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<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Energy Res.</journal-id>
<journal-title-group>
<journal-title>Frontiers in Energy Research</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Energy Res.</abbrev-journal-title>
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<issn pub-type="epub">2296-598X</issn>
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<publisher-name>Frontiers Media S.A.</publisher-name>
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<article-id pub-id-type="publisher-id">1771825</article-id>
<article-id pub-id-type="doi">10.3389/fenrg.2026.1771825</article-id>
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<article-categories>
<subj-group subj-group-type="heading">
<subject>Original Research</subject>
</subj-group>
</article-categories>
<title-group>
<article-title>Characterization and effects of impurities on carbonate quantification in heterogenous matrices</article-title>
<alt-title alt-title-type="left-running-head">Kashyap et al.</alt-title>
<alt-title alt-title-type="right-running-head">
<ext-link ext-link-type="uri" xlink:href="https://doi.org/10.3389/fenrg.2026.1771825">10.3389/fenrg.2026.1771825</ext-link>
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<name>
<surname>Kashyap</surname>
<given-names>Vivek</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
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<xref ref-type="corresp" rid="c001">&#x2a;</xref>
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<name>
<surname>Foster</surname>
<given-names>Kyle</given-names>
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<sup>1</sup>
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<surname>Bell</surname>
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<surname>Hottle</surname>
<given-names>John R.</given-names>
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<sup>2</sup>
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<name>
<surname>Gadikota</surname>
<given-names>Greeshma</given-names>
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<sup>3</sup>
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<surname>Upadhayay</surname>
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<sup>4</sup>
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<aff id="aff1">
<label>1</label>
<institution>National Laboratory of the Rockies</institution>, <city>Golden</city>, <state>CO</state>, <country country="US">United States</country>
</aff>
<aff id="aff2">
<label>2</label>
<institution>Prometheus Materials Inc.</institution>, <city>Longmont</city>, <state>CO</state>, <country country="US">United States</country>
</aff>
<aff id="aff3">
<label>3</label>
<institution>Department of Earth and Environmental Engineering, Columbia University</institution>, <city>New York</city>, <state>NY</state>, <country country="US">United States</country>
</aff>
<aff id="aff4">
<label>4</label>
<institution>Cornell University</institution>, <city>Ithaca</city>, <state>NY</state>, <country country="US">United States</country>
</aff>
<author-notes>
<corresp id="c001">
<label>&#x2a;</label>Correspondence: Vivek Kashyap, <email xlink:href="mailto:vivek.kashyap@nlr.gov">vivek.kashyap@nlr.gov</email>
</corresp>
</author-notes>
<pub-date publication-format="electronic" date-type="pub" iso-8601-date="2026-02-17">
<day>17</day>
<month>02</month>
<year>2026</year>
</pub-date>
<pub-date publication-format="electronic" date-type="collection">
<year>2026</year>
</pub-date>
<volume>14</volume>
<elocation-id>1771825</elocation-id>
<history>
<date date-type="received">
<day>19</day>
<month>12</month>
<year>2025</year>
</date>
<date date-type="rev-recd">
<day>17</day>
<month>01</month>
<year>2026</year>
</date>
<date date-type="accepted">
<day>26</day>
<month>01</month>
<year>2026</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2026 Kashyap, Foster, Vogelsberg, LaPanse, Bell, Hottle, Gadikota, Upadhayay and Rippy.</copyright-statement>
<copyright-year>2026</copyright-year>
<copyright-holder>Kashyap, Foster, Vogelsberg, LaPanse, Bell, Hottle, Gadikota, Upadhayay and Rippy</copyright-holder>
<license>
<ali:license_ref start_date="2026-02-17">https://creativecommons.org/licenses/by/4.0/</ali:license_ref>
<license-p>This is an open-access article distributed under the terms of the <ext-link ext-link-type="uri" xlink:href="https://creativecommons.org/licenses/by/4.0/">Creative Commons Attribution License (CC BY)</ext-link>. The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) 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.</license-p>
</license>
</permissions>
<abstract>
<p>Mineral carbonation simulates a natural weathering phenomena by breaking down silicates and oxides to form Ca &#x26; Mg carbonates. Various mineralization methods have been demonstrated as a potential technique to improve the quality of slags and tailings through neutralization and stabilization of problematic species to yield a product better suited for use in concrete. This study aims to characterize, quantify and analyze carbonates in various carbonated products such as mineralized CaCO<sub>3</sub>, CO<sub>2</sub> mineralized Steel Slags and Mine Tailings. More than 10 samples were analyzed for carbonate measurement and verification from industrial and academic partners that pioneer commercial CO<sub>2</sub> mineralization technologies. The samples were characterized primarily by using X-ray diffraction (XRD), Thermogravimetric Analyses (TGA), and Scanning Electron Microscopy (SEM) to gain insights into CaCO<sub>3</sub> content. A baseline characterization of lab-grade CaCO<sub>3</sub> and MgCO<sub>3</sub> also revealed important considerations for CaCO<sub>3</sub> measurement using TGA alone. The experiments using synthetic lab-grade samples also revealed that the presence of MgCO<sub>3</sub>/MgO can accelerate the decomposition of CaCO<sub>3</sub> and thus can affect measurement parameters. Lab-grade CaCO<sub>3</sub> samples dosed into steel slag and mine tailing also showed significant deviation in their decomposition behavior. These insights are used to inform the development of a standardized protocol for the measurement and verification of carbonate-bearing products.</p>
</abstract>
<kwd-group>
<kwd>carbonate quantification</kwd>
<kwd>carbonation</kwd>
<kwd>CO<sub>2</sub> mineralization</kwd>
<kwd>industrial waste</kwd>
<kwd>thermogravimetric analysis</kwd>
</kwd-group>
<funding-group>
<award-group id="gs1">
<funding-source id="sp1">
<institution-wrap>
<institution>Office of Technology Transitions</institution>
<institution-id institution-id-type="doi" vocab="open-funder-registry" vocab-identifier="10.13039/open_funder_registry">10.13039/100017268</institution-id>
</institution-wrap>
</funding-source>
</award-group>
<award-group id="gs2">
<funding-source id="sp2">
<institution-wrap>
<institution>Office of Fossil Energy and Carbon Management</institution>
<institution-id institution-id-type="doi" vocab="open-funder-registry" vocab-identifier="10.13039/open_funder_registry">10.13039/100020312</institution-id>
</institution-wrap>
</funding-source>
</award-group>
<funding-statement>The author(s) declared that financial support was received for this work and/or its publication. Funding for this work was provided by U.S. Department of Energy 521 Office of Technology Transitions, in partnership with the Offices of Fossil Energy and Carbon 522 Management and Clean Energy Demonstrations. This work was authored by the National Laboratory of the Rockies for the U.S. Department of Energy (DOE) under Contract No. DE-AC36-08GO28308. Funding provided by U.S. Department of Energy Office of Technology Transitions, in partnership with the Offices of Fossil Energy and Carbon Management and Clean Energy Demonstrations. The views expressed in the article do not necessarily represent the views of the DOE or the U.S. Government. </funding-statement>
</funding-group>
<counts>
<fig-count count="15"/>
<table-count count="7"/>
<equation-count count="4"/>
<ref-count count="54"/>
<page-count count="00"/>
</counts>
<custom-meta-group>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Carbon Capture, Utilization and Storage</meta-value>
</custom-meta>
</custom-meta-group>
</article-meta>
</front>
<body>
<sec sec-type="intro" id="s1">
<label>1</label>
<title>Introduction</title>
<p>The rising need for energy and environmental security and sustainability has increased the demand for critical and rare metals, leading to an increased generation of mine waste. The drive for sustainability and future technological developments requires an extensive and reliable supply of critical metals; meeting this crucial need is directly related to the generation of vast quantities of mine waste and tailings. The increase in tailing production and accumulation from mining operations is evident as about 8 billion tons of tailings were produced annually as reported in 2016 whereas Eker et al., in 2022, reported that &#x223c;10&#x2013;15 billion tons of tailings are generated annually across the globe, i.e., only &#x223c;20% of the total waste produced from mining operations (<xref ref-type="bibr" rid="B1">Adiguzel et al., 2022</xref>; <xref ref-type="bibr" rid="B29">Li et al., 2023</xref>; <xref ref-type="bibr" rid="B34">Oberle et al., 2020</xref>). Generally, tailings are hazardous due to the presence of heavy metals and other toxic components depending on the origin and pre-processing conditions. Therefore, sustainable chemical pathways to recover and separate the metals or toxic materials or immobilize them, are needed. From the perspective of these uses of tailings, they are utilized to backfill underground mines or as construction material. Conventionally, they are disposed of into tailing dams. Disposal into tailing dams also poses several significant safety risks including leakage into local ecosystems and contamination of the water table. However, utilization of tailings for further recovery of metals or as construction materials could substantially alleviate the risks of tailings management. Valorizing industrial waste for use in concrete not only reduces ecological damage but also yields economic advantage in terms of industrial waste management. Industrial wastes including steel slags and tailings have been readily studied for their utilization in concrete (<xref ref-type="bibr" rid="B1">Adiguzel et al., 2022</xref>; <xref ref-type="bibr" rid="B12">Gencel et al., 2021</xref>). One of the key concerns of using tailings and slags as ingredients for concrete is the presence of toxic heavy metals along with acidic, alkaline and other hazardous components (<xref ref-type="bibr" rid="B1">Adiguzel et al., 2022</xref>; <xref ref-type="bibr" rid="B42">Santos et al., 2012</xref>). Although blast furnace slags are unanimously accepted as construction materials, utilization of steel slags is not widely accepted primarily due to durability and concerns around leaching heavy metals (<xref ref-type="bibr" rid="B8">DiGiovanni et al., 2024</xref>; <xref ref-type="bibr" rid="B20">Huang et al., 2024</xref>).</p>
