2013
DOI: 10.1002/cssc.201300178
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CaO‐Based CO2 Sorbents: From Fundamentals to the Development of New, Highly Effective Materials

Abstract: The enormous anthropogenic emission of the greenhouse gas CO2 is most likely the main reason for climate change. Considering the continuing and indeed growing utilisation of fossil fuels for electricity generation and transportation purposes, development and implementation of processes that avoid the associated emissions of CO2 are urgently needed. CO2 capture and storage, commonly termed CCS, would be a possible mid-term solution to reduce the emissions of CO2 into the atmosphere. However, the costs associate… Show more

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Cited by 315 publications
(284 citation statements)
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References 166 publications
(53 reference statements)
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“…However,C aO-based sorbents suffer from poor cyclic stabilityover multiple carbonation/calcination (i.e.,C O 2 capture andr egeneration) cycles,w hich is believed to stem from the severe sintering of CaCO 3 .T he Ta mmann temperature (T T )o fC aCO 3 ( % 533 8C) is significantly below the operating temperatures (i.e., % 650 8Cf or carbonation, and % 900 8Cf or regeneration) of the process. [4,5] To improve the CO 2 capture performance of limestone-derived sorbents, various methodsi ncluding hydration [6] and thermalt reatment [7] have been proposed.A lthough these approachesi mprovet he CO 2 uptake performance of limestonederived CaO, the materials still undergo as ignificant degree of deactivation with cycle number.A na lternative to enhance the cyclic stabilityo fC aO-based CO 2 sorbents relies on the incorporationo fs tabilizers with high T T ,s uch as the oxides of Al, Mg, Yo rZ r, intot he CaO framework. [5] The main purpose of the addition of ah igh-T T material is to increase the overall thermals tability of the sorbenta nd thus, minimize the sintering-induced loss of the CO 2 capturec apacity under the harsh operating conditions.…”
Section: Introductionmentioning
confidence: 99%
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“…However,C aO-based sorbents suffer from poor cyclic stabilityover multiple carbonation/calcination (i.e.,C O 2 capture andr egeneration) cycles,w hich is believed to stem from the severe sintering of CaCO 3 .T he Ta mmann temperature (T T )o fC aCO 3 ( % 533 8C) is significantly below the operating temperatures (i.e., % 650 8Cf or carbonation, and % 900 8Cf or regeneration) of the process. [4,5] To improve the CO 2 capture performance of limestone-derived sorbents, various methodsi ncluding hydration [6] and thermalt reatment [7] have been proposed.A lthough these approachesi mprovet he CO 2 uptake performance of limestonederived CaO, the materials still undergo as ignificant degree of deactivation with cycle number.A na lternative to enhance the cyclic stabilityo fC aO-based CO 2 sorbents relies on the incorporationo fs tabilizers with high T T ,s uch as the oxides of Al, Mg, Yo rZ r, intot he CaO framework. [5] The main purpose of the addition of ah igh-T T material is to increase the overall thermals tability of the sorbenta nd thus, minimize the sintering-induced loss of the CO 2 capturec apacity under the harsh operating conditions.…”
Section: Introductionmentioning
confidence: 99%
“…[4,5] To improve the CO 2 capture performance of limestone-derived sorbents, various methodsi ncluding hydration [6] and thermalt reatment [7] have been proposed.A lthough these approachesi mprovet he CO 2 uptake performance of limestonederived CaO, the materials still undergo as ignificant degree of deactivation with cycle number.A na lternative to enhance the cyclic stabilityo fC aO-based CO 2 sorbents relies on the incorporationo fs tabilizers with high T T ,s uch as the oxides of Al, Mg, Yo rZ r, intot he CaO framework. [5] The main purpose of the addition of ah igh-T T material is to increase the overall thermals tability of the sorbenta nd thus, minimize the sintering-induced loss of the CO 2 capturec apacity under the harsh operating conditions. However,t he stabilizers are typically inactive for CO 2 capture under the operating conditions of the process and reduce, thus, the maximal CO 2 uptake capacity of the material on aw eight basis.…”
Section: Introductionmentioning
confidence: 99%
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“…Thus, intensive research has been focused on the reactivation of CaO and the development of routes to obtain more stable CaO-based CO 2 sorbents. The development of methods and modified CaO precursors to mitigate the decay of capture capacity is desired to facilitate the scale-up of this technology (Arias, Grasa, Alonso, & Abanades, 2012;Kierzkowska, Pacciani, & M€ uller, 2013;Manovic & Anthony, 2008;Valverde, Sanchez-Jimenez, & Perez-Maqueda, 2014). Those techniques more widely presented in literature are steam reactivation (Arias, Grasa, & Abanades, 2010;Fennell, Davidson, Dennis, & Hayhurst, 2007;Hughes, Lu, Anthony, & Wu, 2004;Manovic & Anthony, 2007), preactivation (Blamey et al, 2010), selfreactivation effect (Manovic & Anthony, 2008), sorbent doping (Al-Jeboori, Nguyen, Dean, & Fennell, 2013), synthetic sorbents (Abanades et al, 2004;Blamey et al, 2010;Manovic & Anthony, 2008) and recarbonation (Arias et al, 2012;Valverde et al, 2014).…”
Section: Potential Energy Savings In Calmentioning
confidence: 98%
“…Cycling studies of natural limestone show its capacity to reduce by as much as 90 mol% aer only the rst 20 cycles owing to sintering. 5 While one focus of recent research has been to alter the properties of CaO through synthetic methods with different additives such as Al 3 O 3 , Ca 12 Al 14 O 33 , or SiO 2 , [6][7][8] there is still a fundamental lack of understanding regarding how the carbonation reaction proceeds and what parameters control the function of absorbent materials.…”
Section: Introductionmentioning
confidence: 99%