2015
DOI: 10.1016/j.fuel.2014.11.074
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Assessment of self-ignition risks of solid biofuels by thermal analysis

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Cited by 50 publications
(26 citation statements)
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“…These temperatures are essential to ensure the perfect design of the combustor and avoid unburned solid fuel at the outlet of the reactor [22]. It should be noted that T i is also used to compare the reactivity of several substances [19][20][21][22][23][42][43][44]. Several methods have been reported and used in the literature to determine T i and T f [32,[45][46][47][48].…”
Section: Ignition and Final Temperatures Of Combustion Reactionmentioning
confidence: 99%
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“…These temperatures are essential to ensure the perfect design of the combustor and avoid unburned solid fuel at the outlet of the reactor [22]. It should be noted that T i is also used to compare the reactivity of several substances [19][20][21][22][23][42][43][44]. Several methods have been reported and used in the literature to determine T i and T f [32,[45][46][47][48].…”
Section: Ignition and Final Temperatures Of Combustion Reactionmentioning
confidence: 99%
“…This temperature is a very important criterion for evaluating the reactivity of substances [19][20][21][22][23][42][43][44]. Indeed, the lower the T max , the higher the reactivity of the substance.…”
Section: Maximum Temperaturementioning
confidence: 99%
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“…In the case of the samples studied and due to their structural composition, two points of maximum mass loss, the resultant from the devolatilization of holocellulose (MLT_LV), and that corresponding to the devolatilization of lignin (MLT_HV) are obtained [80], as can be seen in Figure 15. As a general rule, when an oxygen stream is used instead of air stream, the reaction takes place quicker, and the sample has a peak mass-loss rate at a determined temperature called characteristic oxidation temperature (Tcharact), that is different for each sample ( Figure 16).…”
Section: Thermal Susceptibilitymentioning
confidence: 96%