Proceedings of the 20th International Conference on Fluidized Bed Combustion 2009
DOI: 10.1007/978-3-642-02682-9_88
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Parametric Study on the CO2 Capture Efficiency of The Carbonate Looping Process in a 10 kW Dual Fluidized Bed

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Cited by 15 publications
(10 citation statements)
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“…A parametric study has been performed on the apparatus with the riser used as the calciner and BFB as the carbonator and a CO 2 capture efficiency of > 90 % was reported. The CO 2 capture efficiency was found to decrease with decreasing CaO looping ratio (CaO looping rate between beds / CO 2 flow to carbonator) and space time (number of moles of CaO in carbonator / CO 2 flow to carbonator) (Charitos et al, 2009). …”
Section: Stuttgartmentioning
confidence: 95%
“…A parametric study has been performed on the apparatus with the riser used as the calciner and BFB as the carbonator and a CO 2 capture efficiency of > 90 % was reported. The CO 2 capture efficiency was found to decrease with decreasing CaO looping ratio (CaO looping rate between beds / CO 2 flow to carbonator) and space time (number of moles of CaO in carbonator / CO 2 flow to carbonator) (Charitos et al, 2009). …”
Section: Stuttgartmentioning
confidence: 95%
“…More than 600 h of operation were accumulated, including experiments with simultaneous combustion of biomass in the carbonator, allowing for 'in situ' CO 2 capture with capture efficiencies consistently over 80%. Charitos et al (2009Charitos et al ( , 2010 from IFK in Stuttgart reported experimental results operating a much taller (12.4 m) circulating fluidized bed carbonator interconnected with a bubbling fluidized bed calciner (see Fig. 21.9), achieving for the first time capture rates close to those expected in large-scale commercial systems (up to 10 mol/m 2 s).…”
Section: Results From Experiments In Laboratory-scale Pilot Reactors mentioning
confidence: 72%
“…A similar version of this model was used by Rodríguez et al (2011a), and Alonso et al (2010Alonso et al ( , 2011c to analyse the experimental results from a 30 kW th pilot post-combustion CaL facility, including data from tests with simultaneous combustion of biomass and CO 2 capture by CaO (Alonso et al, 2011c). similar model approaches have also been used by Charitos et al (2009Charitos et al ( , 2010 to interpret results from a 10 kW scale pilot facility. More recently, both groups using a common approach (Charitos et al, 2011) have jointly interpreted their experimental results from CFb carbonators operating in continuous mode.…”
Section: Fluidized Bed Model Of the Carbonator Reactormentioning
confidence: 96%
“…Their inherent ability to thoroughly address complicated issues such as inert material concentration in bed, fuel mixing efficiency and temperature distribution makes them a very powerful tool for this scope. Moreover, advanced CFD modeling can accommodate the optimization of new processes such as CaO looping (Charitos et al, 2009(Charitos et al, , 2010, providing an in depth understanding of the governing hydrodynamics of such novel CFB reactors.…”
Section: Introductionmentioning
confidence: 99%