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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Chem.</journal-id>
<journal-title>Frontiers in Chemistry</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Chem.</abbrev-journal-title>
<issn pub-type="epub">2296-2646</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1085868</article-id>
<article-id pub-id-type="doi">10.3389/fchem.2022.1085868</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemistry</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Lead-vanadate sorbents for iodine trapping and their conversion into an iodoapatite-based conditioning matrix</article-title>
<alt-title alt-title-type="left-running-head">P&#xe9;n&#xe9;lope 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/fchem.2022.1085868">10.3389/fchem.2022.1085868</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>P&#xe9;n&#xe9;lope</surname>
<given-names>R.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Campayo</surname>
<given-names>L.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1988905/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Fournier</surname>
<given-names>M.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Le Gallet</surname>
<given-names>S.</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Gossard</surname>
<given-names>A.</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2080395/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Grandjean</surname>
<given-names>A.</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2123982/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>CEA</institution>, <institution>DES</institution>, <institution>ISEC</institution>, <institution>DE2D</institution>, <institution>Universit&#xe9; de Montpellier</institution>, <addr-line>Marcoule</addr-line>, <country>France</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>ICB</institution>, <institution>UMR 6303 CNRS-Universit&#xe9; Bourgogne Franche-Comt&#xe9;</institution>, <addr-line>Dijon</addr-line>, <country>France</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>CEA</institution>, <institution>DES</institution>, <institution>ISEC</institution>, <institution>DMRC</institution>, <institution>Universit&#xe9; de Montpellier</institution>, <addr-line>Marcoule</addr-line>, <country>France</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/1579483/overview">Dan Gregg</ext-link>, Australian Nuclear Science and Technology Organisation, Australia</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/381703/overview">Qingjiang Pan</ext-link>, Heilongjiang University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/620799/overview">Anna Shelyug</ext-link>, Institute of Solid State Chemistry, Russia</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: L. Campayo, <email>lionel.campayo@cea.fr</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Inorganic Chemistry, a section of the journal Frontiers in Chemistry</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>21</day>
<month>12</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>1085868</elocation-id>
<history>
<date date-type="received">
<day>31</day>
<month>10</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>12</day>
<month>12</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 P&#xe9;n&#xe9;lope, Campayo, Fournier, Le Gallet, Gossard and Grandjean.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>P&#xe9;n&#xe9;lope, Campayo, Fournier, Le Gallet, Gossard and Grandjean</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 terms.</p>
</license>
</permissions>
<abstract>
<p>New lead-vanadate based sorbents were synthesized with the aim to entrap and confine gaseous iodine in off-gas streams coming from reprocessing facilities of spent nuclear fuel. Their synthesis relies on the shaping of a lead-vanadate, lead sulfide and alginic acid mix as millimetric beads. These beads were calcined between 220&#xb0;C and 500&#xb0;C to remove organic alginic compounds template. However, according to the calcination temperature, lead sulfide could be partially oxidized, limiting iodine loading capacity. A compromise temperature between 290&#xb0;C and 350&#xb0;C was found to remove most of the alginic acid template and avoiding lead sulfide oxidation. These sorbents were tested for iodine trapping in static conditions at 60&#xb0;C. They performed well with a sorption capacity up to 155&#xa0;mg.g<sup>&#x2212;1</sup> by forming PbI<sub>2</sub>. Furthermore, these iodine-loaded sorbents could be easily converted into an iodine-containing lead-vanadate apatite matrix by spark plasma sintering. A dense sample was produced for a sintering temperature of 500&#xb0;C under 70&#xa0;MPa. Such a material could be suitable for radioactive iodine conditioning in deep geological disposal. Finally, lead-vanadate sorbents could provide an easy way to entrap and confine radioactive iodine from off-gas streams into a durable material within a few steps.</p>
