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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Energy Res.</journal-id>
<journal-title>Frontiers in Energy Research</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Energy Res.</abbrev-journal-title>
<issn pub-type="epub">2296-598X</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">809663</article-id>
<article-id pub-id-type="doi">10.3389/fenrg.2022.809663</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Energy Research</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Simulation-Assisted Determination of the Minimum Melting Temperature Composition of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl Salt Mixture for Next-Generation Molten Salt Thermal Energy Storage</article-title>
<alt-title alt-title-type="left-running-head">Villada et&#x20;al.</alt-title>
<alt-title alt-title-type="right-running-head">Molten Chlorides for Next-Generation CSP</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Villada</surname>
<given-names>Carolina</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1432159/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Ding</surname>
<given-names>Wenjin</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="corresp" rid="c001">
<sup>&#x2a;</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1546727/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Bonk</surname>
<given-names>Alexander</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Bauer</surname>
<given-names>Thomas</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>Institute of Engineering Thermodynamics</institution>, <institution>German Aerospace Center (DLR)</institution>, <addr-line>Stuttgart</addr-line>, <country>Germany</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>Institute of Engineering Thermodynamics</institution>, <institution>German Aerospace Center (DLR)</institution>, <addr-line>Cologne</addr-line>, <country>Germany</country>
</aff>
<author-notes>
<fn fn-type="edited-by">
<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1296743/overview">Chuan Li</ext-link>, Beijing University of Technology, China</p>
</fn>
<fn fn-type="edited-by">
<p>
<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/279489/overview">Terry David Humphries</ext-link>, Curtin University, Australia</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/839224/overview">Haochun Zhang</ext-link>, Harbin Institute of Technology, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Wenjin Ding, <email>wenjin.ding@dlr.de</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Process and Energy Systems Engineering, a section of the journal Frontiers in Energy Research</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>04</day>
<month>03</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>809663</elocation-id>
<history>
<date date-type="received">
<day>05</day>
<month>11</month>
<year>2021</year>
</date>
<date date-type="accepted">
<day>07</day>
<month>02</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 Villada, Ding, Bonk and Bauer.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Villada, Ding, Bonk and Bauer</copyright-holder>
<license xlink:href="http://creativecommons.org/licenses/by/4.0/">
<p>This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) 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&#x20;terms.</p>
</license>
</permissions>
<abstract>
<p>Molten chloride mixtures such as MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl are potential thermal energy storage (TES) materials and heat transfer fluids (HTFs) for next-generation concentrating solar power (CSP) systems due to their high operation temperatures (&#x3e;700&#xb0;C) and low costs. This ternary MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl salt mixture with a low material cost (&#x3c;0.35 $/kg) is a promising salt for high-temperature TES/HTF applications, for example, it could enable next-generation CSP plants to have significant power cycle efficiency and lower levelized cost of electricity (LCOE). In this study, the minimum melting temperature composition for the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl mixture was estimated by FactSage simulation, while the binary and ternary phase diagrams of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl salt system, including their phase transitions, were studied. Five different eutectic compositions of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl mixture from literature and simulations were selected to determine the minimum melting temperature composition by the differential scanning calorimetry technique. Results show agreement between experiments and simulations of the melting temperature and its composition. Hence, values of the exact and reliable minimum melting temperature and salt composition in mol% and wt% are given. Based on the determined melting temperature, the minimum operating temperature of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl is recommended according to the safety margin for CSP applications.</p>
</abstract>
<kwd-group>
<kwd>concentrating solar power</kwd>
<kwd>eutectic composition</kwd>
<kwd>heat transfer fluid</kwd>
<kwd>thermal energy storage</kwd>
<kwd>phase diagram</kwd>
</kwd-group>
<contract-sponsor id="cn001">Deutscher Akademischer Austauschdienst<named-content content-type="fundref-id">10.13039/501100001655</named-content>
</contract-sponsor>
</article-meta>
</front>
<body>
<sec id="s1">
<title>Introduction</title>
