Greeshma GadikotaA commentary on
Ex Situ Aqueous Mineral Carbonation
by Gerdemann, S. J., O’Connor, W. K., Dahlin, D. C., Penner, L. R., and Rush, H. (2007). Environ. Sci. Technol. 41, 2587–2593. doi: 10.1021/es0619253
CO2 conversion to calcium and magnesium carbonates has garnered considerable attention since it is a thermodynamically downhill pathway to safely and permanently sequester large quantities of CO2. This seminal work performed at The National Energy Technology Laboratory in Albany (NETL-Albany) reports the conversion of calcium- and magnesium-bearing silicate minerals, such as olivine [(Mg, Fe)2SiO4], wollastonite (CaSiO3), and serpentine [Mg3Si2O5(OH)4], as they are reacted with CO2 in an aqueous environment to form magnesium or calcium carbonates. This paper discusses various pretreatment methods of the starting materials, such as grinding or heat treatment of hydroxylated Mg silicates, to enhance the reaction kinetics. The effects of various chemical additives (e.g., NaCl and NaHCO3), and reaction parameters, such as temperature, pressure, and reaction time, on the conversion are investigated. Feasibility assessments and energy and economic analyses of the direct carbonation of calcium- and magnesium-bearing minerals are presented.
The key contributions of this study are the identification of the optimal conditions for the carbonation of olivine (185°C, , 1.0M·NaCl + 0.64M·NaHCO3), wollastonite (100°C, , distilled water), and heat-treated serpentine (155°C, , 1.0M·NaCl + 0.64M·NaHCO3). High extents of carbonation of 49.5, 81.8, and 73.5% of olivine, wollastonite, and heat-treated serpentine, respectively, achieved within an hour of reacting with CO2 in an aqueous environment are reported. The identification of the optimal reaction conditions to achieve the rapid conversion of calcium- and magnesium-bearing silicate minerals to carbonates has spurred a significant global scientific interest in mineral carbonation as a promising technology for CO2 conversion and storage with the potential reuse of carbonates.
In particular, this work has found unique relevance for ex situ and in situ carbon mineralization. In ex situ mineral carbonation, CO2 is converted to carbonates in engineered processes where there is considerable control over the reaction conditions. In in situ mineral carbonation, CO2 is injected into geological formations containing calcium- and magnesium-bearing minerals and rocks with the aim toward natural carbon mineralization over time. Predicting the fate of CO2 injected into geological formations containing these rocks and minerals and developing chemical processes for converting CO2 to carbonates require a fundamental understanding of the kinetics of mineral carbonation and the corresponding morphological changes in materials. Thus, more recent studies have focused on understanding the carbon mineralization behavior via direct carbonation (Bonfils et al., 2012; Gadikota et al., 2014a; Eikeland et al., 2015) and indirect carbonation, which involves the dissolution of minerals (Park et al., 2003; Park and Fan, 2004; Hänchen et al., 2006; Prigiobbe et al., 2009; Gadikota et al., 2014b), formation of carbonates (Ferrini et al., 2009; Saldi et al., 2009, 2012; Cheng and Li, 2010; Bénézeth et al., 2011; Zhao et al., 2013; Fricker and Park, 2014; Swanson et al., 2014), and the corresponding morphological changes in materials (Hövelmann et al., 2012; Olsson et al., 2012; Gadikota et al., 2014a). The effects of sodium and ammonium salts and Si-, Mg-, and Ca-targeting chelating agents on enhancing mineral carbonation behavior has been investigated (Bonfils et al., 2012; Highfield et al., 2012; Declercq et al., 2013; Zhao et al., 2013; Gadikota et al., 2014a,b; Ghoorah et al., 2014).