</abstract>
<kwd-group>
<kwd>filter</kwd>
<kwd>iodine</kwd>
<kwd>off-gas</kwd>
<kwd>apatite</kwd>
<kwd>waste disposal</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Iodine-129 generated by nuclear industry is a long-lived nuclear waste with a half-life of 15.7 million years. For spent nuclear fuels intended to be reprocessed by the PUREX (plutonium uranium extraction) process (<xref ref-type="bibr" rid="B21">Sakurai et al., 1992</xref>; <xref ref-type="bibr" rid="B5">Bertelsen et al., 2022</xref>), this isotope is essentially met in off-gas streams produced during the acidic dissolution of fuel rods. There, it has to be managed to limit its atmospheric release. Possible management strategies considered for this waste are its isotopic dilution in seawater or its trapping on solid sorbents without downstream processing. Here, we consider another possibility relying on its storage in a deep geological disposal (<xref ref-type="bibr" rid="B27">Von Lensa et al., 2007</xref>). Such a management solution requires iodine incorporation into an inert conditioning matrix to ensure its retention. Iodoapatite Pb<sub>10</sub>(VO<sub>4</sub>)<sub>4.8</sub>(PO<sub>4</sub>)<sub>1.2</sub>I<sub>2</sub> is among promising matrices for this application (<xref ref-type="bibr" rid="B2">Audubert, 1995</xref>; <xref ref-type="bibr" rid="B18">Reiser et al., 2022</xref>). It can incorporate high iodine amounts (&#x3e;8&#xa0;wt.%) and can be consolidated into dense monoliths with densification rates higher than 95% (<xref ref-type="bibr" rid="B30">Yao et al., 2014</xref>; <xref ref-type="bibr" rid="B31">Yao et al., 2015</xref>). It also presents high chemical durability in pure water and groundwater (neutral to alkaline environments) and thus a strong iodine containment over time (<xref ref-type="bibr" rid="B9">Guy et al., 2002</xref>; <xref ref-type="bibr" rid="B32">Zhang et al., 2018</xref>; <xref ref-type="bibr" rid="B33">Zhang et al., 2019</xref>). The formation equation of iodoapatite from PbI<sub>2</sub> can be written as follows:<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:mn>3</mml:mn>
<mml:msub>
<mml:mrow>
<mml:mi>P</mml:mi>
<mml:mi>b</mml:mi>
</mml:mrow>
<mml:mn>3</mml:mn>
</mml:msub>
<mml:msub>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi>V</mml:mi>
<mml:mi>O</mml:mi>
</mml:mrow>
<mml:mn>4</mml:mn>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mn>1.6</mml:mn>
</mml:msub>
<mml:msub>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi>P</mml:mi>
<mml:mi>O</mml:mi>
</mml:mrow>
<mml:mn>4</mml:mn>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mn>0.4</mml:mn>
</mml:msub>
<mml:mo>&#x2b;</mml:mo>
<mml:msub>
<mml:mrow>
<mml:mi>P</mml:mi>
<mml:mi>b</mml:mi>
<mml:mi>I</mml:mi>
</mml:mrow>
<mml:mn>2</mml:mn>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mo>&#x2192;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mrow>
<mml:mi>P</mml:mi>
<mml:mi>b</mml:mi>
</mml:mrow>
<mml:mn>10</mml:mn>
</mml:msub>
<mml:msub>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi>V</mml:mi>
<mml:mi>O</mml:mi>
</mml:mrow>
<mml:mn>4</mml:mn>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mn>4.8</mml:mn>
</mml:msub>
<mml:msub>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi>P</mml:mi>
<mml:mi>O</mml:mi>
</mml:mrow>
<mml:mn>4</mml:mn>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mn>1.2</mml:mn>
</mml:msub>
<mml:msub>
<mml:mi>I</mml:mi>
<mml:mn>2</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>
</p>
<p>As a poorly soluble salt, PbI<sub>2</sub> can be considered as an intermediate reactant to form iodoapatite. However, in nuclear fuel reprocessing plants, iodine is primarily generated in a gaseous state, mainly as I<sub>2(g)</sub> (iodo-organic compounds can also be found) and, to the best of our knowledge, it is not possible to form an iodoapatite phase directly from I<sub>2(g)</sub>. Therefore, iodine trapping in a solid form is necessary before considering the formation of such a phase. Several solid sorbents were designed for iodine trapping such as activated carbon (<xref ref-type="bibr" rid="B10">Ho et al., 2019</xref>; <xref ref-type="bibr" rid="B26">Sun et al., 2019</xref>), graphene (<xref ref-type="bibr" rid="B22">Scott et al., 2015</xref>; <xref ref-type="bibr" rid="B25">Sun et al., 2018</xref>), Metal-Organic Frameworks (MOFs) (<xref ref-type="bibr" rid="B29">Xie et al., 2019</xref>; <xref ref-type="bibr" rid="B35">Zia et al., 2022</xref>), silver zeolites (<xref ref-type="bibr" rid="B4">Azambre et al., 2018</xref>; <xref ref-type="bibr" rid="B28">Wiechert et al., 2020</xref>), silver silica aerogel and many others. Despite the abundance of iodine sorbents (<xref ref-type="bibr" rid="B14">Muhire et al., 2022</xref>; <xref ref-type="bibr" rid="B17">P&#xe9;n&#xe9;lope et al., 2022</xref>; <xref ref-type="bibr" rid="B34">Zhang et al., 2022</xref>), none has the ability to form PbI<sub>2</sub> by reaction