<p>Given the recent growth in carbonation studies of industrial wastes and ubiquitous presence of carbonates, determination of carbonates in a variety of samples requires a standardized approach. The presence of impurities in a heterogeneous matrix and relatively lower concentration of Ca/Mg carbonates can affect their quantification. Thermogravimetric analysis (TGA) is one of the most accessible techniques utilized for carbonate measurement due to straightforward mass-based measurements. Additional analytical power is gained when TGA is coupled with <italic>in situ</italic> Infrared (IR) CO<sub>2</sub> detectors, mass spectrometers, acid digestion, and Total Carbon Analyzers for additional, chemical-specific data outputs that have been more routinely integrated in studies by academics and industry (<xref ref-type="bibr" rid="B21">Ibrahim et al., 2019</xref>; <xref ref-type="bibr" rid="B41">RushendraRevathy et al., 2022</xref>; <xref ref-type="bibr" rid="B24">Kim and Azimi, 2021</xref>; <xref ref-type="bibr" rid="B11">Ferrara et al., 2023</xref>). Despite the straightforward nature of TGA, there is variability in applied methods and sample type that affect data collection. Specific examples include (a) preconditioning of samples to account for moisture content, (b) temperature ranges over which carbonate decomposition is measured, (c) temperature ramp rates, (d) sample particle size, and (e) flow rate and choice of purge gas (e.g., N<sub>2</sub>, CO<sub>2</sub>, Argon, or Air), and (f) competing thermally-driven reactions among sample constituents/impurities that can influence mass gain or loss. Together, these efforts can lead to large deviations when compared with other measurements which can impact data interpretation and constituent identification. An increasing number of construction efforts have emissions-related considerations including embodied carbon accounting, life cycle assessments, carbon crediting, and environmental product declarations as dictated by local and regional regulatory agencies. With cementitious materials and supplementary cementitious materials (SCMs) accounting for large volumes as well as large emissions-related impacts for many projects, inaccuracies in their carbonate quantification will have proportionately large effects. An over estimation CO<sub>2</sub> sequestration for a product will artificially inflate the impact of the selected materials, misrepresent products to regulatory agencies, and potentially damage the credibility of the entity supplying the material. Additionally, an underestimation of CO<sub>2</sub> sequestration would unnecessarily restrict the adoption and implementation of these materials.</p>
<p>Decomposition of CaCO<sub>3</sub> has been analyzed in the presence of CuO, ZnO, SiO<sub>2</sub>, Mg, organic acids, among other simple, binary material systems (<xref ref-type="bibr" rid="B25">Kumar et al., 2016</xref>; <xref ref-type="bibr" rid="B4">Calvo et al., 1990</xref>; <xref ref-type="bibr" rid="B30">Ma et al., 2005</xref>; <xref ref-type="bibr" rid="B19">Hou et al., 2005</xref>). It has been concluded by most authors that the presence of impurities has a catalytic effect on the decomposition of CaCO<sub>3</sub>, generally decreasing the onset temperature of mass loss. It is expected that a similar catalytic effect on decomposition could be present for a variety of industrial wastes, which is important to account for when standardizing the analysis ranges for carbonate determination. To the best of our knowledge, the decomposition of CaCO<sub>3</sub> dosed into samples with known decomposition behavior has not been studied in complex heterogeneous matrix such as mine tailings or steel slags in terms of standardizing a carbonate measurement. This may have a significant industrial relevance given the growth in commercialized technologies aimed at valorizing industrial waste for carbonation. From the literature that exists where carbonate measurements were completed using TGA, temperature ranges and ramp rates utilized are mentioned in <xref ref-type="table" rid="T1">Table 1</xref>. Even for similar material types from different sources, such as steel slag, the temperature ranges considered for carbonate quantification can vary significantly. Coupling this variance and the fact that standalone TGA measures only a mass loss signal results in inconclusive decomposition/dehydration mineral component analyses. This approach makes quantification by solely TGA susceptible to higher margins of errors for carbonate measurement in samples with different mineralogy. Thus, it is relatively easier to quantify high purity CaCO<sub>3</sub> samples compared to those with low purity having CaCO<sub>3</sub> content less than 20 wt%.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>CaCO<sub>3</sub> decomposition temperature range utilized in literature for carbonate quantification in heterogeneous matrix.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">References</th>
<th align="center">Species</th>
<th align="center">Heating rate (&#xb0;C/min)</th>
<th align="center">CaCO<sub>3</sub> decomposition temperature range in TGA (&#xb0;C)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">
<xref ref-type="bibr" rid="B46">Sun et al. (2024)</xref>
</td>
<td align="center">Sintering red mud</td>
<td align="center">10</td>
<td align="center">500&#x2013;800</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B50">Xu et al. (2024)</xref>
</td>
<td align="center">Sintering red mud</td>
<td align="center">10</td>
<td align="center">500&#x2013;760</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B24">Kim and Azimi (2021)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">Not mentioned</td>
<td align="center">600&#x2013;1200</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B51">Zhang et al. (2018)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">Not mentioned</td>
<td align="center">500&#x2013;1000</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B40">Rushendra Revathy et al. (2016)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">Not mentioned</td>
<td align="center">600&#x2013;850</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B35">Pan et al. (2014)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">10</td>
<td align="center">500&#x2013;850</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B21">Ibrahim et al. (2019)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">Not mentioned</td>
<td align="center">700&#x2013;800</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B10">Fang et al. (2024)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">10</td>
<td align="center">600&#x2013;800</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B5">Capelo-Avil&#xe9;s et al. (2024)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">10</td>
<td align="center">500&#x2013;900</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B49">Wang et al. (2024)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">10</td>
<td align="center">500&#x2013;800</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B11">Ferrara et al. (2023)</xref>
</td>
<td align="center">Steel slag</td>
<td align="center">10</td>
<td align="center">550&#x2013;850</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>This study focuses on characterization and quantification of carbonates in heterogeneous matrix primarily by using TGA and XRD. A variety of samples including lab-grade CaCO<sub>3</sub>, MgCO<sub>3</sub>, CO<sub>2</sub> mineralized calcium carbonate, steel slags and mine tailings were analyzed to evaluate effect of heterogeneous matrix on decomposition of CaCO<sub>3</sub>, that directly influences carbonate quantification. The study also attempts to provide considerations for the development of a standardized approach for carbonate quantification in samples with complex mineralogy.</p>
</sec>
<sec id="s2">
<label>2</label>
<title>Challenges with carbonate quantification</title>
<p>Mining waste or tailings are generated from mining, beneficiation, and downstream processing operations around the globe. Several mine wastes (especially from metal mining) are rich in Ca, Mg, and Al bearing lightweight silicate minerals that can be separated in the beneficiation step. Natural carbonation of mine tailings rich in Ca and Mg is generally slow but given the lengthy periods of landfilling result in significant quantities of carbonates. The determination and quantification of carbonates in these tailings can be challenging and analytically expensive given their complex mineralogy, prior processing, and environmental exposure. As discussed in <xref ref-type="sec" rid="s1">Section 1</xref>, TGA decomposition of CaCO<sub>3</sub> and MgCO<sub>3</sub> is one of the simplest ways to quantify carbonates. However, in the case of mine tailings, other components possessing similar temperature ranges of decomposition may affect the measurement. For example, brucite (Mg(OH)<sub>2</sub>), typically present in ultramafic mine tailings, decomposes in the temperature range of 300 &#xb0;C&#x2013;450 &#xb0;C which can overlap with the decomposition temperature range of MgCO<sub>3</sub> depending on the specific sample (<xref ref-type="bibr" rid="B47">Turvey et al., 2022</xref>; <xref ref-type="bibr" rid="B17">Harrison et al., 2013</xref>; <xref ref-type="bibr" rid="B52">Zhao et al., 2021</xref>) as well as overlapping MgCO<sub>3</sub>&#x2219;nH<sub>2</sub>O, as shown in this study. The presence of amorphous components further increases complexity and poses challenges to identify components that can interfere with carbonate measurements via TGA.</p>
</sec>
<sec id="s3">
<label>3</label>
<title>Experiments&#x2013;materials and characterization methods</title>
<sec id="s3-1">
<label>3.1</label>
<title>Materials</title>
<p>Lab-grade calcium carbonate with &#x3e;99% purity was procured from Thermo-Fisher Scientific and magnesium carbonate and amorphous silica gel were procured from Fisher-Scientific. Seven biomineralized calcium carbonate powder samples were provided by Prometheus Materials and prepared by their proprietary process using various algae strains. One mineralized calcium carbonate powder sample prepared by proprietary accelerated carbonation process was provided by the Gadikota Research Group. The steel slag and Cu-Ni mine tailing were received from Nucor Steel and Eagle Mine, Michigan respectively.</p>
</sec>
<sec id="s3-2">
<label>3.2</label>
<title>Experimental mix designs</title>
<p>Model system experiments were performed with synthetic lab-grade CaCO<sub>3</sub>, MgCO<sub>3</sub>&#x2219;nH<sub>2</sub>O and amorphous SiO<sub>2</sub> samples. Simplistic mix designs were used to assess the effects of varying quantities of MgCO<sub>3</sub> and amorphous silica on CaCO<sub>3</sub> decomposition as shown in <xref ref-type="table" rid="T2">Table 2</xref>. The synthetic samples used in this study had a top particle size of 75 &#xb5;m or less. The mineralized CaCO<sub>3</sub> received from research partners were also passed through 200 mesh (75 &#xb5;m) to ensure similar particle size across samples. In some cases, samples were hand-ground to achieve the particle size threshold. The industrial waste samples, mine tailing and steel slag, were ground and sieved with 200 mesh to achieve similar top particle size.</p>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Mix designs for model system experiments.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="left">Sample codes</th>
<th colspan="3" align="center">Target content (wt%)</th>
</tr>
<tr>
<th align="left">CaCO<sub>3</sub>
</th>
<th align="left">MgCO<sub>3</sub>&#x2219;nH<sub>2</sub>O</th>