<p>Concentrating solar power (CSP) has been extensively investigated as a key technology for green electricity generation. A dispatchable form of CSP is the possibility to incorporate thermal energy storage (TES) using molten salts. In addition, for large-scale applications, this technology integrated with TES presents an economic advantage regarding manageability which implies lower demand-oriented levelized cost of electricity (LCOE) than volatile photovoltaic technology (<xref ref-type="bibr" rid="B16">Liu et&#x20;al., 2016</xref>). Molten nitrate salts, especially the so-called solar salt (NaNO<sub>3</sub>-KNO<sub>3</sub> 60&#x2013;40&#xa0;wt%), have been studied extensively for TES and heat transfer applications in the temperature range of 290&#x2013;565&#xb0;C (<xref ref-type="bibr" rid="B3">Bonk et&#x20;al., 2018</xref>). However, their thermal stability is limited by the decomposition above 565&#xb0;C. Thus, the research programs on next-generation CSP, for example, the SunShot Initiative of United&#x20;States Department of Energy (DOE) focus on higher operation temperature for better power cycle efficiency and major cost reduction using chloride salt mixtures comprising CaCl<sub>2</sub>, KCl, MgCl<sub>2</sub>, NaCl, and ZnCl<sub>2</sub> among others (<xref ref-type="bibr" rid="B8">Du et&#x20;al., 2017</xref>; <xref ref-type="bibr" rid="B24">Murphy et&#x20;al., 2019</xref>; <xref ref-type="bibr" rid="B33">Vidal and Klammer, 2019</xref>).</p>
<p>Low-cost molten chloride salts are some of the most promising high-temperature TES and heat transfer fluid (HTF) materials in next-generation CSP plants and other energy applications (e.g., nuclear molten salt reactor) due to, for example, their high thermal stability (&#x3e;800&#xb0;C) and low prices (&#x3c;0.35&#xa0;$/kg) (<xref ref-type="bibr" rid="B24">Murphy et&#x20;al., 2019</xref>; <xref ref-type="bibr" rid="B33">Vidal and Klammer, 2019</xref>; <xref ref-type="bibr" rid="B6">Ding and Bauer, 2021</xref>; <xref ref-type="bibr" rid="B34">Villada et&#x20;al., 2021</xref>). In next-generation CSP plants (see <xref ref-type="fig" rid="F1">Figure&#x20;1</xref>), the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl mixture can achieve higher power cycle efficiencies by using, for example, sCO<sub>2</sub> Brayton power cycle. In its potential high-temperature TES/HTF applications, this ternary salt presents different challenges which require a study from their initial composition and preparation to the final system integration.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Concept of next-generation CSP plant. Adapted from the study by <xref ref-type="bibr" rid="B34">Villada et&#x20;al., (2021</xref>).</p>
</caption>
<graphic xlink:href="fenrg-10-809663-g001.tif"/>
</fig>
<p>The exact and reliable data of the salt properties, such as melting temperature, are vital and essential for the design, construction, and operation of a TES system based on molten salts. However, due to the corrosivity and volatility of molten alkali chlorides at high temperatures and forming of salt hydrates (e.g., MgCl<sub>2</sub>&#x2219;6H<sub>2</sub>O), the experimental determination of thermodynamic properties, particularly at high temperatures, is complex. Thermodynamic simulation provides a practical way to assist the study on the thermophysical properties of molten chlorides. The salt properties, as well as the corrosion control, of molten chloride salts have been intensively studied in these years for TES/HTF applications. Two recent review articles from our group (<xref ref-type="bibr" rid="B6">Ding and Bauer, 2021</xref>; <xref ref-type="bibr" rid="B34">Villada et&#x20;al., 2021</xref>) are suggested for more details on thermophysical properties and corrosion control of MgCl<sub>2</sub>-containing molten chlorides. The initial studies on chloride salt properties were performed by DOE as molten salt coolants in nuclear reactors using experiments and thermodynamic simulation (<xref ref-type="bibr" rid="B18">Manohar et&#x20;al., 2010</xref>). In the early 1990s, experimental results of binary KCl&#x2013;MgCl<sub>2</sub>, KCl&#x2013;NaCl, and MgCl<sub>2</sub>&#x2013;NaCl were reviewed and published by Janz et&#x20;al. (<xref ref-type="bibr" rid="B30">Rowe et&#x20;al., 1972</xref>; <xref ref-type="bibr" rid="B12">Janz et&#x20;al., 1975</xref>). In the 1920s, the experimental MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary diagram has been presented by Scholich with a reported minimum melting temperature below 400&#xb0;C for the composition 32.5&#xa0;mol% NaCl, 18.5&#xa0;mol% KCl, and 49&#xa0;mol% MgCl<sub>2</sub> (<xref ref-type="bibr" rid="B31">Scholich, 1920</xref>). However, due to the experimental limitations at that time, the reported old minimum melting temperature and eutectic composition of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl need to be validated. Some research groups have carried out such validation <italic>via</italic> experiments and simulations, but discrepancies of minimum melting temperature compositions available in the literature (<xref ref-type="bibr" rid="B31">Scholich, 1920</xref>; <xref ref-type="bibr" rid="B11">J&#xe4;necke, 1950</xref>; <xref ref-type="bibr" rid="B27">Podlesnyak et&#x20;al., 1987</xref>; <xref ref-type="bibr" rid="B22">Mohan et&#x20;al., 2018a</xref>; <xref ref-type="bibr" rid="B33">Vidal and Klammer, 2019</xref>) are relatively high (about 2&#xa0;mol%). This may be due to different water contents in the salt mixture used in the experiment, particularly in hygroscopic MgCl<sub>2</sub>. Currently, our group published a review paper (<xref ref-type="bibr" rid="B34">Villada et&#x20;al., 2021</xref>) to recommend the most relevant salt properties besides minimum melting temperature for the design, construction, and operation of a TES/HTF system based on MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl. The properties include vapor pressure, heat capacity, density, thermal conductivity, and dynamic viscosity.</p>