with I<sub>2(g)</sub>. Therefore, the synthesis of iodoapatite from existing sorbents is hardly achievable and would require either additional processing steps or, at least, a bubbling of off-gas streams into a solution containing a soluble salt of Pb<sup>2&#x2b;</sup>. The present work tries to overcome these issues by developing sorbents that can generate PbI<sub>2</sub> by reaction with I<sub>2(g)</sub> and that are directly convertible into an iodine-bearing apatitic phase while minimizing the number of handling steps from the trapping of iodine to its conditioning. For that purpose, lead sulfide was chosen as a compound able to react with I<sub>2(g)</sub> to form PbI<sub>2</sub> on the basis of previous studies (<xref ref-type="bibr" rid="B8">da Silva Filho et al., 2019</xref>; <xref ref-type="bibr" rid="B7">Chaudhuri and Acharya, 1982</xref>) whereas, the main phase of the sorbent was selected as a lead vanadate able to react with PbI<sub>2</sub> to form an iodine-bearing apatitic phase, namely Pb<sub>3</sub>(VO<sub>4</sub>)<sub>1.6</sub>(PO<sub>4</sub>)<sub>0.4</sub> (<xref ref-type="bibr" rid="B2">Audubert, 1995</xref>).</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>2 Materials and methods</title>
<sec id="s2-1">
<title>2.1 Synthesis of lead-vanadate sorbents</title>
<p>The synthesis of lead-vanadate sorbents is adapted from a previous templating procedure (<xref ref-type="bibr" rid="B16">P&#xe9;n&#xe9;lope et al., 2021</xref>). The reagents used for this synthesis include alginic acid sodium salt (Sigma Aldrich), PbS (&#x2265;99.9%, Sigma Aldrich), Pb(NO<sub>3</sub>)<sub>2</sub> (&#x2265;99.0%, Alfa Aesar) and Pb<sub>3</sub>(VO<sub>4</sub>)<sub>1.6</sub>(PO<sub>4</sub>)<sub>0.4</sub> (PbVP), the latter being synthesized by thermal treatment (1,000&#xb0;C for 1&#xa0;h) from a mix of PbO (&#x2265;98%, VWR), V<sub>2</sub>O<sub>5</sub> (&#x2265;99.95%, Sigma Aldrich) and NH<sub>4</sub>H<sub>2</sub>PO<sub>4</sub> (&#x2265;98%, VWR) with respective molar ratios of 3.0/0.8/0.4.</p>
<p>The first 250&#xa0;ml aqueous suspension was prepared with 6&#xa0;wt% of PbVP &#x2b; PbS with a respective molar ratio of 2:1. Alginic acid sodium salt was then gradually added until 2&#xa0;wt.% was reached and the suspension was stirred at room temperature for 4&#xa0;h under magnetic stirring. A second 250&#xa0;ml aqueous solution was prepared with lead nitrate at a concentration of 0.27&#xa0;mol.L<sup>&#x2212;1</sup> and stirred for 4&#xa0;h. The first suspension solution was then transferred by dripping into the second solution with a peristaltic pump REGLO Analog MS-4/8 (Ismatec<sup>&#xae;</sup>, Germany). A pipe of internal diameter of 2.79&#xa0;mm (Cole-Parmer<sup>&#xae;</sup>, USA) was used for the transfer and the speed was fixed to ensure the formation of individual droplets. As a consequence, small beads are obtained in solution because of a cationic substitution between Na<sup>&#x2b;</sup> (from alginic acid sodium) and Pb<sup>2&#x2b;</sup> (from Pb(NO<sub>3</sub>)<sub>2</sub>) resulting in the reticulation of alginate network (<xref ref-type="bibr" rid="B13">Lee and Mooney, 2012</xref>; <xref ref-type="bibr" rid="B1">Abasalizadeh et al., 2020</xref>). The obtained beads were retrieved by filtration, washed twice for 1&#xa0;hour in ultrapure water and once in ethanol. The beads were finally dried for 16&#xa0;h in an oven at 60&#xb0;C and calcined at various temperatures (220&#xb0;C&#x2013;500&#xb0;C) under air for 90&#xa0;min. The beads obtained at each of these synthesis steps are presented in <xref ref-type="fig" rid="F1">Figure 1</xref> and for a calcination temperature of 500&#xb0;C.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Pictures of the obtained beads calcined at 500&#xb0;C at each step of the synthesis.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g001.tif"/>
</fig>
</sec>
<sec id="s2-2">
<title>2.2 Iodine capture tests in static conditions</title>
<p>Iodine capture tests were carried out in static conditions in a hermetic perfluoroalkoxy jar (Savillex<sup>TM</sup>, USA) with 4.5&#xa0;g of solid iodine (I<sub>2</sub>, Acros Chimica) placed at the bottom. A known amount of sorbents (m<sub>s</sub>) (around 1.0&#xa0;g) was placed above a watch glass without contact with solid I<sub>2</sub>. The system was hermetically closed and put in an oven at 60&#xb0;C for 16&#xa0;h. These conditions were chosen based on thermodynamic considerations (<xref ref-type="bibr" rid="B19">Riley et al., 2020</xref>). Indeed, Gibbs&#x2019; free energy of formation of iodo-complexes (for Pb<sup>2&#x2b;</sup>) with I<sub>2(g)</sub> is favorable for such temperatures compared to the formation of oxo-complexes with O<sub>2(g)</sub>. The jar was then cooled to room temperature for 1&#xa0;h and the sorbents were weighed (m<sub>final</sub>) to determine the amount of trapped iodine (&#x394;m &#x3d; m<sub>final</sub>&#x2212;m<sub>s</sub>). The iodine sorption capacity Q<sub>e</sub> (in mg.g<sup>&#x2010;1</sup>) was calculated as follows:<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