<th align="left">SiO<sub>2</sub> gel</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">MD1</td>
<td align="center">99</td>
<td align="center">0</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD2</td>
<td align="center">0</td>
<td align="center">91</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD3</td>
<td align="center">50</td>
<td align="center">50</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD4</td>
<td align="center">30</td>
<td align="center">70</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD5</td>
<td align="center">70</td>
<td align="center">30</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD6</td>
<td align="center">40</td>
<td align="center">40</td>
<td align="center">20</td>
</tr>
<tr>
<td align="center">MD7</td>
<td align="center">30</td>
<td align="center">30</td>
<td align="center">40</td>
</tr>
<tr>
<td align="center">MD8</td>
<td align="center">20</td>
<td align="center">20</td>
<td align="center">60</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>MD1 and MD2 were the lab-grade CaCO<sub>3</sub> and MgCO<sub>3</sub>&#x2219;nH<sub>2</sub>O and their purity were measured using TGA.</p>
</fn>
</table-wrap-foot>
</table-wrap>
<p>The quantification of CaCO<sub>3</sub> was analyzed in a heterogeneous matrix by dosing steel slag and mine tailing with known amounts of lab-grade CaCO<sub>3</sub>. The mix designs for CaCO<sub>3</sub> dosed steel slag and mine tailing are listed in <xref ref-type="table" rid="T3">Table 3</xref>. The appropriate amounts of samples were weighed and mixed by gentle grinding in an agate mortar and pestle to ensure homogeneous mixing. For each matrix, i.e., steel slag and mine tailing, three samples were prepared to have approximately 2, 5, and 10 wt% CaCO<sub>3</sub> respectively.</p>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Mix designs for CaCO<sub>3</sub> quantification in heterogeneous matrix.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="center">Mix designs</th>
<th colspan="3" align="center">Target content (wt%)</th>
</tr>
<tr>
<th align="center">CaCO<sub>3</sub>
</th>
<th align="center">Steel slag</th>
<th align="center">Mine tailing</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">MD9</td>
<td align="center">10</td>
<td align="center">90</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD10</td>
<td align="center">5</td>
<td align="center">95</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD11</td>
<td align="center">2</td>
<td align="center">98</td>
<td align="center">0</td>
</tr>
<tr>
<td align="center">MD12</td>
<td align="center">10</td>
<td align="center">0</td>
<td align="center">90</td>
</tr>
<tr>
<td align="center">MD13</td>
<td align="center">5</td>
<td align="center">0</td>
<td align="center">95</td>
</tr>
<tr>
<td align="center">MD14</td>
<td align="center">2</td>
<td align="center">0</td>
<td align="center">98</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s3-3">
<label>3.3</label>
<title>Material characterization</title>
<p>Material characterization was performed using Thermogravimetric Analysis (TGA), X-ray Powder Diffraction (XRPD), and scanning electron microscope (SEM). The TGA (TA instrument TGA 5500) was used for carbonate quantification via thermal decomposition of CaCO<sub>3</sub>. 8&#x2013;12 mg of sample was loaded in a platinum pan at room temperature. The TGA experiments were performed at heating rates of 10 &#xb0;C/min and 20 &#xb0;C/min using N<sub>2</sub> at a 25 mL/min flowrate. The sample was initially heated to 105 &#xb0;C, followed by an isothermal hold for 15 min to determine the moisture content. Post isothermal hold, the sample was heated to 1000 &#xb0;C at the specified ramp rates above to ensure complete thermal decomposition of MgCO<sub>3</sub> and CaCO<sub>3</sub>. Triplicate TGA measurements were performed to ensure repeatability and reproducibility of this work.</p>
<p>CaCO<sub>3</sub> content was calculated using the sample mass loss in specified temperature range as shown in <xref ref-type="disp-formula" rid="e1">Equations 1</xref>, <xref ref-type="disp-formula" rid="e2">2</xref>.<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:mo>&#x394;</mml:mo>
<mml:mi>m</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi>w</mml:mi>
<mml:mrow>
<mml:mi>o</mml:mi>
<mml:mi>n</mml:mi>
<mml:mi>s</mml:mi>
<mml:mi>e</mml:mi>
<mml:mi>t</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x2212;</mml:mo>
<mml:msub>
<mml:mi>w</mml:mi>
<mml:mrow>
<mml:mi>e</mml:mi>
<mml:mi>n</mml:mi>
<mml:mi>d</mml:mi>
<mml:mi>s</mml:mi>
<mml:mi>e</mml:mi>
<mml:mi>t</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
<mml:msub>
<mml:mi>w</mml:mi>
<mml:mi>i</mml:mi>
</mml:msub>
</mml:mfrac>
<mml:mo>&#xd7;</mml:mo>
<mml:mn>100</mml:mn>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>
<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
<mml:mo>%</mml:mo>
<mml:mi>C</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>C</mml:mi>
<mml:mi>O</mml:mi>
<mml:mn>3</mml:mn>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mo>&#x394;</mml:mo>
<mml:mi>m</mml:mi>
</mml:mrow>
<mml:mn>43.97</mml:mn>
</mml:mfrac>
<mml:mo>&#xd7;</mml:mo>
<mml:mn>100</mml:mn>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>where, &#x394;m &#x3d; % mass loss between the onset and end temperature.</p>
<p>wonset &#x3d; sample mass at the onset decomposition temperature point.</p>
<p>Wendset &#x3d; sample mass at the endset decomposition temperature point</p>
<p>wi &#x3d; initial weight of the sample.</p>
<p>Onset and endset temperature of carbonate decompositions were calculated using tangent intercept method in TRIOS software, and was further used to calculate the range of decomposition as shown in <xref ref-type="disp-formula" rid="e3">Equation 3</xref>:<disp-formula id="e3">
<mml:math id="m3">
<mml:mrow>
<mml:mi>R</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>n</mml:mi>
<mml:mi>g</mml:mi>
<mml:mi>e</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:msub>
<mml:mi>T</mml:mi>
<mml:mrow>
<mml:mi>e</mml:mi>
<mml:mi>n</mml:mi>
<mml:mi>d</mml:mi>
<mml:mi>s</mml:mi>
<mml:mi>e</mml:mi>
<mml:mi>t</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x2212;</mml:mo>
<mml:msub>
<mml:mi>T</mml:mi>
<mml:mrow>
<mml:mi>o</mml:mi>
<mml:mi>n</mml:mi>
<mml:mi>s</mml:mi>
<mml:mi>e</mml:mi>
<mml:mi>t</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
</mml:math>
<label>(3)</label>
</disp-formula>
</p>
<p>In this expression, T<sub>endset</sub> &#x3d; endset decomposition temperature level and T<sub>onset</sub> &#x3d; onset decomposition temperature level. For steel slag and mine tailing samples dosed with known amounts of lab-grade CaCO<sub>3</sub>, % error of measurement was calculated according to <xref ref-type="disp-formula" rid="e4">Equation 4</xref>:<disp-formula id="e4">
<mml:math id="m4">
<mml:mrow>
<mml:mo>%</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mi>e</mml:mi>
<mml:mi>r</mml:mi>
<mml:mi>r</mml:mi>
<mml:mi>o</mml:mi>
<mml:mi>r</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="&#x7c;">
<mml:mrow>
<mml:mo>%</mml:mo>
<mml:mi>C</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>C</mml:mi>
<mml:mi>O</mml:mi>
<mml:mn>3</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:msub>
<mml:mi>Q</mml:mi>
<mml:mrow>
<mml:mi>C</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>C</mml:mi>
<mml:mi>O</mml:mi>
<mml:mn>3</mml:mn>
</mml:mrow>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:msub>
<mml:mi>Q</mml:mi>
<mml:mrow>
<mml:mi>C</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>C</mml:mi>
<mml:mi>O</mml:mi>
<mml:mn>3</mml:mn>
</mml:mrow>
</mml:msub>
</mml:mfrac>
<mml:mo>&#xd7;</mml:mo>
<mml:mn>100</mml:mn>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>
</p>
<p>In this expression, Q<sub>CaCO3</sub> &#x3d; known amount of CaCO<sub>3</sub> dosed into the samples.</p>
<p>XRPD was performed on Rigaku Ultima IV diffractometer with Cu- K&#x3b1; source (40 kV, 40 mA) to collect the diffraction pattern. Profex, open access software, and PDF4&#x2b; mineral database were used to perform Rietveld refinement on the XRPD data. Hitachi S4800 SEM was used to investigate morphological properties. The powders were evenly dispersed using a cotton swab on adhesive copper tape followed by sputter coating to decrease the charging effects.</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s4">
<label>4</label>
<title>Results and discussion</title>
<sec id="s4-1">
<label>4.1</label>
<title>Model system experiments with synthetic samples</title>
<sec id="s4-1-1">
<label>4.1.1</label>
<title>Carbonate decomposition analysis</title>
<p>The control experiments were performed with synthetic samples to establish a baseline and verify the TGA temperature range for quantification of carbonates. Since the samples received from industry partners were produced by their proprietary processes, comparison with lab-grade samples were important to understand influences caused by other constituents present on the TGA decomposition of carbonates. Although the thermal decomposition of pure carbonates is well studied (<xref ref-type="bibr" rid="B13">Georgieva et al., 2013</xref>; <xref ref-type="bibr" rid="B37">Popescu et al., 2014</xref>; <xref ref-type="bibr" rid="B7">Criado et al., 1995</xref>; <xref ref-type="bibr" rid="B36">Pillot et al., 2014</xref>; <xref ref-type="bibr" rid="B18">Hotta et al., 2022</xref>; <xref ref-type="bibr" rid="B9">Elder and Reddy, 1986</xref>), the blends of impurities pose a challenge of severe overlap in the TGA signal. This overlap is due to simultaneous decomposition and dehydration of carbonates, hydrates, and other minerals that may or may not be present in the CO<sub>2</sub> mineralized samples. <xref ref-type="table" rid="T4">Table 4</xref> lists the temperature range of decomposition of high purity CaCO<sub>3</sub> samples as obtained in various studies under different conditions. The decomposition temperature range varies significantly depending on several factors such as heating rate, crystallinity, morphology, and atmosphere. Therefore, using a specific temperature range to estimate the CO<sub>2</sub>/CaCO<sub>3</sub> content of the sample may not be accurate.</p>
<table-wrap id="T4" position="float">
<label>TABLE 4</label>
<caption>
<p>Temperature range of CaCO<sub>3</sub> decomposition as reported in selected literature.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Ref.</th>
<th align="center">Heating rate (&#xb0;C/min)</th>
<th align="center">Atmosphere</th>
<th align="center">Temperature range (&#xb0;C)</th>
<th align="center">Material</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">
<xref ref-type="bibr" rid="B36">Pillot et al. (2014)</xref>
</td>
<td align="center">20</td>
<td align="center">80% N<sub>2</sub>&#x2b;20% O<sub>2</sub>
</td>
<td align="center">575&#x2013;&#x223c;810</td>
<td align="center">Pure calcite</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B22">Karunadasa et al. (2019)</xref>
</td>
<td align="center">10</td>
<td align="left">Air</td>
<td align="center">700&#x2013;800</td>
<td align="center">Pure calcite</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B37">Popescu et al. (2014)</xref>
</td>
<td align="center">10</td>
<td align="left">N/A</td>
<td align="center">600&#x2013;790</td>
<td align="center">Precipitated CaCO<sub>3</sub> (74.5% calcite &#x2b;25.5% vaterite)</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B54">Zhuang et al. (2025)</xref>
