2016
DOI: 10.1016/j.ijggc.2016.04.002
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Review and research needs of Ca-Looping systems modelling for post-combustion CO2 capture applications

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Cited by 107 publications
(65 citation statements)
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“…Advanced hot solid looping technologies such as post-combustion calcium looping (CaL) (Martínez et al 2016) offer also interesting possibilities for CO 2 capture. In CaL, process calcium oxide is used for CO 2 capture.…”
Section: Co 2 Removal Methodsmentioning
confidence: 99%
“…Advanced hot solid looping technologies such as post-combustion calcium looping (CaL) (Martínez et al 2016) offer also interesting possibilities for CO 2 capture. In CaL, process calcium oxide is used for CO 2 capture.…”
Section: Co 2 Removal Methodsmentioning
confidence: 99%
“…In standard CaL systems, approximately 45-50% of the thermal input into the entire system (power plant and CaL) is introduced in the oxy-fired CFB calciner. 37 As can be seen in Fig. 3, the thermal input to the calciner can be drastically reduced by integrating the energy storage system.…”
Section: Papermentioning
confidence: 99%
“…Post-combustion CO 2 capture by CaL has developed rapidly in the last five years up to the scale of the MW th with several pilot plants [29][30][31][32][33][34][35] due to the similarity between its reactors and those of existing circulating fluidized bed power plants and the lower energy penalty compared to that of other CCS systems since extra power can be obtained from the additional heat input required to drive the sorbent regeneration reaction. 36,37 The use of CaO/CaCO 3 in CaL systems makes it possible to integrate a thermochemical energy storage system by taking advantage of the reversible reaction of CaO with CO 2 at high temperature. There is already background knowledge about the use of CaO/CaCO 3 to store nuclear 38,39 or solar energy [40][41][42] or to increase the flexibility of the integrated gasification combined cycle plants.…”
Section: Introductionmentioning
confidence: 99%
“…Different methods for supplying the energy needed for CaCO 3 calcination in the calciner reactor have been studied in the literature over the years, but none of them have been yet developed or proven on a sufficient scale for application. 4 However, the one having reached the largest development consists of operating the calciner under oxyfuel conditions, burning within the calciner additional fuel with pure O 2 as an oxidant. 5 CaO + CO 2 ↔ CaCO 3 ΔH 298 K = −178.8 kJ mol…”
Section: Introductionmentioning
confidence: 99%