2007
DOI: 10.1016/j.cej.2006.11.003
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Kinetic analysis of the carbonation reactions for the capture of CO2 from air via the Ca(OH)2–CaCO3–CaO solar thermochemical cycle

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Cited by 186 publications
(132 citation statements)
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“…The results obtained from direct gas-solid carbonation of natural alkaline oxides, such as MgO and CaO, provide the basis for applying this route to the carbonation of alkaline residues, since such materials are largely composed of calcium and magnesium oxides or hydroxides. Nikulshina et al [15] investigated CaO and Ca(OH) 2 carbonation, observing that the addition of water vapor significantly enhances the reaction kinetics to the extent that, in the first 20 min, the reaction proceeds at a rate that is 22 and 9 times faster than that observed for the dry carbonation of CaO and Ca(OH) 2 . The first study dealing with direct gas/solid carbonation of alkaline residues was by Jia and Anthony [16], who performed pressurized TGA experiments of hydrated and non-hydrated fluidized bed combustion ash, achieving CaO conversion efficiencies up to 60% when operative at temperatures above 400 • C and in a 100% CO 2 atmosphere.…”
Section: Introductionmentioning
confidence: 99%
“…The results obtained from direct gas-solid carbonation of natural alkaline oxides, such as MgO and CaO, provide the basis for applying this route to the carbonation of alkaline residues, since such materials are largely composed of calcium and magnesium oxides or hydroxides. Nikulshina et al [15] investigated CaO and Ca(OH) 2 carbonation, observing that the addition of water vapor significantly enhances the reaction kinetics to the extent that, in the first 20 min, the reaction proceeds at a rate that is 22 and 9 times faster than that observed for the dry carbonation of CaO and Ca(OH) 2 . The first study dealing with direct gas/solid carbonation of alkaline residues was by Jia and Anthony [16], who performed pressurized TGA experiments of hydrated and non-hydrated fluidized bed combustion ash, achieving CaO conversion efficiencies up to 60% when operative at temperatures above 400 • C and in a 100% CO 2 atmosphere.…”
Section: Introductionmentioning
confidence: 99%
“…A summary of rate equations for the carbonation reaction is shown in Table 2. Nikulshina et al (2007) conducted a thermogravimetric (TG) analysis of the carbonation of CaO and Ca(OH) 2 using atmospheric levels of CO 2 . The CaO carbonation reaction rate was chemically controlled initially and switched to a diffusion controlled regime after 20 minutes due to formation of a CaCO 3 product layer.…”
Section: Carbonation Kineticsmentioning
confidence: 99%
“…7. A wide variety of synthetic sorbents designed to reduce degradation over multiple cycles have been studied recently, including calcium aluminate supported CaO (Manovic and Anthony, Acharya et al (2012) (1 ) (Nikulshina et al, 2007). Reproduced with permission from Elsevier.…”
Section: Sorbent Degradationmentioning
confidence: 99%
“…This improved rate of reaction with the addition of steam appears to enable CO 2 to penetrate further into the pellet, concurring with similar observations seen previously in the literature. [29][30][31] However, it may also be an effect of changing porosity linked to the formation of Ca(OH) 2 (especially additional porosity that is formed upon heating the hydroxide phase), especially considering the total extent of carbonation appears unchanged as compared to the pure CO 2 experiments. …”
Section: Inuence Of Steam On Carbonation Observed By In Situ Xrdmentioning
confidence: 99%