</td>
<td align="center">20</td>
<td align="left">N<sub>2</sub>
</td>
<td align="center">475&#x2013;587</td>
<td align="center">Reagent grade CaCO<sub>3</sub> (&#x3e;99% calcite)</td>
</tr>
<tr>
<td align="center">
<xref ref-type="bibr" rid="B33">Mu and Perlmutter (1981)</xref>
</td>
<td align="center">1</td>
<td align="left">N<sub>2</sub>
</td>
<td align="center">605&#x2013;725</td>
<td align="center">99.92% CaCO<sub>3</sub>
</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>
<xref ref-type="fig" rid="F1">Figure 1</xref> shows the TGA decomposition curves for lab-grade CaCO<sub>3</sub> and MgCO<sub>3</sub>&#xb7;nH<sub>2</sub>O samples at heating rates of 10 &#xb0;C/min and 20 &#xb0;C/min. The TGA decomposition data for lab-grade CaCO<sub>3</sub> and MgCO<sub>3</sub> is listed in <xref ref-type="sec" rid="s12">Supplementary Table A1</xref>. The effect of heating rate on the decomposition of MgCO<sub>3</sub>&#xb7;nH<sub>2</sub>O was minor whereas the range of decomposition of CaCO<sub>3</sub> widened when heating rate increased from 10 &#xb0;C to 20 &#xb0;C/min. An increase in heating rate from 10 &#xb0;C to 20 &#xb0;C/min slightly increased the onset temperature (574 &#xb0;C&#x2013;593 &#xb0;C) whereas the end decomposition temperature increased from 769 &#xb0;C to 836 &#xb0;C. The effect of the heating rate observed in this study is consistent with that in literature. Baudin et al. and Elder et al. evaluated various heating rates to investigate the decomposition of CaCO<sub>3</sub> (<xref ref-type="bibr" rid="B36">Pillot et al., 2014</xref>; <xref ref-type="bibr" rid="B9">Elder and Reddy, 1986</xref>). The increase in end decomposition temperature with heating rate is possibly due to the thermal lag, rapid heating or both. However, as can be seen in <xref ref-type="fig" rid="F1">Figure 1</xref>, the lag was more significant for CaCO<sub>3</sub> compared to MgCO<sub>3</sub>. The thermal lag arises from the difference between the sample and furnace temperature but also depends on the thermal diffusivity of samples (<xref ref-type="bibr" rid="B6">Comes et al., 2012</xref>). The particle morphology of lab grade CaCO<sub>3</sub> showed calcite cubes (<xref ref-type="sec" rid="s12">Supplementary Figure A1</xref>). The calcite crystals observed in the lab-grade CaCO<sub>3</sub> were relatively larger than that in CO<sub>2</sub> mineralized samples. Also, a very small amount of aragonite was detected in the lab-grade CaCO<sub>3</sub> sample (<xref ref-type="sec" rid="s12">Supplementary Figure A2</xref>). The XRD quantification indicated that the aragonite content was only 0.7% (<xref ref-type="table" rid="T6">Table 6</xref>). TGA experiments on lab-grade CaCO<sub>3</sub> and MgCO<sub>3</sub>&#xb7;nH<sub>2</sub>O were performed to initially observe the effect of heating rates. 10 &#xb0;C/min and 20 &#xb0;C/min are standard heating rates that have been used in literature frequently (<xref ref-type="table" rid="T4">Table 4</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>TGA decomposition curve of CaCO<sub>3</sub> <bold>(a)</bold> and MgCO<sub>3</sub>.nH<sub>2</sub>O <bold>(b)</bold> at 10 &#xb0;C/min and 20 &#xb0;C/min heating rates.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g001.tif">
<alt-text content-type="machine-generated">Two panel scientific figure showing thermogravimetric analysis (TGA) and derivative weight loss curves for samples heated at rates of ten degrees Celsius per minute and twenty degrees Celsius per minute. Panel a displays weight percentage and derivative weight percentage per minute versus temperature from zero to one thousand degrees Celsius, with curves indicating significant weight loss near eight hundred degrees and corresponding derivative peaks. Panel b shows a similar plot with different sample behavior, including multi-step weight loss events and corresponding derivative peaks, highlighting different thermal decomposition profiles under the two heating rates.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s4-1-2">
<label>4.1.2</label>
<title>Effect of presence of MgCO<sub>3</sub> and amorphous silica</title>
<p>The effect of MgCO<sub>3</sub> and amorphous silica on CaCO<sub>3</sub> decomposition was also evaluated. MgCO<sub>3</sub> and amorphous silica are common mineral species within steel slags and mine tailings (<xref ref-type="bibr" rid="B41">RushendraRevathy et al., 2022</xref>; <xref ref-type="bibr" rid="B24">Kim and Azimi, 2021</xref>; <xref ref-type="bibr" rid="B11">Ferrara et al., 2023</xref>; <xref ref-type="bibr" rid="B10">Fang et al., 2024</xref>). Given the possible carbonated products, it is imperative to consider the effect of other components on quantification of carbonates. <xref ref-type="fig" rid="F2">Figure 2a</xref> shows the derivative (wt%/min) decomposition curve of CaCO<sub>3</sub> and MgCO<sub>3</sub>&#xb7;nH<sub>2</sub>O at different mix ratios. MD3, MD4 and MD5 samples were mixed to have approximately 50%, 30% and 70% CaCO<sub>3</sub> content respectively (<xref ref-type="table" rid="T2">Table 2</xref>). The inclusion of MgCO<sub>3</sub> accelerated the thermal decomposition of CaCO<sub>3</sub>. While MD3, MD4 and MD5 samples had similar decomposition temperature ranges for CaCO<sub>3</sub>, these ranges were lower than that of the pure lab-grade CaCO<sub>3</sub>. This indicates that the variation in MgCO<sub>3</sub> content does not have a significant effect on the decomposition temperature range of CaCO<sub>3.</sub> The observed reduction in CaCO<sub>3</sub> decomposition temperature in the presence of MgCO<sub>3</sub> can be explained by the decomposition of MgCO<sub>3</sub> which occurs first in the binary blend. Upon decomposition, CO<sub>2</sub> is released from MgCO<sub>3</sub> leaving MgO and CaCO<sub>3</sub>. MgO is a reactive species that can act catalytically to begin the decomposition of CaCO<sub>3</sub>. The shift in CaCO<sub>3</sub> decomposition is likely due to the formation of Mg-calcite where Mg exists in a solid solution in a calcium carbonate lattice. Due to higher diffusivity of Mg<sup>2&#x2b;</sup> ions compared to that of Ca<sup>2&#x2b;</sup>, Mg-substituted calcites have lower onset of thermal decomposition (<xref ref-type="bibr" rid="B32">Mo and Panesar, 2012</xref>). Anbalagan et al. also reported that the presence of Cl-salts could act as a catalyst in carbonate decomposition (<xref ref-type="bibr" rid="B15">Gunasekaran and Anbalagan, 2007</xref>).</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Effect of the presence of MgCO<sub>3</sub> and amorphous silica on the thermal decomposition of CaCO<sub>3</sub>. Heating rate: 20 &#xb0;C/min; Atmosphere: N<sub>2</sub>. <bold>(a)</bold> TGA derivative curve of MD3, MD4, and MD5 samples containing CaCO<sub>3</sub> and MgCO<sub>3</sub>; <bold>(b)</bold> TGA derivative curve of MD6, MD7, and MD8 samples containing CaCO<sub>3</sub>, MgCO<sub>3</sub> and amorphous silica gel.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g002.tif">
<alt-text content-type="machine-generated">Two-panel figure showing derivative weight percentage versus temperature for various samples during thermal analysis. Panel a compares lab-grade CaCO&#x2083; and MgCO&#x2083; with MD3, MD4, and MD5, indicating dehydration, MgCO&#x2083; decomposition, and CaCO&#x2083; decomposition with a noted shift in decomposition temperature. Panel b compares lab-grade CaCO&#x2083; with MD6, MD7, and MD8, also showing dehydration, intermediate decomposition, and CaCO&#x2083; decomposition peaks.</alt-text>
</graphic>
</fig>
<p>Similarly, the effect of amorphous silica on lab grade CaCO<sub>3</sub> and MgCO<sub>3</sub> decomposition was also analyzed. <xref ref-type="fig" rid="F2">Figure 2b</xref> shows the derivative curves obtained from the TGA experiments for samples MD6, MD7 and MD8 containing approximately 20%, 40% and 60% amorphous silica gel respectively. The effect of silica was analyzed in the presence of MgCO<sub>3</sub> to have a baseline comparison on its effect on MgCO<sub>3</sub> decomposition. The CaCO<sub>3</sub> and MgCO<sub>3</sub> content in MD6, MD7, and MD8 were kept at 40%, 30%, and 20% respectively as mentioned in <xref ref-type="table" rid="T2">Table 2</xref>. As can be observed from <xref ref-type="fig" rid="F2">Figure 2b</xref>, the decomposition temperature range of MgCO<sub>3</sub> almost remained the same whereas the CaCO<sub>3</sub> decomposition was still observed to have early onset and end temperature compared to pure lab-grade CaCO<sub>3</sub>. This supports the explanation of MgCO<sub>3</sub> acting catalytically to induce early decomposition as observed in samples MD3, MD4, and MD5. The onset temperature of CaCO<sub>3</sub> decomposition in samples MD3, MD4, and MD5 varied from 547 &#xb0;C to556 &#xb0;C whereas with the addition of silica (MD6, MD7, and MD8), the onset temperatures of CaCO<sub>3</sub> decomposition slightly increased to 571 &#xb0;C&#x2013;584 &#xb0;C as shown in <xref ref-type="fig" rid="F3">Figure 3</xref>. The addition of amorphous silica delayed the onset of CaCO<sub>3</sub> decomposition. Nevertheless, the average endset temperature of decomposition remains similar to MD3, MD4, and MD5 samples, leading to a shorter decomposition temperature range. Overall, the average decomposition temperature range of lab-grade CaCO<sub>3</sub> is reduced from a span of 243 &#xb0;C&#x2013;188 &#xb0;C when MgCO<sub>3</sub> was added and further to 170 &#xb0;C after amorphous silica addition.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>TGA thermal decomposition data of lab-grade CaCO<sub>3</sub> in the presence of MgCO<sub>3</sub> and amorphous silica gel. A heating rate of 20 &#xb0;C/min in N<sub>2</sub> atmosphere was used.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g003.tif">
<alt-text content-type="machine-generated">Bar chart comparing onset, endset, peak temperature, and temperature range for lab grade CaCO&#x2083; and six MD samples. Lab grade CaCO&#x2083; has the highest onset, endset, and peak temperatures, and MD samples have lower values overall.</alt-text>
</graphic>
</fig>
</sec>
</sec>
<sec id="s4-2">
<label>4.2</label>
<title>Mineralized CaCO<sub>3</sub> powder</title>
<p>The TGA analyses of mineralized CaCO<sub>3</sub> powders revealed slight differences in decomposition onset temperature compared to the lab grade CaCO<sub>3</sub>. The TGA mass loss curves are shown in <xref ref-type="fig" rid="F4">Figure 4</xref> and the onset and endset temperature of the thermal decomposition of mineralized and lab-grade CaCO<sub>3</sub> samples are listed in <xref ref-type="table" rid="T5">Table 5</xref>. Note that the TGA measurements were performed at heating rate of 10 &#xb0;C/min under N<sub>2</sub> atmosphere. The onset and endset temperature levels have been considered parameters for comparison between different CaCO<sub>3</sub> sample types. It was observed that the onset temperatures of CaCO<sub>3</sub> samples decomposition varied between 515 &#xb0;C and 577 &#xb0;C whereas the endset temperatures varied between 690 &#xb0;C and 763 &#xb0;C. The highest onset and endset temperature levels were observed in the case of lab grade CaCO<sub>3</sub> corresponding to widest temperature range of decomposition. The wide decomposition temperature range for lab-grade CaCO<sub>3</sub> could be due to kinetic limitations at the highest CaCO<sub>3</sub> concentration as well as the higher crystallinity of calcite as confirmed with SEM analyses.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>TGA decomposition curves of lab-grade and mineralized CaCO<sub>3</sub> samples. Heating rate: 10 &#xb0;C/min; Atmosphere: N<sub>2</sub>.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g004.tif">