<p>Since about 2015, there has been a strong renewed interest in the ternary MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl mixture as one of the most promising TES materials in next-generation CSP due to the abundance and low price of the single salts and relatively low melting temperature (<xref ref-type="bibr" rid="B22">Mohan et&#x20;al., 2018a</xref>; <xref ref-type="bibr" rid="B7">Ding et&#x20;al., 2018</xref>). The DLR started research with the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary mixture in 2015 (<xref ref-type="bibr" rid="B17">Maksoud and Bauer, 2015</xref>; <xref ref-type="bibr" rid="B7">Ding et&#x20;al., 2018</xref>), and the National Renewable Energy Laboratory (NREL) considered the binary mixture MgCl<sub>2</sub>&#x2013;KCl in 2016 (<xref ref-type="bibr" rid="B19">Mehos et&#x20;al., 2017</xref>). Several researchers from Savannah River National Lab (SRNL), Oak Ridge National Laboratory (ORNL), Argonne National Lab, and Australian National University (ANU) have also been exploring the ternary mixture for sensible and latent TES applications (<xref ref-type="bibr" rid="B32">Tian and Zhao, 2013</xref>; <xref ref-type="bibr" rid="B21">Mohan et&#x20;al., 2019</xref>). A new molten chloride salt test facility with the high-temperature molten chloride test loop is being designed by the Oak Ridge National Laboratory (ORNL) to demonstrate the viability of molten chlorides for power generation. In their most recent report (<xref ref-type="bibr" rid="B29">Robb et&#x20;al., 2019</xref>), the loop has a designed operating temperature of 725&#xb0;C with 20&#xa0;kg of salt mixture with an approximate composition of 21&#x2013;23&#xa0;mol% NaCl, 42&#x2013;43&#xa0;mol% KCl, and 34&#x2013;36&#xa0;mol% of MgCl<sub>2</sub>. The system considers the alloys Ha C-276/In 600 as the main structural materials, including corrosion monitoring and control. With the most recent advances in the area of molten chlorides, it can be demonstrated that this technology has a lot of application potential in next-generation CSP systems and nuclear molten salt reactors (MSRs) to generate electricity more efficiently and cost-effectively.</p>
<p>Melting temperature is a key parameter in the selection of a sensible TES or heat transfer fluid (HTF) since it determines the minimum operation temperature (partly the storage capacity) and system design to avoid salt freezing (<xref ref-type="bibr" rid="B3">Bonk et&#x20;al., 2018</xref>; <xref ref-type="bibr" rid="B33">Vidal and Klammer, 2019</xref>). For this reason, this study covers a relevant topic as it is the selection of the appropriate composition of the mixture which is one of the challenges associated with improving the properties of TES materials. The minimum melting temperature and eutectic composition of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary mixture were studied <italic>via</italic> FactSage thermodynamic simulation. Comparison with previous results and experimental validation with a differential scanning calorimeter (DSC) is presented after the study on the binary mixtures and their eutectic compositions as well as comparison with previous eutectic compositions reported in the literature. The current study will provide a reliable eutectic composition and minimum melting temperature of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl system as an important step of developing it for applications in the CSP industry and other energy industries. This composition can be used for the commercially used salt mixture, and the important properties such as heat capacity, viscosity, and thermal conductivity, can be better determined for engineering the salt for TES/HTF applications.</p>
</sec>
<sec id="s2">
<title>Materials and Experimental Methods</title>
<sec id="s2-1">
<title>Molten Salt Preparation</title>
<p>Five kinds of mixed chlorides were prepared by mixing KCl, NaCl, and MgCl<sub>2</sub> at different mixed ratios according to the literature and FactSage prediction. The purities of the chloride salts were &#x3e;99.9% for NaCl purchased from VWR BDH Chemicals, the purities of KCl and anhydrous MgCl<sub>2</sub> were both 99%, purchased from Acros Organics and Alfa Aesar, respectively. Since MgCl<sub>2</sub> may absorb H<sub>2</sub>O from the moisture under air, all salt mixtures were prepared inside a glove box under argon atmosphere (argon 5.0, 99.999%, O<sub>2</sub> &#x3c; 0.5&#xa0;ppm, H<sub>2</sub>O &#x3c; 10&#xa0;ppm). In addition, MgCl<sub>2</sub> was held at 150&#xb0;C for 18&#xa0;h to remove the most hydrated water and avoid hydration. Subsequently, around 5.0&#xa0;g of each salt mixture was prepared from stoichiometric weighing of each single chloride salt, followed by mixing and grinding for at least 20&#xa0;min manually to ensure homogenization. For the DSC analysis, around 10&#x2013;20&#xa0;mg sample was transferred into aluminum crucibles, a pierced lid was placed on top of the crucible, and then hermetically sealed with a sealing press from Netzsch. Then, the samples were carefully transported in a desiccator from the glovebox to the DSC apparatus to avoid atmospheric exposure and salt hydration.</p>
</sec>
<sec id="s2-2">
<title>Differential Scanning Calorimetry Measurements</title>
<p>Thermal analysis was carried out with a differential scanning calorimeter DSC 404 from Netzsch using aluminum crucibles under argon atmosphere (Argon 5.0), which was temperature-calibrated using Netzsch standard materials (In, Bi, Zn) in a temperature range of 100&#x2013;480&#xb0;C. Three heating and cooling runs from room temperature up to 480&#xb0;C were performed in total to avoid discrepancies in the melting temperature produced by the traces of hydrated MgCl<sub>2</sub>. The same heating and cooling rates (10&#xb0;C/min) were applied for all samples to allow qualitative comparison of the melting point between the samples and using an empty pan as a reference. The first cycle was used for the removal of traces of absorbed water followed by pre-melting and homogenization of the mixture. For the phase diagrams, the onset of the melting peak during heating was extracted since it represents the melting temperature of the salt mixture.</p>
</sec>
<sec id="s2-3">
<title>Thermodynamic Simulation With FactSage</title>
<p>FactSage is a commercial thermochemical databank system running in a Windows environment with the modules of Information, Database, Calculation, and manipulation (<ext-link ext-link-type="uri" xlink:href="https://www.factsage.com/">https://www.factsage.com/</ext-link>). This study utilizes version 7.2 of this software. Calculation is the main module of FactSage, which is based on the minimum Gibbs-free energy and CalPhaD (calculation of phase diagrams) theory to predict the equilibrium conditions of a system (<xref ref-type="bibr" rid="B2">Bale et&#x20;al., 2016</xref>). It includes the submodules such as Reaction, Predom, EpH, Equilib, Phase Diagram, and Optisage. FactSage gives access to databases of thermodynamic data for thousands of compounds, including hundreds of liquid and solid metals, liquid and solid oxides, molten and solid salts, and aqueous solutions. In this study, the submodule Phase Diagram was used to simulate the binary and ternary phase diagrams of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl salt system to support the experimental determination of the minimum melting temperature composition and melting temperature <italic>via</italic>&#x20;DSC.</p>