<mml:msub>
<mml:mi>Q</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mo>&#x2206;</mml:mo>
<mml:mi mathvariant="normal">m</mml:mi>
</mml:mrow>
<mml:msub>
<mml:mi>m</mml:mi>
<mml:mi>s</mml:mi>
</mml:msub>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>
</p>
<p>This iodine sorption capacity Q<sub>e</sub> considers both chemisorbed and potentially physisorbed iodine. The physisorbed iodine amount was quantified by a gravimetric test after heating the sorbents in an oven at 150&#xb0;C for 1&#xa0;h. The mass loss is attributed to the physisorbed iodine amount.</p>
</sec>
<sec id="s2-3">
<title>2.3 Conversion of iodine-loaded sorbents by SPS</title>
<p>Iodine-loaded sorbents were converted by reactive sintering using Spark Plasma Sintering (SPS). 2.6&#xa0;g of iodine-loaded sorbents were introduced into a graphite mold (15&#xa0;mm inside diameter) to obtain a cylindrical matrix of 2&#xa0;mm in thickness and 15&#xa0;mm in diameter. Samples were pre-compacted at room temperature under 70&#xa0;MPa. Then, a pressure of 40&#xa0;MPa was applied for the whole heating at 500&#xb0;C for 5&#xa0;min (heating ramp of 50&#xb0;C min<sup>&#x2212;1</sup>). Such a temperature was chosen on the basis of the thermal stability of Pb<sub>10</sub>(VO<sub>4</sub>)<sub>4.8</sub>(PO<sub>4</sub>)<sub>1.2</sub>I<sub>2</sub> that can range between 400&#xb0;C and 500&#xb0;C according to the synthesis route (<xref ref-type="bibr" rid="B6">Campayo et al., 2009</xref>; <xref ref-type="bibr" rid="B12">Le Gallet et al., 2010</xref>; <xref ref-type="bibr" rid="B24">Suetsugu, 2014</xref>). In the case of a reactive sintering by SPS, this thermal stability was found to be up to 500&#xb0;C.</p>
</sec>
<sec id="s2-4">
<title>2.4 Characterization techniques</title>
<p>Field emission gun-scanning electron microscopy (FEG-SEM) was used to analyze the microstructure of the samples with a Zeiss Supra 55. Their chemical composition was also determined by energy dispersive X-ray spectroscopy (EDS) analyses with a Bruker AXS X-FlashDetector 4010 system. A probe current of 1&#xa0;nA with an accelerating voltage of 15&#xa0;kV at a working distance of 8.5&#xa0;mm was applied. All the samples were embedded in an epoxy resin, polished (diamond paste&#x2014;1&#xa0;&#xb5;m) and coated with a carbon layer of 10&#xa0;nm. Elemental quantification with an uncertainty of 26&#xa0;at% was determined from real standards spectra by using conventional PhiRhoZ correction. The collected data was processed with the ESPRIT2.0 software (Bruker&#x2122;, USA).</p>
<p>The crystalline phases were determined by X-ray diffraction measurements (XRD) with a X&#x2019;Pert PRO MPD PANalytical instrument (Bragg-Brentano geometry). A copper anode tube (Cu-K&#x3b1; radiation at 0.154056&#xa0;nm) working at 40&#xa0;kV and 40&#xa0;mA was used. Analyses were performed on powder samples at room temperature over a 2&#x3b8; range of 10&#x2013;90&#xb0;. Diffractograms were processed with the DIFFRAC.EVA V4.2 software (Bruker&#x2122;, USA) and the International Centre for Diffraction Data (ICDD) database PD4&#x2b; 2022 was used for identification purposes. Rietveld analysis was carried out with the FullProf Suite Toolbar software (January 2021 version) using the pseudo-Voigt function.</p>
<p>The densification rate of the obtained matrix after SPS conversion was calculated as the ratio between the hydrostatic density over the theoretical density. The theoretical density of the matrix was determined by helium pycnometry on powder samples with AccuPyc II 1340 device (Micromeritics<sup>&#xae;</sup>, USA). Samples were degassed under vacuum for 1&#xa0;h and weighed with an uncertainty of 10<sup>&#x2212;4</sup>&#xa0;g before the measurements. The hydrostatic density was determined using Archimedes method.</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Lead-vanadate synthesized sorbents</title>
<p>The obtained sorbents have the same visual appearance regardless of the applied calcination temperature (220, 290, 350, 400, 450 and 500&#xb0;C). An example of the obtained beads calcined at 500&#xb0;C is shown in <xref ref-type="fig" rid="F1">Figure 1</xref>. They are cohesive (based on a qualitative pinch test) and present a pseudo-spherical shape of 2&#xa0;mm in diameter. The mass losses measured as a function of the calcination temperature are gathered in <xref ref-type="table" rid="T1">Table 1</xref>. The increase of the calcination temperature induced a higher mass loss (from 14% to 21% of loss for 220&#xb0;C and 500&#xb0;C respectively) mainly related to the decomposition of the alginic template. Actually, these mass variations are the result of both the decomposition of alginic acid (Eq. <xref ref-type="disp-formula" rid="e3">3</xref>) and the potential oxidation of PbS (Eqs <xref ref-type="disp-formula" rid="e4">4</xref>, <xref ref-type="disp-formula" rid="e5">5</xref>) (a mass loss being indicative that the first one is the main contributor to this variation).<disp-formula id="e3">