<alt-text content-type="machine-generated">Line graph comparing weight percentage versus temperature in degrees Celsius for eight samples labeled MC1 to MC8, showing a sharp weight loss for all samples between approximately 600 and 800 degrees Celsius.</alt-text>
</graphic>
</fig>
<table-wrap id="T5" position="float">
<label>TABLE 5</label>
<caption>
<p>TGA thermal decomposition data of mineralized CaCO<sub>3</sub> samples. Heating rate: 10 &#xb0;C/min; Atmosphere: N<sub>2</sub>.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Sample name</th>
<th align="center">Onset temperature (&#xb0;C)</th>
<th align="center">Endset temperature (&#xb0;C)</th>
<th align="center">Range (&#xb0;C)</th>
<th align="center">Mass loss (%)</th>
<th align="center">CaCO<sub>3</sub> content (%)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Lab grade CaCO3</td>
<td align="center">577</td>
<td align="center">763</td>
<td align="center">186</td>
<td align="center">43.46</td>
<td align="center">98.84</td>
</tr>
<tr>
<td align="center">MC1</td>
<td align="center">515</td>
<td align="center">699</td>
<td align="center">184</td>
<td align="center">41.49</td>
<td align="center">94.36</td>
</tr>
<tr>
<td align="center">MC2</td>
<td align="center">563</td>
<td align="center">731</td>
<td align="center">168</td>
<td align="center">40.77</td>
<td align="center">92.73</td>
</tr>
<tr>
<td align="center">MC3</td>
<td align="center">550</td>
<td align="center">720</td>
<td align="center">170</td>
<td align="center">41.96</td>
<td align="center">95.43</td>
</tr>
<tr>
<td align="center">MC4</td>
<td align="center">535</td>
<td align="center">711</td>
<td align="center">176</td>
<td align="center">40.97</td>
<td align="center">93.18</td>
</tr>
<tr>
<td align="center">MC5</td>
<td align="center">571</td>
<td align="center">724</td>
<td align="center">153</td>
<td align="center">42.71</td>
<td align="center">97.14</td>
</tr>
<tr>
<td align="center">MC6</td>
<td align="center">561</td>
<td align="center">714</td>
<td align="center">153</td>
<td align="center">39.53</td>
<td align="center">89.91</td>
</tr>
<tr>
<td align="center">MC7</td>
<td align="center">549</td>
<td align="center">690</td>
<td align="center">141</td>
<td align="center">35.27</td>
<td align="center">80.21</td>
</tr>
<tr>
<td align="center">MC8</td>
<td align="center">540</td>
<td align="center">728</td>
<td align="center">188</td>
<td align="center">42.1</td>
<td align="center">95.74</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>In addition to physical parameters such as particle size, sample size, and run conditions, the temperature range of CaCO<sub>3</sub> decomposition not only depends on the crystallinity of calcite but also on the presence of other polymorphs such as vaterite and aragonite (<xref ref-type="bibr" rid="B23">Kemp et al., 2022</xref>). The powder XRD patterns of mineralized CaCO<sub>3</sub> samples are shown in <xref ref-type="fig" rid="F5">Figure 5</xref>. Calcite was found to be the major CaCO<sub>3</sub> polymorph in most of the samples except MC1 and MC2 where vaterite is the major CaCO<sub>3</sub> polymorph. Since the mineralized samples were crystalline, the XRD results showed that calcite and vaterite could easily be identified with the XRD as characteristic diffraction peaks of calcite and vaterite are obtained at 2&#x3b8; angle of 29.4&#xb0; and 27&#xb0; respectively.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>XRD patterns of mineralized CaCO<sub>3</sub> samples showing presence of calcite and vaterite. C: Calcite; V: Vaterite. Note that the minor mineral phases are not indicated in this figure.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g005.tif">
<alt-text content-type="machine-generated">X-ray diffraction pattern with eight overlaid traces labeled MC1 through MC8, displaying intensity versus 2-theta angle from twenty to sixty degrees. Peaks are marked with &#x201C;V&#x201D; for MC1 and &#x201C;C&#x201D; for MC8.</alt-text>
</graphic>
</fig>
<p>
<xref ref-type="table" rid="T6">Table 6</xref> presents detailed QXRD results of mineralized CaCO<sub>3</sub> showing minor components present in the mineralized CaCO<sub>3</sub> samples and include MgCO<sub>3</sub>, MgCO<sub>3</sub>&#xb7;nH<sub>2</sub>O, NaNO<sub>3</sub>, Na<sub>2</sub>SO<sub>4</sub>, CaMg<sub>3</sub>(CO<sub>3</sub>)<sub>4</sub>, SiO<sub>2</sub>, and NaHCO<sub>3</sub>. In general, the presence of minor mineral phases in mineralized CaCO<sub>3</sub> depends a lot on process and chemical reagents used. The QXRD results indicated that MC1, MC2 and MC3 samples contain 59%, 54.5% and 21.3% vaterite respectively. The presence of vaterite in samples MC1, MC2 and MC3 did not lead to decrease in the onset decomposition temperature. The vaterite content slightly decreased from 59% in MC1 to 54.5% in MC2. However, the onset decomposition temperature increased from 515 &#xb0;C in MC1 to 563 &#xb0;C in MC2. The vaterite content did not appear to decrease the onset decomposition temperature of mineralized CaCO<sub>3</sub> samples. The maximum calcite as well as CaCO<sub>3</sub> content in mineralized samples was observed in MC5, i.e., 97%, which corresponds to the highest decomposition onset temperature (571 &#xb0;C) compared to other mineralized CaCO<sub>3</sub> samples analyzed in this study.</p>
<table-wrap id="T6" position="float">
<label>TABLE 6</label>
<caption>
<p>QXRD results of lab-grade and mineralized CaCO<sub>3</sub> obtained from Profex.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th colspan="14" align="center">Quantification (wt%)</th>
<th colspan="4" align="center">Refinement statistics</th>
</tr>
<tr>
<th align="center">
<italic>Sample</italic>
</th>
<th align="center">
<italic>Calcite</italic>
</th>
<th align="center">
<italic>Aragonite</italic>
</th>
<th align="center">
<italic>Vaterite</italic>
</th>
<th align="center">
<italic>MgO</italic>
</th>
<th align="center">
<italic>MgCO</italic>
<sub>
<italic>3</italic>
</sub>
</th>
<th align="center">
<italic>MgCO</italic>
<sub>
<italic>3</italic>
</sub>
<italic>.5H</italic>
<sub>
<italic>2</italic>
</sub>
<italic>O</italic>
</th>
<th align="center">
<italic>MgCO</italic>
<sub>
<italic>3</italic>
</sub>
<italic>.3H</italic>
<sub>
<italic>2</italic>
</sub>
<italic>O</italic>
</th>
<th align="center">
<italic>NaNO</italic>
<sub>
<italic>3</italic>
</sub>
</th>
<th align="center">
<italic>Na</italic>
<sub>
<italic>2</italic>
</sub>
<italic>SO</italic>
<sub>
<italic>4</italic>
</sub>
</th>
<th align="center">
<italic>CaMg</italic>
<sub>
<italic>3</italic>
</sub>
<italic>(CO</italic>
<sub>
<italic>3</italic>
</sub>
<italic>)</italic>
<sub>
<italic>4</italic>
</sub>
</th>
<th align="center">
<italic>Mg-Calcite</italic>
</th>
<th align="center">
<italic>SiO</italic>
<sub>
<italic>2</italic>
</sub>
</th>
<th align="center">
<italic>NaHCO</italic>
<sub>
<italic>3</italic>
</sub>
</th>
<th align="center">
<italic>Rwp</italic>
</th>
<th align="center">
<italic>Rexp</italic>
</th>
<th align="center">
<italic>&#x3c7;2</italic>
</th>
<th align="center">
<italic>GOF</italic>
</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Lab grade CaCO<sub>3</sub>
</td>
<td align="center">99.3</td>
<td align="center">0.7</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">10.2</td>
<td align="center">7.3</td>
<td align="center">1.9</td>
<td align="center">1.4</td>
</tr>
<tr>
<td align="center">MC1</td>
<td align="center">36.9</td>
<td align="center">0.0</td>
<td align="center">59.0</td>
<td align="center">0.0</td>
<td align="center">4.1</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">10.1</td>
<td align="center">6.9</td>
<td align="center">2.1</td>
<td align="center">1.5</td>
</tr>
<tr>
<td align="center">MC2</td>
<td align="center">38.4</td>
<td align="center">1.1</td>
<td align="center">54.5</td>
<td align="center">0.0</td>
<td align="center">6.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">7.2</td>
<td align="center">2.9</td>
<td align="center">6.2</td>
<td align="center">2.5</td>
</tr>
<tr>
<td align="center">MC3</td>
<td align="center">70.3</td>
<td align="center">0.7</td>
<td align="center">21.3</td>
<td align="center">0.0</td>
<td align="center">4.4</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">3.4</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">10.6</td>
<td align="center">6.7</td>
<td align="center">2.5</td>
<td align="center">1.6</td>
</tr>
<tr>
<td align="center">MC4</td>
<td align="center">94.4</td>
<td align="center">0.8</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.2</td>
<td align="center">2.5</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">2.1</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">9.7</td>
<td align="center">7.3</td>
<td align="center">1.8</td>
<td align="center">1.3</td>
</tr>
<tr>
<td align="center">MC5</td>
<td align="center">97.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">2.1</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">9.4</td>
<td align="center">7.5</td>
<td align="center">1.6</td>
<td align="center">1.3</td>
</tr>
<tr>
<td align="center">MC6</td>
<td align="center">89.6</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">1.9</td>
<td align="center">4.0</td>
<td align="center">0.9</td>
<td align="center">3.6</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">7.8</td>
<td align="center">3.0</td>
<td align="center">6.6</td>
<td align="center">2.6</td>
</tr>
<tr>
<td align="center">MC7</td>
<td align="center">85.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">1.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">2.1</td>
<td align="center">5.0</td>
<td align="center">0.0</td>
<td align="center">3.9</td>
<td align="center">0.0</td>
<td align="center">2.2</td>
<td align="center">0.8</td>
<td align="center">7.7</td>
<td align="center">3.0</td>
<td align="center">6.6</td>
<td align="center">2.6</td>
</tr>
<tr>
<td align="center">MC8</td>
<td align="center">85.1</td>
<td align="center">0.0</td>
<td align="center">1.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">2.1</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">0.0</td>
<td align="center">11.8</td>
<td align="center">0.0</td>
<td align="center">0</td>
<td align="center">9.8</td>
<td align="center">6.5</td>
<td align="center">2.3</td>
