## AM-Interaction of carbon black and aqueous bromine involve8 conversion of the halogen into hydrobromic Acid a8 well a8 chemkorption or "iixation" by the carbon black. The amount converted varies with surface acidity of the black while the amount fixed varies with the amount of CO,-complex elimi
Chemistry of aqueous mineral carbonation for carbon sequestration and explanation of experimental results
β Scribed by Chen, Zhong-Ying ;O'Connor, William K. ;Gerdemann, S.J.
- Publisher
- American Institute of Chemical Engineers
- Year
- 2006
- Tongue
- English
- Weight
- 171 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0278-4491
- DOI
- 10.1002/ep.10127
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β¦ Synopsis
Abstract
In aqueous mineral carbonation for carbon sequestration, highβpressure CO~2~ is injected into water or sodium bicarbonate solution mixed with olivine or serpentine to produce magnesium carbonate. Thus, CO~2~ gas is fixed in a solid carbonate for sequestration. Such reactions are generally slow, and a significant amount of research was conducted to increase the reaction rate. This article is an initial effort using basic thermodynamic analysis to understand this complicated heterogeneous chemical process, and to explain some experimental results. The approach started with decomposing the process into two basic steps: magnesium ion dissolution from the olivine or serpentine, and magnesite precipitation. Thermodynamic calculation then is used to assess two important parameters for each of these two steps: the pH and carbonic ion concentration. The calculations explain the roles of increased CO~2~ pressure, elevated temperature, and adding sodium bicarbonate for enhancing the carbonation reaction, and these results agreed well with the experimental data. The analysis also indicates that for reaction routes in which leaching magnesium silicate and forming magnesium carbonate occur in the same reactor, lowering the pH helps dissolve magnesium ions from silicate, but it lowers carbonic ion concentration and limits precipitation of magnesite; careful balance of these two steps is critical. Further improvement may be built upon this model. Β© 2006 American Institute of Chemical Engineers Environ Prog, 2006
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