These studies have formed the basis for understanding CO2 interactions with calcium and magnesium silicates that extend beyond the laboratory to the demonstration scale (Reddy et al., 2010; Kelly et al., 2011; Zevenhoven et al., 2011; Hitch and Dipple, 2012; Brent, 2015) and toward geological carbon storage (Kelemen and Matter, 2008; Matter and Kelemen, 2009; Schaef and McGrail, 2009; Gislason et al., 2010; Rosenbauer et al., 2012). The studies performed at NETL-Albany have also been extensively cited in studies for the accelerated carbonation of industrial alkaline wastes [Pan et al. (2012), Gadikota and Park (2014), Sanna et al. (2012), and references contained therein]. These materials are often fine, highly reactive, and have a high Ca and Mg content. Examples of these materials include coal fly ash, steel and stainless steel slags, cement and lime kiln dusts, and red mud. However, the availability of industrial alkaline wastes is much smaller compared to calcium- and magnesium-bearing silicate minerals. The global CO2 storage potential of industrial alkaline wastes is about 200–300 Mt of CO2 per year, while calcium- and magnesium-bearing silicates can store carbon to the order of thousands of Gt (Sanna et al., 2012). Regardless, the integration of carbon mineralization technologies with these carbon-intensive industries reduces the CO2 footprint, the alkalinity of the wastes, and could lead to the potential reuse of the carbonated materials as building, construction, or filler materials. Further development of carbon mineralization technologies requires a fundamental understanding of the formation of mass transfer limiting layers containing Si and Fe (Béarat et al., 2006; King et al., 2010; Daval et al., 2011; Saldi et al., 2013, 2015; Sissmann et al., 2013; Harrison et al., 2015), linkages between the morphology with the chemistry (Hövelmann et al., 2012; Olsson et al., 2012; Gadikota et al., 2014a; Eikeland et al., 2015), and the impact of impurities in the gas streams (e.g., SO2) on the conversion of CO2 to carbonates (Liu et al., 2010; Zevenhoven et al., 2014). While these findings are in the context of ex situ mineral carbonation, they are of relevance to in situ conversion of CO2 to carbonates.
When CO2 is directly injected into geological reservoirs with calcium- and magnesium-bearing silicates, carbonate formation is aided by the geothermal gradient, which provides reaction temperatures in excess of 80°C, available post-combustion and compression, and the presence of ground water. These conditions are analogous to the reaction conditions identified in this study. Of particular interest are the Oman peridotite (olivine-rich rock) (Kelemen and Matter, 2008; Matter and Kelemen, 2009) and the basalts in Iceland and Columbia River in the United States (Matter et al., 2009; McGrail et al., 2011). The chemomechanical effects due to extensive carbonate growth may induce microfractures, which in turn impact the permeability, fluid flow, and further reactivity of the rock (Kelemen et al., 2013). Regardless, the permanent in situ conversion of CO2 to carbonates reduces the need to monitor mobile CO2 over time.
While the experimental methodologies developed by the researchers at NETL-Albany have laid the foundation for a number of studies in this field, considerable uncertainties in the energy requirements for mineral carbonation exist. These uncertainties are attributed to some key parameters, such as the availability and cost of the feedstock, preprocessing of the materials, such as crushing and grinding, the conversion routes, and the use of heat vs. electricity. Regardless, the work performed at NETL-Albany has highlighted the need for a multi-scale understanding of the kinetics, mass transfer behaviors, competing reactions, and microstructural and chemical changes in heterogeneous materials, when reacted with CO2. These insights can be used to tune the reactivity and morphology of the carbonated end-materials. Ultimately, a fundamental understanding of CO2–reaction fluid–mineral/rock interactions is essential for developing large-scale chemical processes for converting CO2 to carbonates, and for predicting the fate of CO2 injected into geological formations containing calcium and magnesium silicate minerals and rocks.
Author Contributions
The author confirms being the sole contributor of this work and approved it for publication.
Conflict of Interest Statement
The author declares that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
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Keywords: mineral carbonation, carbon mineralization, CO2 conversion, utilization and storage, magnesium and calcium silicates, magnesium and calcium carbonates, alkaline industrial wastes
Citation: Gadikota G (2016) Commentary: Ex Situ Aqueous Mineral Carbonation. Front. Energy Res. 4:21. doi: 10.3389/fenrg.2016.00021
Received: 18 March 2016; Accepted: 12 May 2016;
Published: 26 May 2016
Edited by:
Peter Styring, The University of Sheffield, UKReviewed by:
Ron Zevenhoven, Åbo Akademi University, FinlandCopyright: © 2016 Gadikota. This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) or licensor are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
*Correspondence: Greeshma Gadikota, gadikota@princeton.edu