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CO2 Capture Capacity of CaO in Long Series of Carbonation/Calcination Cycles
Abstract
Calcium oxide can be an effective sorbent to separate CO 2 at high temperatures. When coupled with a calcination step to produce pure CO 2, the carbonation reaction is the basis for several high-temperature CO 2 capture systems. The evolution with cycling of the capture capacity of CaO derived from natural limestones is experimentally investigated in this work. Long series of carbonation/calcination cycles (up to 500) varying different variables affecting sorbent capacity have been tested in a thermogravimetric apparatus. Calcination temperatures above T > 950 °C and very long calcination times accelerate the decay in sorption capacity, while other variables have a comparatively modest effect on the overall sorbent performance. A residual conversion of about 7−8% that remains constant after many hundreds of cycles and that seems insensitive to process conditions has been found. This residual conversion makes very attractive the carbonation/calcination cycle, by reducing (or even eliminating) sorbent purge rates in the system. A semiempirical equation has been proposed to describe sorbent conversion with the number of cycles based on these new long data series.
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Metadata
- Authors
- Grasa, G. S., & Abanades, J. C.
- Venue
- Industrial & Engineering Chemistry Research
- Publisher
- American Chemical Society (ACS)
- Published
- 2006-11-09
- Volume
- 45
- Issue
- 26
- Pages
- 8846-8851
- ISSN
- 0888-5885 (ISSN-L)
- 1520-5045
- OpenAlex
- W1999180312
- Cited by
- 757
- References
- 0
- FWCI
- 60.30
- Type
- journal article
- Language
- en
- Open access
- closed
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