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</disp-formula>
<disp-formula id="e4">
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<disp-formula id="e5">
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</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Mass losses as a function of the calcination temperature of the sorbents.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Calcination temperature (&#xb0;C)</th>
<th align="center">220</th>
<th align="center">290</th>
<th align="center">350</th>
<th align="center">400</th>
<th align="center">450</th>
<th align="center">500</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Mass loss (%)</td>
<td align="center">14</td>
<td align="center">18</td>
<td align="center">17</td>
<td align="center">18</td>
<td align="center">21</td>
<td align="center">21</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>XRD characterizations of the sorbents were carried out (<xref ref-type="fig" rid="F2">Figure 2</xref>) as a function of calcination temperature to identify the potential reactions occurring upon the thermal treatment. For calcination temperatures of 220, 290 and 350&#xb0;C, lead sulfide and Pb<sub>3</sub>(VO<sub>4</sub>)<sub>1.6</sub>(PO<sub>4</sub>)<sub>0.4</sub> (identified by comparing the obtained diffractogram with that of Robin et al. (<xref ref-type="bibr" rid="B20">Robin et al., 1999</xref>)) are present. The comparison of the relative intensities of the prominent peaks of PbVP and PbS (28.4&#xb0; and 30.1&#xb0; respectively) revealed an increase in the intensity of the first compared to the second as the calcination temperature rose. As the formation of PbVP during calcination is excluded (no supply of vanadium and phosphorus), the reactivity of PbS was considered to be at the origin of these fluctuations. Although no additional phase could be formally identified on the diffractograms, non-indexed peaks of small intensity were observed between 40&#xb0; and 42&#xb0;. This indicates the formation of at least one new phase, which can be ascribed to PbS reactivity. No amorphous signal corresponding to alginate (<xref ref-type="bibr" rid="B11">Jana et al., 2015</xref>) was visible on the X-Ray diffractograms showing that the residual alginate content is too low to be identified by XRD. However, according to the work of Soares et al. (<xref ref-type="bibr" rid="B23">Soares et al., 2004</xref>), alginate residues are probably present in the calcined sorbents (from 220&#xb0;C to 500&#xb0;C), the complete decomposition of alginate being obtained at around 520&#xb0;C.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>X-Ray diffractograms of <bold>(A)</bold> PbVP, PbS, lead-vanadate sorbents calcined at 220, 290, 350&#xb0;C and <bold>(B)</bold> calcined at 400, 450 and 500&#xb0;C.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g002.tif"/>
</fig>
<p>A similar X-ray diffractogram was observed for the sorbents calcined at 400&#xb0;C even if a newly formed metallic lead (Pb<sup>0</sup>) was also indexed. Its presence implies a reduction phenomenon during the calcination step. Indeed, lead is initially present as Pb<sup>2&#x2b;</sup> form within alginate, PbVP or PbS and, alginate being mainly composed of carbon, it could impose sufficiently reducing conditions to reduce some Pb<sup>2&#x2b;</sup> to metallic lead. For the sorbents calcined at 450&#xb0;C and 500&#xb0;C, Pb<sub>2</sub>(SO<sub>4</sub>)O, a Pb<sub>4</sub>(VO<sub>4</sub>)<sub>2</sub>O&#x2013;like phase, Pb<sup>0</sup>, PbVP and PbS are present. The existence of Pb<sub>2</sub>(SO<sub>4</sub>)O could result from the reaction between PbSO<sub>4</sub> (generated from PbS oxidation for these calcination temperatures (<xref ref-type="bibr" rid="B15">Nafees et al., 2017</xref>)) and PbO coming from the oxidation of metallic lead. In the case of Pb<sub>4</sub>(VO<sub>4</sub>)<sub>2</sub>O (where some vanadium is substituted by phosphorus), its presence can be explained by the reactivity between PbVP and PbO, the latter one coming from the oxidation of PbS (Pb<sub>3</sub>(VO<sub>4</sub>)<sub>1.6</sub>(PO<sub>4</sub>)<sub>0.4</sub> &#x2b; PbO &#x2192; Pb<sub>4</sub>(VO<sub>4</sub>)<sub>1.6</sub>(PO<sub>4</sub>)<sub>0.4</sub>O). The prominent peak of metallic lead at 34.1&#xb0; is less intense when the calcination temperature increases and this could therefore align with the hypothesis suggested for Pb<sub>2</sub>(SO<sub>4</sub>)O formation. An alternative to limit this PbS oxidation would be to carry out sorbents calcination under vacuum or with N<sub>2</sub> or Ar atmosphere. SEM characterizations of the sorbents calcined at 500&#xb0;C (<xref ref-type="fig" rid="F3">Figure 3</xref>) revealed the presence of carbonate residues derived from the decomposition of the alginic template. This confirms that, even after calcining at 500&#xb0;C, not all the carbon could be removed from the beads.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>X-Ray elemental mapping analysis of a cross-section of a sorbent bead calcined at 500&#xb0;C.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g003.tif"/>
