Fluidized Bed Technologies for Near-Zero Emission Combustion and Gasification 2013
DOI: 10.1533/9780857098801.4.931
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Calcium looping for CO 2 capture in combustion systems

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Cited by 6 publications
(5 citation statements)
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“…Recently, a SrO sorbent was investigated at high temperature in a thermobalance by Miccio et al, and its performance was compared with that of HA. However, SrO exhibited a decay of the sorption capability with repeated cycles of CO 2 uptake/release, similar to Ca-based sorbents …”
Section: Introductionmentioning
confidence: 78%
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“…Recently, a SrO sorbent was investigated at high temperature in a thermobalance by Miccio et al, and its performance was compared with that of HA. However, SrO exhibited a decay of the sorption capability with repeated cycles of CO 2 uptake/release, similar to Ca-based sorbents …”
Section: Introductionmentioning
confidence: 78%
“…2 Furthermore, the largest part of the CCS cost is attributed to the CO 2 uptake, accounting for 75% of the whole cost. 3 In the past decade, the calcium (Ca) loop 4 was proposed as an effective method for the capture of CO 2 at high temperature. It is based on a carbonation step of a Ca-based sorbent (e.g., calcined limestone), which is normally carried out at 700 °C, followed by a calcination step at higher temperature.…”
Section: Introductionmentioning
confidence: 99%
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“…Temperature is a crucial factor for both the gasification process and the carbonation reaction. Our previous research results indicated that a higher temperature could promote hydrogen production and reduce tars whereas 650 • C is a suitable temperature for CaO absorption reaction with CO 2 with the calcination reaction tending to be active above 900 • C [5,26]. Therefore, the temperature range was set as 700-800 • C. Regarding the CaO/C ratio, the stoichiometric molar ratio of carbonation reaction is 1 for CO 2 absorption reaction.…”
Section: Experimental Designmentioning
confidence: 99%