“…XRD analysis (see Figure 1.a) confirmed that no carbonates were present in the crystalline phase of the SSA samples obtained at incineration temperatures above 650 °C. Several authors found that the release of alkali and alkaline earth metals (specifically Ca, K, Mg and Na) from biomass fuels in general increases with increasing incineration temperature [34][35][36][37]. Yet, in this work, the Ca, K, Mg and Na concentration in the SSA remained relatively constant with increasing incineration temperature (5.45 -5.76% of DM, 1.94 -2.02% of DM, 1.24 -1.32% of DM and 0.34 -0.39% of DM for a temperature increase from 550 to 1100 °C, respectively).…”
Section: Ssa Characterizationmentioning
confidence: 99%
“…Yet, in this work, the Ca, K, Mg and Na concentration in the SSA remained relatively constant with increasing incineration temperature (5.45 -5.76% of DM, 1.94 -2.02% of DM, 1.24 -1.32% of DM and 0.34 -0.39% of DM for a temperature increase from 550 to 1100 °C, respectively). This is related to the high concentration of Si in the SS and hence also in the SSA (18.79 -19.58% of DM), retaining Ca, K, Mg and Na in the silicate fraction [34][35][36][37]. XRD analysis (see Figure 1.d) indeed showed that these alkali and alkaline earth metals are bound in the silicate fraction as diopside (CaMgSi2O6), microcline (KAlSi3O8), muscovite (KAl3Si3O10(OH,F)2), plagioclase ((Na,Ca)(Si,Al)4O8) and smectite-related minerals (e.g., (Na,Ca)0.3(Al,Mg)2Si4O10(OH)2.xH2O), all having high boiling points.…”
Section: Ssa Characterizationmentioning
confidence: 99%
“…Between 550 and 650 °C, there was a decrease in the amount of amorphous fraction, after which it remained more or less constant between 650 and 900 °C. At temperatures above 900 °C, the amount of amorphous fraction started to increase again since higher incineration temperatures imply more glassy SSA due to agglomeration caused by silicate melting [37,[48][49][50][51]. Unfortunately, the mineralogy of the heavy metals could not be detected by XRD analysis because of their low concentrations in the SSA samples [45,46].…”
“…XRD analysis (see Figure 1.a) confirmed that no carbonates were present in the crystalline phase of the SSA samples obtained at incineration temperatures above 650 °C. Several authors found that the release of alkali and alkaline earth metals (specifically Ca, K, Mg and Na) from biomass fuels in general increases with increasing incineration temperature [34][35][36][37]. Yet, in this work, the Ca, K, Mg and Na concentration in the SSA remained relatively constant with increasing incineration temperature (5.45 -5.76% of DM, 1.94 -2.02% of DM, 1.24 -1.32% of DM and 0.34 -0.39% of DM for a temperature increase from 550 to 1100 °C, respectively).…”
Section: Ssa Characterizationmentioning
confidence: 99%
“…Yet, in this work, the Ca, K, Mg and Na concentration in the SSA remained relatively constant with increasing incineration temperature (5.45 -5.76% of DM, 1.94 -2.02% of DM, 1.24 -1.32% of DM and 0.34 -0.39% of DM for a temperature increase from 550 to 1100 °C, respectively). This is related to the high concentration of Si in the SS and hence also in the SSA (18.79 -19.58% of DM), retaining Ca, K, Mg and Na in the silicate fraction [34][35][36][37]. XRD analysis (see Figure 1.d) indeed showed that these alkali and alkaline earth metals are bound in the silicate fraction as diopside (CaMgSi2O6), microcline (KAlSi3O8), muscovite (KAl3Si3O10(OH,F)2), plagioclase ((Na,Ca)(Si,Al)4O8) and smectite-related minerals (e.g., (Na,Ca)0.3(Al,Mg)2Si4O10(OH)2.xH2O), all having high boiling points.…”
Section: Ssa Characterizationmentioning
confidence: 99%
“…Between 550 and 650 °C, there was a decrease in the amount of amorphous fraction, after which it remained more or less constant between 650 and 900 °C. At temperatures above 900 °C, the amount of amorphous fraction started to increase again since higher incineration temperatures imply more glassy SSA due to agglomeration caused by silicate melting [37,[48][49][50][51]. Unfortunately, the mineralogy of the heavy metals could not be detected by XRD analysis because of their low concentrations in the SSA samples [45,46].…”
“…Three-dimensional diffusion E α and A estimates gained by the above two kinetic approaches are employed to compute the changes in enthalpy (∆H), Gibbs free energy (∆G), and entropy (∆S), expressed as [44]:…”
Section: Coats-redfern Approachmentioning
confidence: 99%
“…The values of the changes in enthalpy (∆H), Gibbs free energy (∆G), and entropy (∆S) of hardwood and softwood in region 1 were estimated from the thermogravimetric data at the heating rate of 15 K/min, as listed in Table 7. The difference between E and ∆H represents the potential energy barrier in the process of biomass combustion [44]. The smaller the potential energy barrier, the easier the reactants transform into products.…”
In order to utilize woody biomass effectively for bioenergy and chemical feedstocks, the comparative thermal degradation behaviors and kinetic mechanisms of typical hardwood (beech wood) and softwood (camphorwood) were studied at various heating rates in air. The Kissinger-Akahira-Sunose approach combined with the Coats-Redfern approach was employed to estimate the kinetic triplet. Softwood degradation began and ended at lower temperatures than hardwood. Compared with softwood, the maximal reaction rate of hardwood was greater and occurred in the higher temperature region. Two decomposition regions were determined by the variation of activation energy, and the dividing point was α = 0.6 and α = 0.65 for hardwood and softwood, respectively. Moreover, the average activation energy of hardwood was larger than that of softwood during the whole decomposition process. The thermal degradation process occurring in region 1 was dominated by the Avrami-Erofeev and 3D diffusion models for hardwood and softwood, respectively. Furthermore, the kinetic modeling results showed good consistency between the experimental and simulated curves under 5, 15, 20, and 40 K/min. It is noted that the thermogravimetric experimental profile under 20 K/min was not used for estimating the kinetic triplet. Besides, the combustion performance of hardwood is superior to softwood under the same external conditions (heating rate and atmosphere).
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