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Experimental Validation of the Calcium Looping CO<sub>2</sub> Capture Process with Two Circulating Fluidized Bed Carbonator Reactors

173

Citations

28

References

2011

Year

Abstract

[EN] Postcombustion CO2 capture using CaO as a regenerable solid sorbent in a circulating fluidized bed&#13;\n(CFB) carbonator is emerging as a promising CO2 capture technology. Experimental validation of this&#13;\nconcept is provided through a comparative analysis of the results obtained in two laboratory-scale dual&#13;\nfluidized bed (DFB) installations located at INCAR-CSIC (Spain) and IFK (Germany). The analysis is focused on the performance of the CFB carbonator reactors operated with continuous solid circulation of&#13;\nCaO. A reasonable closure of the carbon balances (i) between the CO2 that has disappeared from the gas&#13;\nphase, (ii) the CaCO3 circulating between the reactors and (iii) the CaCO3 that is formed within the&#13;\ncarbonator bed has been established. A necessary condition for the capture of a given molar flow of CO2&#13;\nis experimentally demonstrated and requires that a slightly over-stoichiometric molar flow of active CaO&#13;\nis supplied to the carbonator. The deactivation behavior of the sorbents during continuous looping&#13;\nconditions has been measured. The key parameter to interpret the carbonator reactor results has been the&#13;\nactive space time, that is indicative of the CaO inventory per molar flow of CO2 participating in the&#13;\ncarbonation reaction and of the reaction rate of the solid inventory in the reactor. Two different&#13;\napproaches have been utilized in order to find a suitable expression for this parameter, thus achieving its&#13;\ncorrelation with the CO2 capture efficiency. A simple model assuming instant mixing of solids and plugflow&#13;\nof the gas has been tested. Based mainly on carbonator active space time variation, the CO2 capture&#13;\nefficiency are shown to lie between 30 % and above 90 %. These results confirm the technical viability&#13;\nof the calcium looping postcombustion CO2 capture process. They have been used for designing the&#13;\ncurrent pilot-plant facilities which are scaled up 20-50 times in regard to the lab-scale units. Moreover,&#13;\nthe lab-scale results obtained allow for simulation work to be initiated in regard to the full scale Ca looping application.

References

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