</fig>
</sec>
<sec id="s3-2">
<title>3.2 Iodine sorption capacity of the sorbents</title>
<p>As an illustration, <xref ref-type="fig" rid="F4">Figure 4</xref> shows a change in the color of the sorbents calcined at 290&#xb0;C before and after exposure to I<sub>2(g)</sub>. This behavior was similar for all the sorbents. Their XRD characterizations after iodine exposure (<xref ref-type="fig" rid="F5">Figure 5</xref>) revealed the presence of a new phase of PbI<sub>2</sub>. The other phases are similar to those already identified before iodine exposure (<xref ref-type="fig" rid="F2">Figure 2</xref>). This demonstrates that these lead-vanadate sorbents can trap gaseous iodine by forming PbI<sub>2</sub> as expected. However, the remaining presence of PbS indicates that not all the active sites react with I<sub>2(g)</sub>, which is probably due to their inaccessibility to iodine. The formation of PbI<sub>2</sub> was accompanied by a mass gain calculated as sorption capacity using Eq. <xref ref-type="disp-formula" rid="e2">2</xref> and listed in <xref ref-type="table" rid="T2">Table 2</xref>.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Sorbents calcined at 290&#xb0;C before and after exposure to I<sub>2(g)</sub>.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g004.tif"/>
</fig>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>X-Ray diffractograms of lead-vanadate sorbents calcined at different temperatures after iodine capture.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g005.tif"/>
</fig>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Iodine sorption capacity of lead-vanadate sorbents.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Calcination temperature (&#xb0;C)</th>
<th align="center">Not calcined</th>
<th align="center">220</th>
<th align="center">290</th>
<th align="center">350</th>
<th align="center">400</th>
<th align="center">450</th>
<th align="center">500</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Sorption capacity (mg.g<sup>&#x2212;1</sup>)</td>
<td align="center">0</td>
<td align="center">20</td>
<td align="center">155</td>
<td align="center">120</td>
<td align="center">55</td>
<td align="center">85</td>
<td align="center">45</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>These results show a significant increase in the sorption capacity from a calcination temperature of 220&#xb0;C&#x2013;290&#xb0;C (20&#x2013;155&#xa0;mg.g<sup>&#x2212;1</sup> respectively) and then a decrease when the temperature still increases. It is worth noting that, after a thermal treatment at 150&#xb0;C for 1&#xa0;h, none of these sorbents showed a significant mass loss. This reveals a negligible contribution of physisorbed iodine to the measured sorption capacities. The minimum sorption capacity was reached for the sorbents calcined at 220&#xb0;C (20&#xa0;mg.g<sup>&#x2212;1</sup>). This can be explained by a significant presence of residual alginic template for such a calcination temperature, preventing access of gaseous iodine to the PbS active sites. This is consistent with the non-adsorption observed on the non-calcined sorbents due to the physical diffusion barrier constituted by alginate molecules. After calcination at 290&#xb0;C, the sorption capacity reached a maximum value of 155&#xa0;mg.g<sup>&#x2212;1</sup>. In this case, the decomposition of the alginic template seems sufficiently advanced to ensure good accessibility of iodine to the PbS active sites. By increasing the calcination temperature above 290&#xb0;C, the sorption capacity of the sorbents decreased from 120&#xa0;mg.g<sup>&#x2212;1</sup> (sorbents calcined at 350&#xb0;C) to 45&#xa0;mg.g<sup>&#x2212;1</sup> (sorbents calcined at 500&#xb0;C). This can be explained by the decrease in PbS content because of its oxidation at high temperature as well as by the formation of secondary phases that could prevent the accessibility of PbS particles to I<sub>2(g)</sub>.</p>
</sec>
<sec id="s3-3">
<title>3.3 Conversion of iodine-loaded sorbents into iodoapatite</title>
