2010
DOI: 10.1016/j.fuel.2010.07.014
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Modelling of an updraft fixed-bed gasifier operated with softwood pellets

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Cited by 92 publications
(77 citation statements)
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“…For a fixed/packed bed reactor the final products yield of this reaction can be considered constant as reported in Table 1. Tar Page 6 of 30 is modelled as C 6 H 8 O , as in Mandl et al [27]. Furthermore, in our case, due to the extremely high temperature gradient at the bed entrance and concentrated energy flux, the pyrolysis is considered to be instantaneous (Flash-pyrolysis) [28][29][30].…”
Section: $mentioning
confidence: 99%
See 1 more Smart Citation
“…For a fixed/packed bed reactor the final products yield of this reaction can be considered constant as reported in Table 1. Tar Page 6 of 30 is modelled as C 6 H 8 O , as in Mandl et al [27]. Furthermore, in our case, due to the extremely high temperature gradient at the bed entrance and concentrated energy flux, the pyrolysis is considered to be instantaneous (Flash-pyrolysis) [28][29][30].…”
Section: $mentioning
confidence: 99%
“…Specific heating values (Cp i ) of the species were combined with sensible enthalpies to obtain a comprehensive formulation, as suggested in [36]. Only specific heat of tar and ashes were supposed to be constant and taken from the literature [27].…”
Section: Governing Equationsmentioning
confidence: 99%
“…The one step global reaction model is simpler which considers decomposition of biomass into char, gas and tar. This model neglects all the intermediate reactions but it can still predict the process very well as it has been reported by many researches Blasi and Branca (2013); Peters (2011); Mandl et al (2010).…”
Section: Introductionmentioning
confidence: 68%
“…However, in a gasification unit, drying, pyrolysis gasification and combustion all occur simultaneously [16]. Gasification is an endothermic process and the energy released from the combustion process is used to supply the energy required for gasification.…”
Section: Biomass Gasificationmentioning
confidence: 99%