torrefaction (Bates and Ghoniem, 2012) a thermochemical model has been developed to describe their thermal, chemical, and physical properties as well as the rates of heat release. The first stage of torrefaction, associated with hemicellulose decomposition, is exothermic releasing between 40 and 280 kJ/kginitial. The second stage is associated with the decomposition of the remaining lignocellulosic components, completes over a longer period, and is predicted to be either endothermic or exothermic depending on the temperature and assumed solid properties. Cumulative heat release increases with the degree of torrefaction quantified by the mass loss. The rate of mass loss and rate of heat release increase with higher temperatures. The higher heating value of volatiles produced during torrefaction was estimated to be between 4.4 and 16 MJ/kg increasing with the level of mass loss. 
520 |a BP (Firm) 
546 |a en_US 
655 7 |a Article 
773 |t Bioresource Technology