<td align="center">1.5</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Overall, CaCO<sub>3</sub> contents obtained from QXRD and TGA were in good agreement except for MC7 sample (<xref ref-type="fig" rid="F6">Figure 6</xref>). The CaCO<sub>3</sub> content in MC7 obtained from QXRD and TGA were about 86.1% and 80.5%, respectively. Particularly for MC7 sample, QXRD and TGA measurements were not in good agreement. A minor amount of NaNO<sub>3</sub> (4%&#x2013;5%) was detected in MC6 and MC7 samples (<xref ref-type="table" rid="T6">Table 6</xref>) that also have a similar temperature range of decomposition as CaCO<sub>3</sub>. The thermal decomposition of sodium nitrate has an onset in the range of 580 &#xb0;C&#x2013;600 &#xb0;C (<xref ref-type="bibr" rid="B2">Bartos et al., 1944</xref>; <xref ref-type="bibr" rid="B14">Gimenez and Fereres, 2015</xref>). Gimenez et al. used a similar TGA decomposition temperature profile to that in this study (10 &#xb0;C/min; N<sub>2</sub>) and found the onset decomposition temperature of NaNO<sub>3</sub> being close to &#x223c;613 &#xb0;C (<xref ref-type="bibr" rid="B14">Gimenez and Fereres, 2015</xref>). However, in case of MC7, the deviation in CaCO<sub>3</sub> measurement should not be entirely attributed to presence of these minor components. The presence of organic components may also result in overestimation in case of QXRD. In this case, QXRD measurement clearly appears to overestimate the CaCO<sub>3</sub> content where TGA measurement can also be deemed an underestimation due to possible overlap with decomposition of NaNO<sub>3</sub>.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>CaCO<sub>3</sub> contents calculated for mineralized samples using QXRD and TGA.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g006.tif">
<alt-text content-type="machine-generated">Scatterplot with black data points comparing calcium carbonate content measured by TGA on the x-axis and by QXRD on the y-axis, featuring a dotted trend line with the equation y equals 1.0144x and R squared value 0.9995. Points labeled MC6 and MC7 are visible.</alt-text>
</graphic>
</fig>
<p>The overlap between decomposition temperature ranges of CaCO<sub>3</sub> and NaNO<sub>3</sub> or other minor components appears to be another important factor affecting carbonate quantification when using only TGA. Although the magnitude of error in this study is relatively smaller, higher concentrations of NaNO<sub>3</sub> or other components may affect the TGA measurement of CaCO<sub>3</sub> content significantly.</p>
<p>The particle morphological examination of mineralized CaCO<sub>3</sub> samples provided more insight into the presence of different polymorphs, cubic as well as rhombohedral calcite crystals. SEM images of MC1, MC4, MC5, and MC8 are shown in <xref ref-type="fig" rid="F7">Figures 7</xref>&#x2013;<xref ref-type="fig" rid="F9">9</xref> respectively. MC1 was mostly observed to contain cubic calcite crystals where calcites mostly appear as clusters, however, isolated vaterite crystals were also found. The vaterite crystals present were not perfectly spherical and were seemingly fused together as shown in <xref ref-type="fig" rid="F7">Figure 7c</xref>. Due to the presence of vaterite clusters, the grain size calculated from XRD data is different from that observed under the SEM. MC4 and MC5 exhibit very different particle morphologies as compared to other samples. MC4 contained two different types of calcite crystals, i.e., poorly crystallized cubic calcite and hexagonal calcite rose-like morphology (<xref ref-type="fig" rid="F8">Figure 8a</xref>). On the other hand, MC5 was mostly observed to have layered rhombohedral calcite crystals. <xref ref-type="fig" rid="F9">Figure 9</xref> shows the cubic crystallites of calcite observed in MC8. Most of the calcite crystallites are smaller than a micron and appear in clusters. Some isolated calcite crystals bigger than a micron were also observed but were found to contain cubic ultrafine crystallites clustered together. As also calculated from the XRD data, calcites with the smallest grain size were present in MC8, i.e., 36.3 nm MC2, MC6, MC7, and MC8 were found to exhibit crystallite size of less than 100 nm (<xref ref-type="sec" rid="s12">Supplementary Table A2</xref>).</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>SEM images of MC1 showing presence of vaterite <bold>(a,c)</bold> and calcite <bold>(b)</bold>.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g007.tif">
<alt-text content-type="machine-generated">Panel a shows a scanning electron microscope image of clustered spherical vaterite particles labeled with an arrow. Panel b displays both spherical vaterite and a central cuboidal calcite crystal with annotated size measurements. Panel c depicts fused vaterite formations indicated by an arrow, with granular texture and varying particle shapes.</alt-text>
</graphic>
</fig>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>SEM image of MC4 <bold>(a)</bold> and MC5 <bold>(b)</bold>. Distorted and hexagonal calcite crystals observed in MC4. Stacked calcite crystals observed in MC5.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g008.tif">
<alt-text content-type="machine-generated">Panel a features four scanning electron microscope micrographs of mineral particles with rough, irregular surfaces and layered crystalline textures at varying magnifications, ranging from several micrometres to submicrometre scales.Panel b presents four scanning electron microscope images of different mineral particles, displaying distinct angular, faceted structures and visible crystalline edges at varying sizes, highlighting differences in morphology between samples.</alt-text>
</graphic>
</fig>
<fig id="F9" position="float">
<label>FIGURE 9</label>
<caption>
<p>SEM image of MC8 showing cubic calcite ultrafine crystals.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g009.tif">
<alt-text content-type="machine-generated">Scanning electron microscope image panel showing four grayscale micrographs labeled i, ii, iii, and iv at different magnifications. Images depict clusters of angular and irregularly shaped particles with varying sizes and surface textures. Scale bars range from one point five micrometers to six hundred nanometers.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s4-3">
<label>4.3</label>
<title>Mine tailing</title>
<p>The Cu-Ni mine tailing exhibited a complex mineralogy, having a mix of various ultramafic silicate minerals, sulfides, sulfates, and other basaltic minerals such as chlorite. The qualitative XRD analysis confirmed the presence of lizardite, augite, forsterite, bytownite, chlorite, pyrrhotite as major crystalline phases (<xref ref-type="fig" rid="F10">Figure 10</xref>). A complete list of mineral phases identified in Mine Tailing sample is mentioned in <xref ref-type="sec" rid="s12">Supplementary Table A3</xref>. Note that there was no characteristic CaCO<sub>3</sub> peak observed in this case. A similar class of mineral phases were observed in a study by Mends et al. on flotation tailing from Eagle mine (<xref ref-type="bibr" rid="B31">Mends et al., 2025</xref>).</p>
<fig id="F10" position="float">
<label>FIGURE 10</label>
<caption>
<p>Major mineral phases identified in Mine Tailing using XRD.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g010.tif">
<alt-text content-type="machine-generated">X-ray diffraction (XRD) pattern graph with intensity in arbitrary units versus 2-theta in degrees, indicating various mineral phases: lizardite, pyrrhotite, quartz, magnetite, augite, bytownite, and forsterite, identified by different symbols.</alt-text>
</graphic>
</fig>
<p>The TGA thermal decomposition results of raw mine tailing showed a continuous mass loss especially in the range of 450 &#xb0;C&#x2013;1000 &#xb0;C. Two major derivative peaks at 514 &#xb0;C and 679 &#xb0;C were observed as indicated in <xref ref-type="fig" rid="F11">Figure 11a</xref>. The first mass loss was observed in the range of &#x223c;410 &#xb0;C&#x2013;625 &#xb0;C whereas the second mass loss in the range of 615 &#xb0;C&#x2013;751 &#xb0;C, followed by two small derivative peaks ranging up to &#x223c;850 &#xb0;C. Majority of the mass loss in the range of 450 &#xb0;C&#x2013;800 &#xb0;C can be attributed to the decomposition of lizardite and chlorite. However, a small part of mass loss can also be attributed to dolomite decomposition that occurs in the similar temperature range. Lizardite, the major mineral phase in the mine tailing sample, decomposes in a similar temperature range to that of CaCO<sub>3</sub>. Zhou et al. studied the dehydroxylation of lizardite and observed a continuous mass loss in the range of 580 &#xb0;C&#x2013;700 &#xb0;C and a peak at &#x223c;624 &#xb0;C with 15 &#xb0;C/min heating rate in N<sub>2</sub> atmosphere (<xref ref-type="bibr" rid="B53">Zhou et al., 2017</xref>). Lempart et al. studied the dehydroxylation of three different chlorite samples and observed mass loss in two steps with major mass loss being in the range of &#x223c;400 &#xb0;C&#x2013;600 &#xb0;C with a heating rate of 10 &#xb0;C/min in N<sub>2</sub> atmosphere (<xref ref-type="bibr" rid="B27">Lempart et al., 2018</xref>). Note that the dehydroxylation of both chlorite and lizardite releases water vapor that is known to have a catalytic effect on the decomposition of CaCO<sub>3</sub> (<xref ref-type="bibr" rid="B45">Silakhori et al., 2021</xref>), albeit it may not have significant effect in this case given the small amount of sample.</p>
<fig id="F11" position="float">
<label>FIGURE 11</label>
<caption>
<p>TGA thermal decomposition mass loss and derivative curves; <bold>(a)</bold> raw mine tailing; <bold>(b)</bold> raw and CaCO<sub>3</sub> dosed mine tailing samples; <bold>(c)</bold> Comparison with pure lab grade CaCO<sub>3</sub>. Heating rate: 20 &#xb0;C/min; Atmosphere: N<sub>2</sub>.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g011.tif">
<alt-text content-type="machine-generated">Panel a shows a thermogravimetric analysis plot with weight and derivative weight versus temperature, highlighting chlorite and lizardite dehydroxylation. Panel b compares four samples&#x2019; weight loss and derivative weight, labeled as Mine Tailing, MD12, MD13, and MD14. Panel c depicts derivative weight versus temperature for four samples and lab grade CaCO&#x2083;, showing a major peak for CaCO&#x2083; near 800 degrees Celsius.</alt-text>
</graphic>
</fig>
<p>
<xref ref-type="fig" rid="F11">Figures 11b,c</xref> shows the derivative curves of samples with lab-grade CaCO<sub>3</sub> dosed into mine tailing and pure lab-grade CaCO<sub>3</sub>. The decomposition of lab-grade CaCO<sub>3</sub>, irrespective of concentration, overlaps with that of the lizardite dehydroxylation step. This indicates that baseline correction is needed in order to quantify the fresh carbonates. As also mentioned in previous sections, in addition to operating conditions such as heating rate, particle size, CO<sub>2</sub> partial pressure, crystallinity etc., the decomposition temperature range of calcium carbonate varies significantly given the presence of polymorphs and impurities. The CaCO<sub>3</sub> dosing was helpful in order to recognize its decomposition temperature range in a specific matrix, especially in complex matrices such as tailings and slags. The dosing technique could be helpful for carbonation studies to deconvolute temperature ranges of decomposition of calcium carbonates and other components in a given matrix. The thermal decomposition data of mine tailing samples dosed with calcium carbonate is also mentioned in <xref ref-type="table" rid="T7">Table 7</xref>.</p>
<table-wrap id="T7" position="float">
<label>TABLE 7</label>
<caption>
<p>TGA thermal decomposition data of lab-grade CaCO<sub>3</sub> in steel slag and mine tailing matrix. Note: Average numbers are reported based on triplicate measurement for each sample.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Sample</th>
<th align="center">Matrix</th>
<th align="center">Onset temperature (&#xb0;C)</th>
<th align="center">Endset temperature (&#xb0;C)</th>
<th align="center">Range (&#xb0;C)</th>