<p>Only the iodine-loaded sorbents calcined at 350&#xb0;C were converted by SPS. This sorbent was chosen because it has a high sorption capacity (120&#xa0;mg.g<sup>&#x2212;1</sup>), a satisfactory elimination rate of the alginic template and a PbVP/PbI<sub>2</sub> molar ratio greater than 3 (unlike sorbents calcined at 290&#xb0;C). This last characteristic is necessary to avoid over-stoichiometry of PbI<sub>2</sub> compared to proportions given by Eq. <xref ref-type="disp-formula" rid="e1">1</xref> for iodoapatite synthesis. In this way, it limits iodine loss above 400&#xb0;C, which could result from the melting of PbI<sub>2</sub> if it was not entirely converted into an iodine-containing apatitic phase. The PbVP/PbI<sub>2</sub> ratio was determined from the iodine sorption capacity where the content of PbI<sub>2</sub> was calculated for 1&#xa0;g of sorbent. The mass remaining to reach 1&#xa0;g of sorbent was entirely attributed to PbVP. Therefore, the residual PbS and the carbonate residues from alginate were not taken into account, which overestimated the PbVP content and then the PbVP/PbI<sub>2</sub> ratio. The obtained matrix after SPS treatment is shown in <xref ref-type="fig" rid="F6">Figure 6</xref>.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Matrix obtained after SPS conversion of iodine-loaded sorbents calcined at 350&#xb0;C <bold>(A)</bold> in front view and <bold>(B)</bold> in slice view. <bold>(C)</bold> Graphite tools used after the sorbents conversion.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g006.tif"/>
</fig>
<p>Visual examination of the matrix revealed a dense material without fracture and macroscopic porosities. From its theoretical density (6.18 &#xb1; 0.01) (measured by helium pycnometry on a finely ground piece) and its hydrostatic density (6.06 &#xb1; 0.06), a densification rate of 98.1 &#xb1; 1.2% was calculated. This confirms that the matrix was dense and without significant open porosity (densification rate &#x2265; 92%). Note that the graphite tools, initially black, became partially yellow on the upper surface after the SPS treatment. This color change was arbitrarily attributed to a slight iodine deposit even if no characterization was performed to formally confirm this point.</p>
<p>SEM characterizations (<xref ref-type="fig" rid="F7">Figure 7</xref>) of the obtained matrix indicate the presence of four phases. Among them, metallic lead (phase 1), PbS (phase 2) and PbVP (phase 4) are clearly identified from their chemical composition as determined by EDS. Metallic lead could come from the reduction of Pb<sup>2&#x2b;</sup> initially present in the calcined alginic template residues. Indeed, such a phase was also observed for sorbents treated within the same temperature range (500&#xb0;C) before gaseous iodine exposure (<xref ref-type="fig" rid="F2">Figure 2</xref>). For their own, PbS and PbVP phases were already present before SPS treatment and a part of them still remained after. If PbS and metallic lead can be clearly evidenced by XRD (<xref ref-type="fig" rid="F8">Figure 8</xref>), this is not the case for PbVP, probably because of a low content in the sample. As well as with the absence of PbI<sub>2</sub>, this means that a reaction involving PbI<sub>2</sub> and PbVP could happen but such a reaction did not lead to the formation of Pb<sub>10</sub>(VO<sub>4</sub>)<sub>4.8</sub>(PO<sub>4</sub>)<sub>1.2</sub>I<sub>2</sub> as this phase was not identified. However, from elemental quantification (<xref ref-type="fig" rid="F7">Figure 7</xref>), the chemical formula of the phase 3 can be written as Pb<sub>10.7</sub>(VO<sub>4</sub>)<sub>4.7</sub>(PO<sub>4</sub>)<sub>1.3</sub>I<sub>1.3</sub>O<sub>0.9</sub>, which is close to the composition of the targeted iodine-bearing apatite but that would exhibit a lesser iodine content. Nevertheless, assuming the presence of an iodine-bearing apatite, a Rietveld analysis of the X-Ray diffractogram was carried out to identify the crystalline phase(s) corresponding to the non-indexed peaks. The results are presented in <xref ref-type="fig" rid="F9">Figure 9</xref>.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>SEM pictures (BSE) <bold>(A)</bold> x34, <bold>(B)</bold> x200, <bold>(C)</bold> x3000 and <bold>(D)</bold> x6000 as well as EDS and elemental quantification of the matrix.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g007.tif"/>
</fig>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>X-Ray diffractogram of the matrix.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g008.tif"/>
</fig>
<fig id="F9" position="float">
<label>FIGURE 9</label>
<caption>
<p>Experimental (R<sub>exp</sub>) and simulated (R<sub>simu</sub>) X-Ray diffractograms of the matrix. Bragg positions of the several phases and intensity differences between R<sub>exp</sub> and R<sub>simu</sub> are also presented.</p>
</caption>
<graphic xlink:href="fchem-10-1085868-g009.tif"/>
</fig>
