2011
DOI: 10.1016/j.cherd.2010.11.010
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Combustion modelling opportunities and challenges for oxy-coal carbon capture technology

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Cited by 163 publications
(88 citation statements)
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References 175 publications
(211 reference statements)
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“…Previous studies [27,28] found that the exchange of N 2 for CO 2 in oxyfuel combustion does not have much influence on devolatilisation. It was thus deemed su cient for the purpose of this study to represent the devolatilisation of the volatile gases from the coal particle using the single-step reaction rate model [29], which assumes a single reaction for the total weight loss of the volatiles:…”
Section: Coal Combustion Modelmentioning
confidence: 99%
“…Previous studies [27,28] found that the exchange of N 2 for CO 2 in oxyfuel combustion does not have much influence on devolatilisation. It was thus deemed su cient for the purpose of this study to represent the devolatilisation of the volatile gases from the coal particle using the single-step reaction rate model [29], which assumes a single reaction for the total weight loss of the volatiles:…”
Section: Coal Combustion Modelmentioning
confidence: 99%
“…Combustion processes modeled using the EDM are mixing-limited, thus the complex chemical kinetic rates can be neglected [37,38]. The particle combustion process, where heterogenous reaction occurred was divided into several submodels shown in Table 6.…”
Section: Modeling Oxy-fuel Combustionmentioning
confidence: 99%
“…Either a constant approximation [10] or simplified empirical expressions [11] are used for the gas emissivity and equivalent radiating gas temperature. For oxyfuel combustion, these approaches need to be reconsidered due to the fundamental changes in gas properties [12]. This can be done by incorporating a detailed CFD model of the boiler within a full plant process model.…”
Section: Introductionmentioning
confidence: 99%