2012
DOI: 10.1016/j.ijggc.2011.11.006
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High-temperature CO2 capture cycles for CaO-based pellets with kaolin-based binders

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Cited by 71 publications
(52 citation statements)
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“…carbonation temperature for steel slag was 600 8C in this study, which was clearly higher than the optimal temperature for air pollution control system residues (400-500 8C) [27,30,31] but close to the optimal temperature for limestone or other CaO-based adsorbents (600-700 8C). [29,38,39] The influence of CO 2 concentration (Figure 3) and the presence of SO 2 ( Figure 4) on the carbonation conversion of steel slag was not as strong as that of temperature. As shown in Figure 3, all sequestration curves were similar over a reaction time of 1 h; the curve representing the carbonation between steel slag and 100 % CO 2 was slightly higher than the other three, and the uptake of CO 2 gradually increased as the CO 2 concentration increased in the simulated flue gases.…”
Section: Evaluation Of the Carbonation Potentialmentioning
confidence: 97%
“…carbonation temperature for steel slag was 600 8C in this study, which was clearly higher than the optimal temperature for air pollution control system residues (400-500 8C) [27,30,31] but close to the optimal temperature for limestone or other CaO-based adsorbents (600-700 8C). [29,38,39] The influence of CO 2 concentration (Figure 3) and the presence of SO 2 ( Figure 4) on the carbonation conversion of steel slag was not as strong as that of temperature. As shown in Figure 3, all sequestration curves were similar over a reaction time of 1 h; the curve representing the carbonation between steel slag and 100 % CO 2 was slightly higher than the other three, and the uptake of CO 2 gradually increased as the CO 2 concentration increased in the simulated flue gases.…”
Section: Evaluation Of the Carbonation Potentialmentioning
confidence: 97%
“…Maintaining a high make-up flow to replace the spent sorbents and elutriated materials has been found to negatively influence the economics of the process [12]. As a result, there have been extensive research efforts to improve the reactivity of the sorbent by chemical doping [10,[13][14][15], organic acid treatment [16][17][18][19], and hydration [20]. In some cases of doping CaO-based material with metals, doped sorbents exhibited low performance, even inferior to that of the undoped material, such as in the case of doping CaO with the alkali metal lithium [13].…”
Section: Introductionmentioning
confidence: 99%
“…However, these modification techniques risk being cost-ineffective due to the relatively high cost of chemicals and treatment procedures and require further development [22,23]. Pelletization still allows the possibility of sorbent doping but has also been proposed to improve the mechanical strength of the sorbent using different binders, such as bentonites [24], kaolin [25], alumina [25], and calcium aluminate cement [19,26].…”
Section: Introductionmentioning
confidence: 99%
“…The sorbent stability can be significantly enhanced by incorporating suitable inert particles into CaO, yielding well-distributed oxides within the calcium oxides. Impregnating CaO with an inert particle helps to avoid the deterioration of the spent sorbent, for example, of CaO/ SiO 2 [10], Ca/Al-oxide [11], Zr/Ca complex [12], limestone/kaolin [13], CaO/aluminate cement [14], and extruded particles of Ca(OH) 2 /cement [15].…”
Section: Introductionmentioning
confidence: 99%