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Parameters optimization for direct flue gas CO sub(2) capture and sequestration by aqueous mineral carbonation using activated serpentinite based mining residue

Naturally occurring mineral carbonation can significantly reduce GHG emissions. Adapting the reaction in order to sequester post combustion CO sub(2) is a potential industrial mitigation pathway, but such a process must be chemically and economically efficient. Research to date has focused on reacti...

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Bibliographic Details
Published in:Applied geochemistry 2014-11, Vol.50, p.66-73
Main Authors: Pasquier, Louis-Cesar, Mercier, Guy, Blais, Jean-Francois, Cecchi, Emmanuelle, Kentish, Sandra
Format: Article
Language:English
Online Access:Get full text
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Summary:Naturally occurring mineral carbonation can significantly reduce GHG emissions. Adapting the reaction in order to sequester post combustion CO sub(2) is a potential industrial mitigation pathway, but such a process must be chemically and economically efficient. Research to date has focused on reacting a concentrated CO sub(2) stream with alkaline rocks. Significant carbonation rates where reached but required a system operating at high pressure and temperature. This article describes the parameter optimization for direct flue gas CO sub(2) capture and sequestration when using finely-ground, heat-activated serpentine derived from mining residues. The gas is contacted with the minerals in an aqueous phase at ambient temperature and moderate pressure (10.5 bar). Once the solution is saturated with dissolved CO sub(2) and Mg, it is filtered and carbonates precipitated in a downstream operation. The solid is mixed with fresh water and recirculated to treat more gas until no further Mg can be leached from the solid media. Reaction parameters such as the pulp density, the volumetric ratio of gas to liquid, the reaction time and the particle size were investigated with a 18.2% CO sub(2) gas stream in a batch mode. This innovative approach permits the use of moderate temperature and pressure conditions and the production of pure MgCO sub(3) with a potential sale value. After parameter optimization, batch mode tests showed that 64 wt.% of the Mg could be leached from the solid and that 62.5 wt.% of the CO sub(2) removed from the gas phase giving a ratio of 0.28 kg of CO sub(2) sequestered per kg of residues.
ISSN:0883-2927
DOI:10.1016/j.apgeochem.2014.08.008