</sec>
</sec>
<sec id="s3">
<title>Result and Discussion of Binary Systems: KCl&#x2013;MgCl<sub>2</sub>, KCl&#x2013;NaCl, MgCl<sub>2</sub>&#x2013;NaCl</title>
<sec id="s3-1">
<title>Literature Review</title>
<p>There have been numerous studies to investigate the binary KCl&#x2013;MgCl<sub>2</sub>, KCl&#x2013;NaCl, and MgCl<sub>2</sub>&#x2013;NaCl mixtures and their compositions as candidate materials for thermal energy storage. The phase diagrams of the KCl&#x2013;MgCl<sub>2</sub> and MgCl<sub>2</sub>&#x2013;NaCl binary systems were experimentally studied by Menge (1911) (<xref ref-type="bibr" rid="B20">Menge, 1911</xref>) as well as the binary NaCl&#x2013;KCl by Kurnakow (1907) (<xref ref-type="bibr" rid="B14">Kurnakow and Zhemchuzhnui, 1907</xref>). Later, Janz, Scholich, and J&#xe4;necke (<xref ref-type="bibr" rid="B31">Scholich, 1920</xref>; <xref ref-type="bibr" rid="B11">J&#xe4;necke, 1950</xref>; <xref ref-type="bibr" rid="B12">Janz et&#x20;al., 1975</xref>; <xref ref-type="bibr" rid="B13">Janz and Tomkins, 1981</xref>) confirmed those results and discussed their thermophysical properties.</p>
<p>In the review of the literature published by Rowe et&#x20;al. (<xref ref-type="bibr" rid="B30">Rowe et&#x20;al., 1972</xref>), three eutectic compositions, namely, E<sub>1</sub>, E<sub>2</sub>, and E<sub>3</sub> are reported for the KCl&#x2013;MgCl<sub>2</sub> system. The compositions are 58&#xa0;mol% MgCl<sub>2</sub> for E<sub>1</sub> with a eutectic temperature of 470&#xb0;C, 36&#xa0;mol% MgCl<sub>2</sub> for E<sub>2</sub>, and 30&#xa0;mol% MgCl<sub>2</sub> for E<sub>3</sub> with a eutectic temperature of 431 and 430&#xb0;C, respectively. Polimeni et&#x20;al. (<xref ref-type="bibr" rid="B28">Polimeni et&#x20;al., 2018</xref>) as well as Xu et&#x20;al. (<xref ref-type="bibr" rid="B37">Xu et&#x20;al., 2018a</xref>) evaluated the KCl&#x2013;MgCl<sub>2</sub> binary mixture as the HTF in CSP solar tower configuration. In 2016, The National Renewable Energy Laboratory (NREL) considered the eutectic binary mixture MgCl<sub>2</sub>&#x2013;KCl (37.5&#x2013;62.5&#xa0;wt%, 32.0&#x2013;68.0&#xa0;mol%, melting temperature of 426&#xb0;C) as the TES/HTF in the next-generation CSP system.</p>
<p>For the KCl&#x2013;NaCl binary mixture, Kurnakow (<xref ref-type="bibr" rid="B14">Kurnakow and Zhemchuzhnui, 1907</xref>) found that this system forms a complete solid solution which unmixes at lower temperatures. The minimum temperature of 664&#xb0;C is located between 50&#x2013;51&#xa0;mol%&#x20;KCl.</p>
<p>The MgCl<sub>2</sub>-NaCl system was experimentally studied by Menge (<xref ref-type="bibr" rid="B20">Menge, 1911</xref>) with a eutectic temperature of 430&#xb0;C for a composition of 56&#xa0;mol% NaCl and later, Rowe et&#x20;al. (<xref ref-type="bibr" rid="B30">Rowe et&#x20;al., 1972</xref>) summarized previous results with a eutectic temperature of 450&#xb0;C for 62&#xa0;mol%&#x20;NaCl.</p>
</sec>
<sec id="s3-2">
<title>FactSage Thermodynamic Simulation</title>
<p>The binary phase diagrams of KCl&#x2013;MgCl<sub>2</sub>, KCl&#x2013;NaCl, and MgCl<sub>2</sub>&#x2013;NaCl have been estimated using the Phase Diagram module as well as the FTsalt database which contains data of the species Mg, K, and Na chloride, and the temperature range was chosen between 350&#x2013;850&#xb0;C. The binary phase diagrams of the KCl&#x2013;MgCl<sub>2</sub>, KCl&#x2013;NaCl, and MgCl<sub>2</sub>&#x2013;NaCl estimated with FactSage are shown in <xref ref-type="fig" rid="F2">Figure&#x20;2</xref>. The compositions mentioned here are all based on mole fractions.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Estimated phase diagrams for the binary <bold>(A)</bold> KCl&#x2013;MgCl<sub>2</sub>, <bold>(B)</bold> KCl&#x2013;NaCl, and <bold>(C)</bold> MgCl<sub>2</sub>&#x2013;NaCl systems from the FTsalt database using FactSage 7.2 thermodynamic software (<xref ref-type="bibr" rid="B10">FTSalt, 2019</xref>).</p>
</caption>
<graphic xlink:href="fenrg-10-809663-g002.tif"/>
</fig>
<p>According to FactSage 7.2, the KCl&#x2013;MgCl<sub>2</sub> system presents three eutectic temperatures at 472.72&#xb0;C, 428.96 &#xb0;C, and 422.68&#xb0;C with the intermetallic KMgCl<sub>3</sub>, K<sub>3</sub>Mg<sub>2</sub>Cl<sub>7</sub>, and K<sub>2</sub>MgCl<sub>4</sub> respectively, which are in good agreement with the literature data for E<sub>1</sub> and E<sub>2</sub> (<xref ref-type="bibr" rid="B30">Rowe et&#x20;al., 1972</xref>). Discrepancies in the eutectic temperature for E<sub>3</sub> are 8&#xb0;C lower than the previous reported temperature.</p>
<p>For the KCl&#x2013;NaCl binary mixture, the formation of the solid solution can be confirmed with a minimum temperature of 656.35&#xb0;C and a composition of 50.23&#xa0;mol% NaCl which is good agreement with the previous reported data from Rowe and Kurnakow (<xref ref-type="bibr" rid="B30">Rowe et&#x20;al., 1972</xref>; <xref ref-type="bibr" rid="B14">Kurnakow and Zhemchuzhnui, 1907</xref>).</p>
<p>The MgCl<sub>2</sub>-NaCl system exhibits eutectic temperature at 459.14&#xb0;C with a composition of 57&#xa0;mol% NaCl followed by the formation of the compounds NaMgCl<sub>3</sub> and Na<sub>2</sub>MgCl<sub>4</sub> that leads to a peritectic transformation at 465 and 474&#xb0;C, respectively.</p>
<p>Compared to the KCl&#x2013;NaCl and MgCl<sub>2</sub>&#x2013;NaCl phase diagrams, the KCl&#x2013;MgCl<sub>2</sub> has the lowest melting temperature of 422.68&#xb0;C. These three binary phase diagrams are important as the starting point of the evaluation of the ternary phase diagram.</p>