<th align="center">Peak temperature (&#xb0;C)</th>
<th align="center">Known amount of CaCO3 (wt%)</th>
<th align="center">Wt.% of CaCO3 (calculated)</th>
<th align="center">% error</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">MD9</td>
<td rowspan="3" align="center">Steel slag</td>
<td align="center">631</td>
<td align="center">762</td>
<td align="center">131</td>
<td align="center">709</td>
<td align="center">10.37</td>
<td align="center">10.53</td>
<td align="center">1.50</td>
</tr>
<tr>
<td align="left">MD10</td>
<td align="center">615</td>
<td align="center">746</td>
<td align="center">131</td>
<td align="center">695</td>
<td align="center">5.03</td>
<td align="center">5.14</td>
<td align="center">2.23</td>
</tr>
<tr>
<td align="left">MD11</td>
<td align="center">610</td>
<td align="center">747</td>
<td align="center">137</td>
<td align="center">688</td>
<td align="center">1.98</td>
<td align="center">1.89</td>
<td align="center">&#x2212;4.78</td>
</tr>
<tr>
<td align="left">MD12</td>
<td rowspan="3" align="center">Mine tailing</td>
<td align="center">617</td>
<td align="center">762</td>
<td align="center">145</td>
<td align="center">716</td>
<td align="center">10.02</td>
<td align="center">9.72</td>
<td align="center">&#x2212;2.97</td>
</tr>
<tr>
<td align="left">MD13</td>
<td align="center">612</td>
<td align="center">758</td>
<td align="center">146</td>
<td align="center">695</td>
<td align="center">4.38</td>
<td align="center">4.2</td>
<td align="center">&#x2212;4.04</td>
</tr>
<tr>
<td align="left">MD14</td>
<td align="center">603</td>
<td align="center">752</td>
<td align="center">149</td>
<td align="center">685</td>
<td align="center">2.05</td>
<td align="center">2.02</td>
<td align="center">&#x2212;1.26</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s4-4">
<label>4.4</label>
<title>Steel slag</title>
<p>Like mine tailings, steel slags also possessed a complex mineralogy, however, the measurement of carbonates in steel slag must take into account a slightly different silicate matrix. A qualitative XRD analysis revealed that calcite, merwinite, belite and akermanite are the major crystalline phases present whereas minor phases such as wustite, mayenite, magnetite, magnesite, quartz, were also observed (<xref ref-type="fig" rid="F12">Figure 12</xref>). A complete list of mineral phases identified in a mine tailing sample is mentioned in <xref ref-type="sec" rid="s12">Supplementary Table A3</xref>. In addition to all the possible minor crystalline phases, a part of the sample was amorphous or poorly crystalline as possible amorphous humps were observed at 2&#x3b8; close to 11&#xb0; and 32&#xb0;. The accuracy of QXRD methods is typically high, however, the presence of amorphous mineral phases could result in uncertainty in carbonate quantification.</p>
<fig id="F12" position="float">
<label>FIGURE 12</label>
<caption>
<p>Major mineral phases identified in EAF Steel Slag using XRD.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g012.tif">
<alt-text content-type="machine-generated">X-ray diffraction graph with intensity on the y-axis and 2&#x03B8; in degrees on the x-axis, displaying various symbol markers identifying different minerals including calcite, merwinite, belite, wustite, quartz, akermanite, mayenite, and magnetite. Calcite was found as the major mineral phase present in the EAF steel slag.</alt-text>
</graphic>
</fig>
<p>
<xref ref-type="fig" rid="F13">Figure 13a</xref> shows the TGA decomposition curve of steel slag with step wise mass losses in different temperature range. Although qualitative mineralogical analysis is conducive in understanding mass losses in respective temperature ranges, it is difficult to dedicate mass loss in the range of 105 &#xb0;C&#x2013;850 &#xb0;C to a particular thermal event due to their potential overlaps. As shown in <xref ref-type="fig" rid="F13">Figure 13a</xref>, based on the derivative curve, TGA mass loss of the steel slag can be segmented into five temperature ranges. The mass loss in the isothermal segment at 105 &#xb0;C can be attributed to loosely adsorbed moisture in the sample. The mass loss ranging from 105 &#xb0;C to 304 &#xb0;C can be dedicated to the beginning of dehydration or dehydroxylation of schwertmannite, nacrite and some organic components that may be present (<xref ref-type="bibr" rid="B26">L&#xe1;zaro et al., 2022</xref>; <xref ref-type="bibr" rid="B3">Ben, 1997</xref>). In the temperature range of 304 &#xb0;C&#x2013;405 &#xb0;C, several possible overlaps between the dehydration of brucite and continued dehydration of schwertmannite should be expected (<xref ref-type="bibr" rid="B17">Harrison et al., 2013</xref>; <xref ref-type="bibr" rid="B26">L&#xe1;zaro et al., 2022</xref>; <xref ref-type="bibr" rid="B44">Siauciunas et al., 2023</xref>). Amara et al. observed two major dehydration derivative peaks of nacrite at 108 &#xb0;C and 245 &#xb0;C (<xref ref-type="bibr" rid="B3">Ben, 1997</xref>). The final dehydroxylation peak of nacrite was observed at 627 &#xb0;C. The brucite decomposition window can range from 315 &#xb0;C to 450 &#xb0;C (<xref ref-type="bibr" rid="B47">Turvey et al., 2022</xref>). The decomposition of Magnesite and brucite may or may not overlap with each other but can severely overlap with that of portlandite in the temperature range of &#x223c;400 &#xb0;C&#x2013;500 &#xb0;C (<xref ref-type="bibr" rid="B48">Villagr&#xe1;n-Zaccardi et al., 2017</xref>). For temperature ranges pertaining to CaCO<sub>3</sub> decomposition in the steel slag matrix (&#x223c;550 &#xb0;C-&#x223c;750 &#xb0;C in this case), simultaneous decomposition of schwertmannite, nacrite, magnesite and CaCO<sub>3</sub> should be expected. The loss of structural sulfate of schwertmannite occurs between 400 &#xb0;C and 700 &#xb0;C, centered at &#x223c;615 &#xb0;C (<xref ref-type="bibr" rid="B26">L&#xe1;zaro et al., 2022</xref>). The above discussion clarifies the role of presence of other components on CaCO<sub>3</sub> and MgCO<sub>3</sub> quantification in steel slag samples. Therefore, baseline correction is important for accurate determination of fresh carbonates. However, for carbonation studies, it is also important to ensure that the components potentially interfering with carbonate measurements are not undergoing carbonation.</p>
<fig id="F13" position="float">
<label>FIGURE 13</label>
<caption>
<p>TGA thermal decomposition mass loss and derivative curves; <bold>(a)</bold> raw steel slag; <bold>(b)</bold> raw and CaCO<sub>3</sub> dosed steel slag samples; <bold>(c)</bold> Comparison with pure lab grade CaCO<sub>3</sub>. Heating rate: 20 &#xb0;C/min; Atmosphere: N<sub>2</sub>.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g013.tif">
<alt-text content-type="machine-generated">Figure with three panels showing thermal analysis of different materials. Panel a shows weight percentage and derivative weight versus temperature, with curves for one sample, highlighting weight loss and peak changes. Panel b displays similar plots for four samples, with a legend identifying Steel Slag, MD9, MD10, and MD11, showing distinct thermal behavior among the samples. Panel c presents derivative weight versus temperature for these four samples plus lab grade calcium carbonate, where the lab grade CaCO3 shows a much higher peak near 800 degrees Celsius compared to other samples.</alt-text>
</graphic>
</fig>
<p>
<xref ref-type="fig" rid="F13">Figures 13b,c</xref> show the TGA decomposition curves of steel slag sample dosed with known amounts (&#x223c;10%, &#x223c;5% and &#x223c;2%) of lab-grade CaCO<sub>3</sub> and comparison of their derivatives with lab-grade CaCO<sub>3</sub>. It can be clearly observed that the decomposition temperature range of the same lab-grade CaCO<sub>3</sub> in the steel slag matrix shrinks as compared to the pure lab-grade CaCO<sub>3</sub>. The calculated onset, endset, and peak temperatures for the derivative curve of CaCO<sub>3</sub> dosed steel slag samples are also mentioned in <xref ref-type="table" rid="T7">Table 7</xref>. The span of temperature range of CaCO<sub>3</sub> decomposition in steel slag matrix varies from 130 &#xb0;C to 138 &#xb0;C whereas that of pure lab-grade CaCO<sub>3</sub> is &#x223c;243 &#xb0;C (<xref ref-type="sec" rid="s12">Supplementary Table A1</xref>). Additionally, the decomposition of CaCO<sub>3</sub> in the steel slag matrix was found to have onset temperature in the range of 611 &#xb0;C&#x2013;626 &#xb0;C whereas the pure lab-grade CaCO<sub>3</sub> had an onset temperature at around 593 &#xb0;C. This is similar to the results obtained in the case of mine tailings, suggesting the silicate matrices tend to slightly delay the onset of CaCO<sub>3</sub> decomposition.</p>
</sec>
<sec id="s4-5">
<label>4.5</label>
<title>Standardized protocol development and best practices for carbonate quantification</title>
<p>The quantification of carbonates requires more attention and needs to be revisited given the growth in number of accelerated carbonation studies in the last 2 decades. Most of the carbonation studies use TGA for carbonate quantification with assumptions that all or most of the mass losses in the approximate temperature range of &#x223c;500 &#xb0;C&#x2013;850 &#xb0;C are due to CaCO<sub>3</sub> decomposition which may not always be true. The temperature range of CaCO<sub>3</sub> decomposition is also dependent on the impurities present in the carbonated product which can have catalytic effects (e.g., MgO). TGA alone is insufficient for carbonate quantification, especially in the case of industrial waste that exhibits complex mineralogy. The focus of this study was on the characterization and evaluation of factors affecting carbonate quantification in relatively higher purity samples as well as heterogeneous matrices of industrial waste samples consisting of silicates. A variety of samples including mineralized CaCO<sub>3</sub>, steel slag, mine tailing, synthetic samples such as lab-grade CaCO<sub>3</sub>, MgCO<sub>3</sub>, amorphous silica, CaCO<sub>3</sub> dosed mine tailing and steel slag were analyzed. The CaCO<sub>3</sub> was dosed in different amounts (2, 5 and 10 wt%) in steel slag and mine tailing samples. The variation in CaCO<sub>3</sub> content did not have significant effect on the decomposition temperature levels. In general, the presence of impurities significantly lowered the endset temperature of CaCO<sub>3</sub> decomposition as shown in <xref ref-type="fig" rid="F14">Figure 14</xref> whereas the onset of decomposition was variably affected depending on the type of impurity. The TGA results revealed significant variation in the decomposition temperature range of CaCO<sub>3</sub> in the presence of different impurity types. It is worth noting that the decomposition temperature range of pure lab-grade CaCO<sub>3</sub> was widest, suggesting a kinetic component related to the sheer quantity of carbonates (&#x223c;99%). The presence of MgCO<sub>3</sub> resulted in a catalytic effect on the decomposition of lab-grade CaCO<sub>3</sub> whereas the industrial wastes (steel slag and mine tailing) delayed the onset decomposition temperature. The addition of amorphous silica gel along with MgCO<sub>3</sub> still had a slight catalytic effect on the onset of decomposition. These findings are crucial in terms of carbonate quantification and improve understanding on the influence of impurities on CaCO<sub>3</sub> decomposition temperature ranges.</p>
