CO2 capture from air and co-production of H2 via the Ca(OH)2–CaCO3 cycle using concentrated solar power–Thermodynamic analysis
V. Nikulshina,
D. Hirsch,
M. Mazzotti and
A. Steinfeld
Energy, 2006, vol. 31, issue 12, 1715-1725
Abstract:
The thermodynamics of a solar thermochemical cycle for the capture of CO2 from air are analyzed. The cycle encompasses 3 reactors: an aerosol-type carbonator for capturing CO2 from air using a spray of Ca(OH)2 aqueous solution, a solar calciner for thermally decomposing CaCO3 into CaO using concentrated solar energy, and a conventional slaker for regenerating Ca(OH)2. Two approaches are examined: (1) a closed-material cycle that delivers pure CO2; and (2) an open-material cycle that, additionally, co-produces hydrogen. The 2nd approach features the same components as those of the closed-material cycle, except that the calciner co-produces CaO and syngas by the combined CaCO3-decomposion and CH4-reforming processes, and syngas is further processed to separate streams of H2 and CO2. Its thermodynamic efficiency, defined as the ratio of ΔG298K∘|H2+0.5O2→H2O for the H2 produced to the thermal energy input (solar energy+heating value of CH4) is 22.7%. The solar chemical reactor technology for the calcination and for the combined calcination-reforming is presented.
Keywords: CO2 capture; Hydrogen; Carbonation; Calcination; Methane reforming (search for similar items in EconPapers)
Date: 2006
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Citations: View citations in EconPapers (14)
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Persistent link: https://EconPapers.repec.org/RePEc:eee:energy:v:31:y:2006:i:12:p:1715-1725
DOI: 10.1016/j.energy.2005.09.014
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