<p>These results of the binary chloride salt simulation include different eutectic, peritectic, and solid-solution compositions. Those invariant points are summarized in <xref ref-type="table" rid="T1">Table&#x20;1</xref> at 1&#xa0;atm in the temperature range 350&#x2013;850&#xb0;C.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Invariant reactions of KCl&#x2013;MgCl<sub>2</sub>, KCl&#x2013;NaCl, and MgCl<sub>2</sub>&#x2013;NaCl using FactSage thermodynamic simulation (L: Salt liquid).</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">System KCl&#x2013;MgCl<sub>2</sub>
</th>
<th align="center">Phase transition</th>
<th align="center">T (&#xb0;C)</th>
<th align="center">Composition (X<sub>mole</sub>)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">L&#x3c;&#x3d;&#x3e; MgCl<sub>2</sub>&#x2b;KMgCl<sub>3</sub>
</td>
<td align="left">Eutectic (E<sub>1</sub>)</td>
<td align="left">472.72</td>
<td align="center">0.4158 KCl&#x2013;0.5842 MgCl<sub>2</sub>
</td>
</tr>
<tr>
<td align="left">L &#x2b; KMgCl<sub>3</sub>&#x3c;&#x3d;&#x3e; K<sub>3</sub>Mg<sub>2</sub>Cl<sub>7</sub>
</td>
<td align="left">Peritectic (P<sub>1</sub>)</td>
<td align="center">440.09</td>
<td align="center">0.6253 KCl&#x2013;0.3747 MgCl<sub>2</sub>
</td>
</tr>
<tr>
<td align="left">L&#x3c;&#x3d;&#x3e; K<sub>3</sub>Mg<sub>2</sub>Cl<sub>7</sub>&#x2b;K<sub>2</sub>MgCl<sub>4</sub>
</td>
<td align="left">Eutectic (E<sub>2</sub>)</td>
<td align="center">428.96</td>
<td align="center">0.6541 KCl&#x2013;0.3459 MgCl<sub>2</sub>
</td>
</tr>
<tr>
<td align="left">L&#x3c;&#x3d;&#x3e; K<sub>2</sub>MgCl<sub>4</sub>&#x2b;KCl</td>
<td align="left">Eutectic (E<sub>3</sub>)</td>
<td align="center">422.68</td>
<td align="center">0.6987 KCl&#x2013;0.3013 MgCl<sub>2</sub>
</td>
</tr>
<tr>
<td align="left">
<bold>System KCl&#x2013;NaCl</bold>
</td>
<td align="center">
<bold>Phase transition</bold>
</td>
<td align="center">
<bold>T (&#xb0;C)</bold>
</td>
<td align="center">
<bold>Composition</bold> (<bold>X</bold>
<sub>
<bold>mole</bold>
</sub>)</td>
</tr>
<tr>
<td align="left">L&#x3c;&#x3d;&#x3e; NaCl &#x2b; KCl (ss)</td>
<td align="left">Solid solution (ss)</td>
<td align="left">656.35</td>
<td align="center">0.4977 KCl&#x2013;0.5023 NaCl</td>
</tr>
<tr>
<td align="left">
<bold>System MgCl</bold>
<sub>
<bold>2</bold>
</sub>
<bold>&#x2013;NaCl</bold>
</td>
<td align="left">
<bold>Phase transition</bold>
</td>
<td align="left">
<bold>T (&#xb0;C)</bold>
</td>
<td align="left">
<bold>Composition</bold> (<bold>X</bold>
<sub>
<bold>mole</bold>
</sub>)</td>
</tr>
<tr>
<td align="left">&#x2003;L &#x2b; NaCl&#x3c;&#x3d;&#x3e; Na<sub>2</sub>MgCl<sub>4</sub>
</td>
<td align="left">Peritectic (P<sub>1</sub>)</td>
<td align="left">474.95</td>
<td align="center">0.3662 MgCl<sub>2</sub>&#x2013;0.6338 NaCl</td>
</tr>
<tr>
<td align="left">&#x2003;L &#x2b; MgCl<sub>2</sub>&#x3c;&#x3d;&#x3e; NaMgCl<sub>3</sub>
</td>
<td align="left">Peritectic (P<sub>2</sub>)</td>
<td align="left">465.67</td>
<td align="center">0.4818 MgCl<sub>2</sub>&#x2013;0.5182 NaCl</td>
</tr>
<tr>
<td align="left">&#x2003;L&#x3c;&#x3d;&#x3e; Na<sub>2</sub>MgCl<sub>4</sub>&#x2b;NaMgCl<sub>3</sub>
</td>
<td align="left">Eutectic (E<sub>1</sub>)</td>
<td align="left">459.14</td>
<td align="center">0.4296 MgCl<sub>2</sub>&#x2013;0.5704 NaCl</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
</sec>
<sec id="s4">
<title>Result and Discussion of the Ternary System MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl</title>
<sec id="s4-1">
<title>Literature Review</title>
<p>In the first MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary diagram presented by Scholich in 1920 (<xref ref-type="bibr" rid="B31">Scholich, 1920</xref>), no ternary compounds but incongruently melting binary compounds, such as Na<sub>2</sub>MgCl<sub>4</sub>, and the congruently melting binary KMgCl<sub>3</sub> were reported. Below 480&#xb0;C, MgCl<sub>2</sub> is insoluble in the (NaCl &#x2b; KCl) solid solution. This was confirmed by Chartrand and Pelton (<xref ref-type="bibr" rid="B5">Chartrand and Pelton, 2001</xref>) who reported evidence of the solid solubility between Na<sub>2</sub>MgCl<sub>4</sub>&#x2013;K<sub>2</sub>MgCl<sub>4</sub> and NaMgCl<sub>3</sub>&#x2013;KMgCl<sub>3</sub>.</p>
<p>Further studies by Bradwell et&#x20;al. (<xref ref-type="bibr" rid="B4">Bradwell et&#x20;al., 2012</xref>) have used the composition 30&#xa0;mol% NaCl, 20&#xa0;mol% KCl, and 50&#xa0;mol% MgCl<sub>2</sub> as the molten electrolyte with a melting temperature of 396&#xb0;C. In a recent work, Li et&#x20;al. (<xref ref-type="bibr" rid="B15">Li et&#x20;al., 2017</xref>) investigated a variety of compositions with a minimum temperature between 383&#x2013;396&#xb0;C. Xu et&#x20;al. (<xref ref-type="bibr" rid="B36">Xu et&#x20;al., 2018b</xref>) experimentally studied different compositions of the ternary mixture in the range of 40&#x2013;50&#xa0;mol% MgCl<sub>2</sub>, in which the minimum temperature at 405&#xb0;C was found for a composition of 27.5&#xa0;mol% NaCl, 32.5&#xa0;mol% KCl, and 40&#xa0;mol% MgCl<sub>2</sub>. Mohan et&#x20;al. (<xref ref-type="bibr" rid="B22">Mohan et&#x20;al., 2018a</xref>; <xref ref-type="bibr" rid="B23">Mohan et&#x20;al., 2018b</xref>) experimentally validated the ternary mixture by DSC with a melting temperature of 387&#xb0;C for the composition reported by J&#xe4;necke and Nemecek (<xref ref-type="bibr" rid="B11">J&#xe4;necke, 1950</xref>; <xref ref-type="bibr" rid="B26">Nemecek et&#x20;al., 1978</xref>) of 45.4&#xa0;mol% MgCl<sub>2</sub>, 21.6&#xa0;mol% KCl, 33&#xa0;mol%&#x20;NaCl.</p>
<p>As suggested by Fink et&#x20;al. (<xref ref-type="bibr" rid="B36">Xu et&#x20;al., 2018b</xref>), the ternary system is incomplete in consequence of missing compounds in the binary systems. Variations of the salt compositions from different literature sources in this mixture lead to slight differences in the minimum melting temperature. For this reason, different liquid&#x2013;solid transitions have been reported with the solid phases NaMgCl<sub>3</sub>, KMgCl<sub>3</sub>, K<sub>3</sub>Mg<sub>2</sub>Cl<sub>7</sub>, Na<sub>2</sub>MgCl<sub>4</sub>, and K<sub>2</sub>MgCl<sub>4</sub> which should be considered in order to select the correct minimum temperature and eutectic composition since discrepancies are linked to incomplete identification of those compounds (<xref ref-type="bibr" rid="B1">Baek et&#x20;al., 2016</xref>).</p>