<fig id="F14" position="float">
<label>FIGURE 14</label>
<caption>
<p>Decomposition temperature range of lab-grade CaCO<sub>3</sub> in heterogeneous matrices. Heating rate: 20 &#xb0;C/min; Atmosphere: N<sub>2</sub>.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g014.tif">
<alt-text content-type="machine-generated">Horizontal bar chart comparing decomposition temperature ranges for various matrices such as mine tailing, steel slag, MgCO&#x2083; with SiO&#x2082;, MgCO&#x2083;, and lab grade CaCO&#x2083;. Mine tailings and steel slags show slightly delayed onset and reduced catalytic effect, while the change in endpoint temperature is illustrated, with lab grade CaCO&#x2083; decomposing at the highest temperatures. Temperature range spans from five hundred to eight hundred degrees Celsius.</alt-text>
</graphic>
</fig>
<p>The increasing focus on accelerated or natural carbonation studies has necessitated the development of a standardized protocol for quantification of carbonates, especially in complex and heterogeneous matrices. Guo <italic>et al.</italic> assessed the progress on carbonation of tailings and observed a four-fold increase in number of publications on carbonation of mine tailings (<xref ref-type="bibr" rid="B16">Guo et al., 2024</xref>). In addition to mine tailings, different types of slags, municipal solid waste incinerator residues, natural rocks, and other heterogenous materials have been utilized in various carbonation studies (<xref ref-type="bibr" rid="B10">Fang et al., 2024</xref>; <xref ref-type="bibr" rid="B39">Raza et al., 2022</xref>; <xref ref-type="bibr" rid="B38">Qin et al., 2022</xref>; <xref ref-type="bibr" rid="B28">Li et al., 2007</xref>; <xref ref-type="bibr" rid="B43">Sexsmith et al., 2003</xref>). However, there is a lack of publications and studies on precise quantification of carbonates in samples that often possess complex minerology coupled with wide ranges of impurities. Studies by Ferrara et al. and Kemp et al. are relevant to this study as they explored the quantification of carbonation using various methodologies (<xref ref-type="bibr" rid="B11">Ferrara et al., 2023</xref>; <xref ref-type="bibr" rid="B23">Kemp et al., 2022</xref>). The development of a standardized protocol will benefit the quantification of carbonates in carbonated products and ensure safe and durable concrete production that conform to required standards when they are used as SCM.</p>
<p>Based on our results, a generalized workflow was drafted for improved quantification of carbonates in the CO<sub>2</sub> mineralized samples (<xref ref-type="fig" rid="F15">Figure 15</xref>). The workflow highlights the importance of pre-characterization and utilization of analytical methods to identify and quantify the mineral phases that interfere with TGA measurement of CaCO<sub>3</sub>. Quantitative methods such as QXRD should be utilized when possible. However, for samples with amorphous mineral phases, the use of FTIR or organic elemental analyzer is recommended.</p>
<fig id="F15" position="float">
<label>FIGURE 15</label>
<caption>
<p>Recommended general workflow for carbonate quantification in mineralized CaCO<sub>3</sub> powders.</p>
</caption>
<graphic xlink:href="fenrg-14-1771825-g015.tif">
<alt-text content-type="machine-generated">Flowchart illustrating the analysis process for a mineralized powder sample: pre-characterization using XRD, FTIR, and organic elemental analyses, followed by identification of interfering phases. If interfering phases are present, quantification with QXRD precedes TGA; if absent, proceed directly to TGA.</alt-text>
</graphic>
</fig>
<p>Based on the characterization and carbonate quantification results obtained in this study, the following are the proposed best practices identified for calcium carbonate quantification in complex and heterogeneous matrices:<list list-type="bullet">
<list-item>
<p>Use of a fixed temperature range is not accurate for carbonate quantification. Temperature range of decomposition of lab-grade CaCO<sub>3</sub> varies with types of impurities and matrices.</p>
</list-item>
<list-item>
<p>A thorough characterization should be performed as the presence of minor components may artificially inflate carbonate quantification due to simultaneous decomposition.</p>
</list-item>
<list-item>
<p>For samples with complex mineralogy such as steel slag and mine tailing, the identification of components that decompose in the temperature range similar to CaCO<sub>3</sub> is important.</p>
</list-item>
<list-item>
<p>TGA, by itself, may be used for carbonate quantification of high purity CaCO<sub>3</sub> samples, as demonstrated by the quantification of mineralized CaCO<sub>3</sub> presented here. Whereas TGA is likely insufficient in properly quantifying complex mineralogical samples, such as carbonated steel slag or mine tailings. In some cases, Thermogravimetric Analyzer&#x2013;Mass Spectrometry (TGA-MS) or Total Inorganic Carbon (TIC) analyzer can provide results with better precision.</p>
</list-item>
<list-item>
<p>A baseline correction must be used for samples such as steel slag or mine tailing to avoid over-estimation of CaCO<sub>3</sub> since presence of decomposition/dehydroxylation of other components overlaps with CaCO<sub>3</sub> decomposition.</p>
</list-item>
</list>
</p>
</sec>
</sec>
<sec sec-type="conclusion" id="s5">
<label>5</label>
<title>Conclusion</title>
<p>This study focused on advancing robust carbonate quantification in CO<sub>2</sub> mineralized products with the presence of impurities. A variety of CO<sub>2</sub> mineralized samples from industry and academic partners were evaluated and compared against synthetic lab-grade samples. Biomineralized CaCO<sub>3</sub> powders were found to contain a different CaCO<sub>3</sub> polymorph (Vaterite) but exhibited a relatively low level of complexity compared to mineralized industrial waste samples in terms of carbonate quantification. The presence of vaterite did not appear to influence the onset decomposition temperature levels as has been observed by other researchers. However, carbonate measurement in bio-mineralized samples could be influenced by the presence of minor components. The effects of impurities on carbonate quantification were found to be significant and need to be considered as an important factor in carbonate quantification in the mineralized products. The presence of complex and heterogeneous matrices as found in steel slags and mine tailings can further complicate the quantification due to the possibility of several impurities dehydrating and decomposing in the similar temperature range as CaCO<sub>3</sub>. TGA results obtained in this study indicate that MgCO<sub>3</sub> has a catalytic effect on the onset of the CaCO<sub>3</sub> decomposition whereas amorphous SiO<sub>2</sub> slightly delayed the onset temperature. A similar effect was observed for industrial residue samples exhibiting a mix of silicate phases. Although more sophisticated instruments such as TGA-MS could improve the carbonate measurements, they are inaccessible to most of the scientific community and relevant industries (mostly dominated by startups). Thus, it becomes imperative to improve quantification of carbonates using more accessible and standard instruments such as TGA, XRD, and total carbon analyzer. The present study also attempts to provide important considerations and best practices for carbonate quantification using standard instruments while emphasizing the necessity to develop a standardized protocol.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s6">
<title>Data availability statement</title>
<p>The original contributions presented in the study are included in the article/<xref ref-type="sec" rid="s12">Supplementary Material</xref>, further inquiries can be directed to the corresponding author.</p>
</sec>
<sec sec-type="author-contributions" id="s7">
<title>Author contributions</title>
<p>VK: Conceptualization, Data curation, Investigation, Methodology, Writing &#x2013; original draft, Writing &#x2013; review and editing. KF: Data curation, Formal Analysis, Methodology, Validation, Writing &#x2013; review and editing. AV: Data curation, Formal Analysis, Investigation, Resources, Writing &#x2013; review and editing. AL: Data curation, Investigation, Resources, Validation, Writing &#x2013; review and editing. SB: Supervision, Writing &#x2013; review and editing. JH: Data curation, Funding acquisition, Supervision, Validation, Writing &#x2013; review and editing. GG: Conceptualization, Funding acquisition, Resources, Supervision, Validation, Writing &#x2013; review and editing. VU: Data curation, Formal Analysis, Investigation, Resources, Validation, Writing &#x2013; review and editing. KR: Conceptualization, Formal Analysis, Funding acquisition, Resources, Supervision, Validation, Writing &#x2013; review and editing.</p>
</sec>
<ack>
<title>Acknowledgements</title>
<p>The U.S. Government retains and the publisher, by accepting the article for publication, acknowledges that the U.S. Government retains a nonexclusive, paid-up, irrevocable, worldwide license to publish or reproduce the published form of this work, or allow others to do so, for U.S. Government purposes.</p>
</ack>
<sec sec-type="COI-statement" id="s9">
<title>Conflict of interest</title>
<p>Authors AV, AL, SB, and JH were employed by Prometheus Materials Inc.</p>
<p>The remaining author(s) declared that this work was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
<p>The author GG declared that they were an editorial board member of Frontiers at the time of submission. This had no impact on the peer review process and the final decision.</p>
</sec>
<sec sec-type="ai-statement" id="s10">
<title>Generative AI statement</title>
<p>The author(s) declared that generative AI was not used in the creation of this manuscript.</p>
<p>Any alternative text (alt text) provided alongside figures in this article has been generated by Frontiers with the support of artificial intelligence and reasonable efforts have been made to ensure accuracy, including review by the authors wherever possible. If you identify any issues, please contact us.</p>
</sec>
<sec sec-type="disclaimer" id="s11">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
<sec sec-type="supplementary-material" id="s12">
<title>Supplementary material</title>
<p>The Supplementary Material for this article can be found online at: <ext-link ext-link-type="uri" xlink:href="https://www.frontiersin.org/articles/10.3389/fenrg.2026.1771825/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fenrg.2026.1771825/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="DataSheet1.docx" id="SM1" mimetype="application/docx" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2178786/overview">Amin Shokrollahi</ext-link>, The University of Adelaide, Australia</p>
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<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/939763/overview">Rodrigo Castillo</ext-link>, Pontificia Universidad Cat&#xf3;lica de Chile, Chile</p>
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<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/3334563/overview">Niladri Shekhar Samanta</ext-link>, Presidency University Bangalore, India</p>
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