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Product Layer Diffusion during the Reaction of Calcium Oxide with Carbon Dioxide
Abstract
The carbonation rate of 15−20 μm, nonporous, calcium oxide crystals has been studied over a temperature range of 550−1100 °C and a CO 2 pressure range of 1−11.7 atm. At temperatures greater than 600 °C, the carbonation rate decreases more rapidly with time than would be expected from diffusion through a uniform product layer and the activation energy is initially low but increases with conversion. The product layer consists of crystalline grains, and these product layer grains grow by coalescence from less than one μm diameter to the approximate dimension of the particle. The carbonation rate can be described by a model where CO 2 pressure-independent grain boundary diffusion and diffusion through the carbonate crystals act in parallel. The relative importance of bulk diffusion through the product layer crystals increases with time relative to transport through the grain boundaries and has an effective activation energy of 57 kcal/mol. Diffusion through the crystal boundaries has low activation energy and low dependence on CO 2 pressure. At temperatures greater than 900 °C and times greater than 600 min, bulk diffusion through the product layer becomes dominant and the rate approaches first order in CO 2 pressure.
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Cited by
Carbon dioxide sequestration in cement kiln dust through mineral carbonation
Huntzinger, D. N., Gierke, J. S., Kawatra, S. K., Eisele, T. C., & Sutter, L. L. (2009) · Environmental Science & Technology · doi:10.1021/es802910z · Cited by 442
Dean, C. C., Blamey, J., Florin, N. H., Al-Jeboori, M. J., & Fennell, P. S. (2011) · Chemical Engineering Research and Design · doi:10.1016/j.cherd.2010.10.013 · Cited by 375
Capture of CO2 from combustion gases in a fluidized bed of CaO
Abanades, J. C., Anthony, E. J., Lu, D. Y., Salvador, C., & Alvarez, D. (2004) · AIChE Journal · doi:10.1002/aic.10132 · Cited by 373
Performance Enhancement of Calcium Oxide Sorbents for Cyclic CO2 Capture—A Review
Liu, W., An, H., Qin, C., Yin, J., Wang, G., Feng, B., & Xu, M. (2012) · Energy & Fuels · doi:10.1021/ef300220x · Cited by 320
Elucidating the accelerated carbonation products of calcium silicates using multi-technique approach
Ashraf, W., & Olek, J. (2018) · Journal of CO2 Utilization · doi:10.1016/j.jcou.2017.11.003 · Cited by 224
An apparent kinetic model for the carbonation of calcium oxide by carbon dioxide
Lee, D. K. (2004) · Chemical Engineering Journal · doi:10.1016/j.cej.2003.12.003 · Cited by 214
Recent developments and consideration issues in solid adsorbents for CO2 capture from flue gas
Nie, L., Mu, Y., Jin, J., Chen, J., & Mi, J. (2018) · Chinese Journal of Chemical Engineering · doi:10.1016/j.cjche.2018.07.012 · Cited by 122
Metadata
- Authors
- Mess, D., Sarofim, A. F., & Longwell, J. P.
- Venue
- Energy & Fuels
- Publisher
- American Chemical Society (ACS)
- Published
- 1999-07-22
- Volume
- 13
- Issue
- 5
- Pages
- 999-1005
- ISSN
- 0887-0624 (ISSN-L)
- 1520-5029
- OpenAlex
- W2008422223
- Cited by
- 237
- References
- 0
- FWCI
- 1.74
- Type
- journal article
- Language
- en
- Open access
- closed
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