<p>According to Fink and Neil (<xref ref-type="bibr" rid="B9">Fink and Seifert, 1984</xref>; <xref ref-type="bibr" rid="B25">Neil et&#x20;al., 1965</xref>), as well as evidenced by the binary MgCl<sub>2</sub>&#x2013;NaCl and KCl&#x2013;MgCl<sub>2</sub> systems presented in <xref ref-type="fig" rid="F2">Figure&#x20;2</xref>, the presence of incongruently melting compounds leads to peritectic transformations and intermediate compounds. Podlesnyak and Orekhova (<xref ref-type="bibr" rid="B27">Podlesnyak et&#x20;al., 1987</xref>) have experimentally measured the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary system by conductivity techniques in which the ternary compound NaKMgCl<sub>4</sub> is reported and associated with a peritectic at 398&#xb0;C, and Chartrand et&#x20;al. (<xref ref-type="bibr" rid="B5">Chartrand and Pelton, 2001</xref>) measured the KMgCl<sub>3</sub>&#x2013;NaCl section in the ternary phase diagram shown in <xref ref-type="fig" rid="F3">Figure&#x20;3</xref>. The eutectic KMgCl<sub>3</sub>/NaCl mixture has the melting temperature of around 400&#xb0;C and 35&#x2013;45&#xa0;mol% NaCl (<xref ref-type="bibr" rid="B5">Chartrand and Pelton, 2001</xref>).</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>KMgCl<sub>3</sub>/NaCl section in the ternary phase diagram adapted from the study by Chartrand et&#x20;al. (<xref ref-type="bibr" rid="B5">Chartrand and Pelton, 2001</xref>). Two experimental points from the study by Podlesnyak et&#x20;al. (<xref ref-type="bibr" rid="B27">Podlesnyak et&#x20;al., 1987</xref>) and Fink et&#x20;al. (<xref ref-type="bibr" rid="B9">Fink and Seifert, 1984</xref>) are added to verify this phase diagram.</p>
</caption>
<graphic xlink:href="fenrg-10-809663-g003.tif"/>
</fig>
<p>The salt compositions and minimum melting temperature data from literature are summarized for comparison in <xref ref-type="table" rid="T2">Table&#x20;2</xref>. The discrepancies of minimum melting temperature compositions are relatively high (standard deviation of about 2&#xa0;mol% for each salt species), while the reported minimum melting temperatures are in the range of 385&#x2013;400&#xb0;C.</p>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Different compositions (in mol%) and minimum melting temperature data following the literature review with phase diagram measurements.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" colspan="2" align="left">Work</th>
<th colspan="3" align="center">Salt composition (mol%)</th>
<th rowspan="2" align="center">Reported minimum temperature (&#xb0;C)</th>
</tr>
<tr>
<th align="center">MgCl<sub>2</sub>
</th>
<th align="center">KCl</th>
<th align="center">NaCl</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">A</td>
<td align="left">Scholich (<xref ref-type="bibr" rid="B31">Scholich, 1920</xref>)</td>
<td align="center">49.0</td>
<td align="center">18.5</td>
<td align="center">32.5</td>
<td align="center">385</td>
</tr>
<tr>
<td align="left">B</td>
<td align="left">J&#xe4;necke, Mohan, Nemecek (<xref ref-type="bibr" rid="B11">J&#xe4;necke, 1950</xref>; <xref ref-type="bibr" rid="B26">Nemecek et&#x20;al., 1978</xref>; <xref ref-type="bibr" rid="B22">Mohan et&#x20;al., 2018a</xref>)</td>
<td align="center">45.4</td>
<td align="center">21.6</td>
<td align="center">33.0</td>
<td align="center">385&#x2013;387</td>
</tr>
<tr>
<td align="left">C</td>
<td align="left">Podlesnyak (<xref ref-type="bibr" rid="B27">Podlesnyak et&#x20;al., 1987</xref>)</td>
<td align="center">46.5</td>
<td align="center">22.2</td>
<td align="center">31.3</td>
<td align="center">&#x3c;400</td>
</tr>
<tr>
<td align="left">D</td>
<td align="left">Vidal et&#x20;al. (<xref ref-type="bibr" rid="B33">Vidal and Klammer, 2019</xref>)</td>
<td align="center">44.7</td>
<td align="center">25.8</td>
<td align="center">29.4</td>
<td align="center">385</td>
</tr>
<tr>
<td align="left">This&#x20;work</td>
<td align="left">Average &#xb1; Standard deviation</td>
<td align="center">
<bold>46.4&#x20;&#xb1; 1.6</bold>
</td>
<td align="center">
<bold>22.0&#x20;&#xb1; 2.6</bold>
</td>
<td align="center">
<bold>31.6&#x20;&#xb1; 1.4</bold>
</td>
<td align="center">
<bold>385 &#x2264; <italic>T</italic>
</bold>
<sub>
<bold>
<italic>m</italic>
</bold>
</sub> <bold>&#x3c; 400</bold>
</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s4-2">
<title>FactSage Thermodynamic Simulation</title>
<p>In this section, a thermodynamic simulation was performed using FactSage 7.2. The ternary phase diagram of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl have been estimated using the Phase Diagram module as well as the FTsalt database which contains data of the species Mg, K, and NaCl, and the temperature range was chosen between 350&#x2013;850&#xb0;C. This ternary phase diagram was estimated through the first melting temperature projection and, all compositions are referred on mole fractions.</p>
<p>According to FactSage simulation shown in <xref ref-type="fig" rid="F4">Figure&#x20;4</xref>, the zone in which the minimum temperature is located corresponds to a composition of 30.2&#xa0;mol% NaCl, 22.7&#xa0;mol% KCl, and 47.1&#xa0;mol% of MgCl<sub>2</sub> with a minimum temperature of 385.4&#xb0;C compared to the minimum temperature of 383&#xb0;C for 32.96&#xa0;mol% NaCl, 21.62&#xa0;mol% KCl, and 45.42&#xa0;mol% MgCl<sub>2</sub> previously reported by Mohan et&#x20;al. (<xref ref-type="bibr" rid="B22">Mohan et&#x20;al., 2018a</xref>; <xref ref-type="bibr" rid="B35">Villada et&#x20;al., 2019</xref>), as well as the average and standard deviation of the minimum melting temperature salt composition from <xref ref-type="table" rid="T2">Table&#x20;2</xref>. In addition, the eutectic composition is formed by the compounds KMgCl<sub>3</sub> &#x2b; NaMgCl<sub>3</sub> (36&#x2013;64&#xa0;mol%) according to our thermodynamic analysis. This implies that the theoretical exact eutectic composition of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl is 50&#x2013;18&#x2013;32&#xa0;mol%. In the KMgCl<sub>3</sub>/NaCl section from the ternary system, it has also been reported previously that the eutectic point at about 400&#xb0;C (<xref ref-type="bibr" rid="B9">Fink and Seifert, 1984</xref>; <xref ref-type="bibr" rid="B5">Chartrand and Pelton, 2001</xref>).</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Ternary phase diagram of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl obtained from FactSage 7.2 thermodynamic database in this work (lines: isothermal liquidus projections). The blue circle, which represents the average and standard deviation of the minimum melting temperature salt composition from <xref ref-type="table" rid="T2">Table&#x20;2</xref>, is also presented for comparison.</p>