<p>The Rietveld refinement was performed by taking into consideration Pb<sup>0</sup> and PbS phases (Fm-3m space group) and assuming the presence of an iodoapatite with initial chemical formula of Pb<sub>9.85</sub>(VO<sub>4</sub>)<sub>4.8</sub>(PO<sub>4</sub>)<sub>1.2</sub>I<sub>1.7</sub> (P6<sub>3</sub>/m space group). Note that site occupancies for lead and iodine were allowed to vary. This apatite composition was derived from Audubert et al. work (<xref ref-type="bibr" rid="B3">Audubert et al., 1999</xref>), as measured for an iodoapatite of theoretical composition Pb<sub>9.85</sub>(VO<sub>4</sub>)<sub>6</sub>I<sub>1.7</sub> synthesized in sealed quartz tubes at 800&#xa0;&#xb0;C. Crystallographic data used for the refinement was retrieved from the "Crystallography Open Database&#x201d; (accession numbers: 1539418 for PbS&#x2014;1011119 for Pb<sup>0</sup>&#x2014;2008226 for Pb<sub>9.85</sub>(VO<sub>4</sub>)<sub>6</sub>I<sub>1.7</sub>). By comparing the experimental X-ray diffractogram with the simulated one, a good superposition is observed and Bragg factors of 16.370, 11.390 and 9.874 were obtained for Pb<sup>0</sup>, PbS and iodoapatite respectively. Such results confirmed the presence of an iodoapatite phase within the matrix. The work of Audubert et al. (<xref ref-type="bibr" rid="B2">Audubert, 1995</xref>) demonstrated that the substitution of OH<sup>&#x2212;</sup> groups for I<sup>&#x2212;</sup> groups within an apatite structure resulted in an increase in the parameter <italic>a</italic> and had a negligible impact on <italic>c</italic>. For the iodoapatite phase present in the obtained matrix, a value of 10.283&#xa0;&#xc5; for parameter <italic>a</italic> was calculated against 10.372 and 10.113&#xa0;&#xc5; for Pb<sub>10</sub>(VO<sub>4</sub>)<sub>4.8</sub>(PO<sub>4</sub>)<sub>1.2</sub>I<sub>2</sub> and Pb<sub>10</sub>(VO<sub>4</sub>)<sub>4.8</sub>(PO<sub>4</sub>)<sub>1.2</sub>(OH)<sub>2</sub> respectively (<xref ref-type="bibr" rid="B2">Audubert, 1995</xref>). By considering a linear relation between the parameter <italic>a</italic> and the substitution rate of I<sup>&#x2212;</sup> by OH<sup>&#x2212;</sup>, an under-stoichiometry in iodine of 33% within the obtained iodoapatite (phase 4 of <xref ref-type="fig" rid="F7">Figure 7</xref>) could be calculated which agrees well with elemental composition as determined by EDS. Such an under-stoichiometry could be explained by the initial PbVP/PbI<sub>2</sub> molar ratio that was slightly higher than the theoretical proportion given by Eq. <xref ref-type="disp-formula" rid="e1">1</xref>, as well as in a slight iodine volatilization (<xref ref-type="fig" rid="F6">Figure 6C</xref>). Actually, a lower thermal stability of such a kind of iodine&#x2013;deficient apatite (compared to an apatitic phase having the targeted composition) could be at the origin of a slight iodine volatilization by itself. This point should have to be investigated in a future work.</p>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>The synthesis of a new class of lead-vanadate based sorbents able to entrap gaseous iodine and directly convertible into iodoapatite matrix by reactive sintering was demonstrated here. The synthesis of the sorbents could be achieved by an easy liquid route using an alginic organic template to form solid beads of 2&#xa0;mm in diameter. Various calcination temperatures (220&#xb0;C&#x2013;500&#xb0;C) were applied to the beads to maximize alginate removal while limiting lead sulfide oxidation which is required to entrap gaseous iodine as PbI<sub>2</sub>. Iodine capture tests in static conditions at 60&#xb0;C indicated the highest sorption capacity of 155 and 120&#xa0;mg.g<sup>&#x2212;1</sup> for the sorbents calcined at 290&#xb0;C and 350&#xb0;C. No physisorbed iodine was detected and I<sub>2(g)</sub> was efficiently entrapped as PbI<sub>2</sub> form. After the SPS conversion of the iodine-loaded sorbents at 500&#xb0;C under 70&#xa0;MPa, a conditioning matrix containing an iodoapatite phase, without residual PbI<sub>2</sub>, was obtained. Such a material could be suitable for radioactive iodine conditioning in deep geological disposal. Even if more studies have to be carried out (role of dynamic conditions, influence of aging in a prototypic environment &#x2026;), this work hints for the first time the possibility for a sorbent to entrap gaseous iodine into PbI<sub>2</sub> form and to be directly converted into a conditioning matrix by reactive sintering with a low iodine volatilization.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s5">
<title>Data availability statement</title>
<p>The datasets presented in this study can be found in online repositories. The names of the repository/repositories and accession number(s) can be found below: <ext-link ext-link-type="uri" xlink:href="http://www.crystallography.net/cod/">http://www.crystallography.net/cod/</ext-link>- 2008226, 1011119, 1539418.</p>
</sec>
<sec id="s6">
<title>Author contributions</title>
<p>All authors listed have made a substantial, direct, and intellectual contribution to the work and approved it for publication.</p>
</sec>
<sec sec-type="COI-statement" id="s7">
<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="s8">
<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>
<ref-list>
<title>References</title>
<ref id="B1">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Abasalizadeh</surname>
<given-names>F.</given-names>
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