2011
DOI: 10.1016/j.cherd.2010.10.013
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The calcium looping cycle for CO2 capture from power generation, cement manufacture and hydrogen production

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Cited by 326 publications
(227 citation statements)
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“…This will fix the activity of CaO at unity early in the experiments and so lead to a low partial pressure of CO 2 to be established in the system. The combined, total reaction occurring with CaO and MF/CaF2 (M = Li or Na) as the active substances is described by equation (3). The Gibbs free energies for the combined reaction for the different alkali-earth metal elements are plotted in Figure 1B.…”
Section: Resultsmentioning
confidence: 99%
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“…This will fix the activity of CaO at unity early in the experiments and so lead to a low partial pressure of CO 2 to be established in the system. The combined, total reaction occurring with CaO and MF/CaF2 (M = Li or Na) as the active substances is described by equation (3). The Gibbs free energies for the combined reaction for the different alkali-earth metal elements are plotted in Figure 1B.…”
Section: Resultsmentioning
confidence: 99%
“…In this work, up to 20% CaO in CaCl 2 has been used while the solubility of CaO in CaCl 2 at 800°C is 6% [19]. At 74.2% carbonation, this is equivalent to an uptake capacity of CO 2 of 0.105 g/g liquid if 90% CaCO 3 to Ca conversion as recorded with this composition is assumed. This is similar to numbers recently reported for synthetic, stable sorbents in Ca-looping where CaO is present as nanostructures on a solid, inert carrier [21].…”
Section: Resultsmentioning
confidence: 99%
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“…capture efficiencies while minimizing the make-up flow of sorbent. Unless there is a strong synergy with a cement producer (which would also impose limits on the composition of the purge material used), low limestone consumption is always an economic advantage [46][47]. F 0 can be reduced when using high-quality coals and/or when the sorbent is reactivated.…”
Section: Gas Streamsmentioning
confidence: 99%