</caption>
<graphic xlink:href="fenrg-10-809663-g004.tif"/>
</fig>
</sec>
<sec id="s4-3">
<title>Differential Scanning Calorimetry Measurements</title>
<p>Since there are limited experimental measurements for the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary system, more detailed discussion is useful in understanding the minimum melting temperature and composition of this mixture. The minimum melting temperature and related eutectic composition of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary system were validated by DSC experiments on the salt mixtures (Samples A&#x2013;D) from the literature listed in <xref ref-type="table" rid="T2">Table&#x20;2</xref> and the predicted salt mixture (Sample E) 30.2&#xa0;mol% NaCl, 22.7&#xa0;mol% KCl, and 47.1&#xa0;mol% of MgCl<sub>2</sub> in this work. The DSC heating and solidification curves of the five compositions are given in <xref ref-type="fig" rid="F5">Figure&#x20;5</xref>.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>DSC heating <bold>(A)</bold> and solidification <bold>(B)</bold> curves for the ternary MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl mixtures with the minimum melting temperature composition reported and listed&#x20;above.</p>
</caption>
<graphic xlink:href="fenrg-10-809663-g005.tif"/>
</fig>
<p>
<xref ref-type="fig" rid="F5">Figure&#x20;5</xref> (a) shows the melting temperature which is taken from the onset of the main endothermic peak at the heating cycle from the DSC curve, excluding the water losses in the first cycle. There is only one main melting peak at approximately 388.5&#xb0;C in all curves, as would be expected for a congruent melting compound. Moreover, an overlapping melting peak (Sample B, C, and E) or a plateau (Sample D) can be observed which implies that the salt mixture is not completely eutectic. A similar phenomenon can be observed in the solidification curves. The onset temperature of the main endothermic peak in the heating curve is about 3&#xb0;C higher than the predicted temperature value by FactSage. The end temperatures of phase transition during heating were between &#x223c;405 and 425&#xb0;C. The melting temperatures for the five salt compositions measured <italic>via</italic> DSC in this work are slightly higher than the melting temperatures reported in <xref ref-type="table" rid="T2">Table&#x20;2</xref>. The experimental results show that among these five salt compositions, the composition of Sample A (MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl 49.0&#x2013;18.5&#x2013;32.5&#xa0;mol%) is shown to be very close to the exact eutectic composition, as almost no secondary peak can be found in the heating and solidification curve. This also agrees with the fact that the composition of Sample A is closer to the theoretical exact eutectic composition.</p>
</sec>
<sec id="s4-4">
<title>Discussion</title>
<p>The melting temperature is a key parameter in the development of next-generation molten chloride salts, and it is represented by the onset of the DSC melting peak for a minimum melting temperature or eutectic mixture. From previous experience in our group with molten nitrate salts, the melting temperature of minimum melting temperature compositions can be successfully determined by differential scanning calorimetry&#x2014;DSC (e.g., ASTM E794 (<xref ref-type="bibr" rid="B3">Bonk et&#x20;al., 2018</xref>)). For mixtures with a melting range, the liquids temperature is relevant. A simple endset or peak maximum measurement as reported by some authors is misleading due to the influence of heating rates, sample mass, and composition (<xref ref-type="bibr" rid="B38">Yu-ting et&#x20;al., 2017</xref>). Overall, the minimum operating temperature of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary system for sensible TES applications should not exceed 420&#xb0;C assuming a melting temperature of about 390&#xb0;C and the recommended safety margin of 30&#xb0;C for CSP applications (<xref ref-type="bibr" rid="B3">Bonk et&#x20;al., 2018</xref>). It can also be seen from this work that the composition values for the minimum melting temperature are usually referred to compositions of 44.7&#x2013;49&#xa0;mol% MgCl<sub>2</sub>, 18.5&#x2013;25.8&#xa0;mol% KCl, and 29.4&#x2013;33&#xa0;mol%&#x20;NaCl.</p>
<p>The melting temperatures of the ternary MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl system with different compositions, including this work, are listed in <xref ref-type="table" rid="T3">Table&#x20;3</xref>. All onset values are mostly around 388.40&#x20;&#xb1; 0.55&#xb0;C. The variations of the DSC liquidus temperature for the five different ternary mixtures at 10&#xa0;K/min are shown in <xref ref-type="fig" rid="F6">Figure&#x20;6</xref>, in which the influence of each single chloride from the ternary mixture is notable. Both NaCl and MgCl<sub>2</sub> contribute to a decrease in the liquidus temperature, whereas the KCl content increases the liquidus temperature. The results confirm the main conclusion in the last subsection that the composition of Sample A (MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl 49.0&#x2013;18.5&#x2013;32.5&#xa0;mol%), which has the highest MgCl<sub>2</sub> content and lowest KCl content, is closer to the exact eutectic composition.</p>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Comparison of salt compositions and melting temperatures of the studied five MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary salt mixtures experimentally obtained by DSC at 10&#xb0;C/min heating rate. The error of the measured temperatures is the standard deviation of three different measurements.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th colspan="4" align="left">Salt composition (mol%)</th>
<th rowspan="2" align="center">Reported or predicted Temp. (&#xb0;C)</th>
<th rowspan="2" align="center">Onset Temp. (&#xb0;C)</th>
<th rowspan="2" align="center">End Temp. (&#xb0;C) at 10&#xa0;K/min</th>
</tr>
<tr>
<th align="left"/>
<th align="center">MgCl<sub>2</sub>
</th>
<th align="center">KCl</th>
<th align="center">NaCl</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">A (<xref ref-type="bibr" rid="B31">Scholich, 1920</xref>)</td>
<td align="char" char=".">49.0</td>
<td align="char" char=".">18.5</td>
<td align="char" char=".">32.5</td>
<td align="center">385</td>
<td align="char" char="plusmn">388.20&#x20;&#xb1; 0.14</td>
<td align="char" char="plusmn">404.9&#x20;&#xb1; 0.14</td>
</tr>
<tr>
<td align="left">B (<xref ref-type="bibr" rid="B11">J&#xe4;necke, 1950</xref>; <xref ref-type="bibr" rid="B26">Nemecek et&#x20;al., 1978</xref>; <xref ref-type="bibr" rid="B22">Mohan et&#x20;al., 2018a</xref>)</td>
<td align="char" char=".">45.4</td>
<td align="char" char=".">21.6</td>
<td align="char" char=".">33</td>
<td align="center">385&#x2013;387</td>
<td align="char" char="plusmn">388.33&#x20;&#xb1; 0.21</td>
<td align="char" char="plusmn">410.55&#x20;&#xb1; 0.78</td>
</tr>
<tr>
<td align="left">C (<xref ref-type="bibr" rid="B27">Podlesnyak et&#x20;al., 1987</xref>)</td>
<td align="char" char=".">46.5</td>
<td align="char" char=".">22.2</td>
<td align="char" char=".">31.3</td>
<td align="center">400</td>
<td align="char" char="plusmn">388.47&#x20;&#xb1; 0.06</td>
<td align="char" char="plusmn">411.17&#x20;&#xb1; 2.57</td>
</tr>
<tr>
<td align="left">D (<xref ref-type="bibr" rid="B33">Vidal and Klammer, 2019</xref>)</td>
<td align="char" char=".">44.7</td>
<td align="char" char=".">25.8</td>
<td align="char" char=".">29.4</td>
<td align="center">385</td>
<td align="char" char="plusmn">388.45&#x20;&#xb1; 0.07</td>
<td align="char" char="plusmn">426.35&#x20;&#xb1; 0.92</td>
</tr>
<tr>
<td align="left">E (This work)</td>
<td align="char" char=".">47.1</td>
<td align="char" char=".">22.7</td>
<td align="char" char=".">30.2</td>
<td align="center">385.4</td>
<td align="char" char="plusmn">388.55&#x20;&#xb1; 0.07</td>
<td align="char" char="plusmn">415.90&#x20;&#xb1; 0.14</td>
</tr>
</tbody>
</table>
</table-wrap>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Determined onset and liquidus at 10&#xa0;K/min depending on <bold>(A)</bold> NaCl, <bold>(B)</bold> MgCl<sub>2</sub>, and <bold>(C)</bold> KCl concentration of DSC measurements for five different ternary mixtures. <bold>(D)</bold> Detailed amplified triangle section.</p>
</caption>
<graphic xlink:href="fenrg-10-809663-g006.tif"/>
</fig>
</sec>
</sec>
<sec id="s5">
<title>Summary and Conclusions</title>
<p>This study investigated the binary and ternary phase diagrams of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl system using literature data and FactSage simulation and own DSC measurements in order to determine the minimum melting temperature of the MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl ternary salt. This mixture is relevant for high temperature TES for next-generation CSP systems.</p>
<p>In this study, five different compositions of the ternary MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl salt mixture from literature and simulation of this study have been synthesized in an inert atmosphere (i.e.,&#x20;water impurity in the salt mixtures is neglectable) and tested according to the previous reported compositions, and their experimental melting temperatures were determined by the DSC technique.</p>
<p>After detailed analysis of literature, FactSage simulation and own DSC measurements, a minimum melting composition of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl 49.0&#x2013;18.5&#x2013;32.5&#xa0;mol% or 58.7&#x2013;17.4&#x2013;23.9&#xa0;wt% with the experimental melting temperature of 388.5&#xb0;C is recommended. In addition, the phase transition that describes this eutectic composition is given by the composition KMgCl<sub>3</sub> &#x2b; NaMgCl<sub>3</sub> (36&#x2013;64&#xa0;mol%). This implies that the theoretical exact eutectic composition of MgCl<sub>2</sub>&#x2013;KCl&#x2013;NaCl is 50&#x2013;18&#x2013;32&#xa0;mol%, which agrees very well with the recommended composition. Based on these results, the minimum recommended operating temperature for high-temperature TES is 420&#xb0;C (more than 30&#xb0;C higher than the melting temperature). However, material cost aspects and larger safety margins may lead to other salt compositions (e.g., less MgCl<sub>2</sub> and more NaCl in salt mixture) and operating temperatures higher than 420&#xb0;C regarding the overall TES costs. Moreover, as the salt composition and melting temperature can be changed (i.e.,&#x20;shift of salt composition) by the by-reactions of the salt with impurities in salt or gas atmosphere during the use, monitoring of salt health is suggested in order to avoid inconveniences such as salt freezing.</p>
</sec>
</body>
<back>
<sec id="s6">
<title>Data Availability Statement</title>
<p> The simulation details have been added to the article. Further inquiries can be directed to the corresponding author.</p>
</sec>
<sec id="s7">
<title>Author Contributions</title>
<p>CV: conceptualization, investigation, writing&#x2013;original draft, preparation, and visualization. WD: conceptualization, investigation, writing&#x2013;original draft, preparation, visualization, review and editing, and revision. AB: Writing&#x2013;review and editing. TB: Writing&#x2013;review and editing and funding acquisition.</p>
</sec>
<sec id="s8">
<title>Funding</title>
<p>This research has been performed within the DLR-DAAD fellowship program (Grant number 91716495), which is funded by German Academic Exchange Service (DAAD) and German Aerospace Center (DLR).</p>
</sec>
<sec sec-type="COI-statement" id="s9">
<title>Conflict of Interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s10">
<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>
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