Reaction mechanisms underpinning the removal of Cs from simulated Cs-contaminated ash during thermal treatment with NaCl or KCl

•Vaporization of Cs in ash during thermal treatment with NaCl or KCl was investigated.•Interactions between Cs and Cl-bearing solid species were responsible for Cs vaporization.•An N2 atmosphere facilitated the vaporization of Cs relative to an air atmosphere. The vaporization mechanism of cesium (C...

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Veröffentlicht in:Fuel (Guildford) 2021-04, Vol.289, p.119905, Article 119905
Hauptverfasser: Jiao, Facun, Wu, Chengli, Liu, Tao, Li, Hanxu, Dong, Zhongbing, Ninomiya, Yoshihiko
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container_issue
container_start_page 119905
container_title Fuel (Guildford)
container_volume 289
creator Jiao, Facun
Wu, Chengli
Liu, Tao
Li, Hanxu
Dong, Zhongbing
Ninomiya, Yoshihiko
description •Vaporization of Cs in ash during thermal treatment with NaCl or KCl was investigated.•Interactions between Cs and Cl-bearing solid species were responsible for Cs vaporization.•An N2 atmosphere facilitated the vaporization of Cs relative to an air atmosphere. The vaporization mechanism of cesium (Cs) in simulated Cs-contaminated ash during thermal treatment with the addition of NaCl or KCl was systemically examined in a laboratory-scale horizontal electrical-heating furnace. A thermodynamic equilibrium calculation was performed to predict the distribution of Cs and Cl in the solid and gas phases under different experimental conditions. The results indicated that Cs vaporized following heat treatment of the simulated ash with the addition of NaCl or KCl. The vaporization ratio of Cs increased as the reaction temperature. As the content of NaCl or KCl was increased, the vaporization ratio also increased at > 1000 °C; whereas, it initially increased but then decreased at 900 °C. Both NaCl and KCl underwent direct vaporization and decomposition via chemical reactions with silicate/aluminosilicates in the ash, thus releasing HCl/Cl2. The interactions between Cs and solid Cl-bearing species (e.g. NaCl, Na2AlCl6, and KCl) formed CsCl and were responsible for the vaporization of Cs. Nevertheless, the release of HCl/Cl2 from the decomposition of NaCl and KCl had an insignificant effect on the vaporization of Cs. Compared to an air atmosphere, N2 facilitated the vaporization of Cs because the vaporization and/or decomposition of NaCl, Na2AlCl6, and KCl were delayed under the N2 atmosphere, which in turn enhanced the chlorination of Cs. By comparing the effect of adding NaCl, KCl, CaCl2, or MgCl2 on the vaporization of Cs, alkali chlorides (NaCl and KCl) were found to exhibit the best performance.
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The vaporization mechanism of cesium (Cs) in simulated Cs-contaminated ash during thermal treatment with the addition of NaCl or KCl was systemically examined in a laboratory-scale horizontal electrical-heating furnace. A thermodynamic equilibrium calculation was performed to predict the distribution of Cs and Cl in the solid and gas phases under different experimental conditions. The results indicated that Cs vaporized following heat treatment of the simulated ash with the addition of NaCl or KCl. The vaporization ratio of Cs increased as the reaction temperature. As the content of NaCl or KCl was increased, the vaporization ratio also increased at &gt; 1000 °C; whereas, it initially increased but then decreased at 900 °C. Both NaCl and KCl underwent direct vaporization and decomposition via chemical reactions with silicate/aluminosilicates in the ash, thus releasing HCl/Cl2. The interactions between Cs and solid Cl-bearing species (e.g. NaCl, Na2AlCl6, and KCl) formed CsCl and were responsible for the vaporization of Cs. Nevertheless, the release of HCl/Cl2 from the decomposition of NaCl and KCl had an insignificant effect on the vaporization of Cs. Compared to an air atmosphere, N2 facilitated the vaporization of Cs because the vaporization and/or decomposition of NaCl, Na2AlCl6, and KCl were delayed under the N2 atmosphere, which in turn enhanced the chlorination of Cs. By comparing the effect of adding NaCl, KCl, CaCl2, or MgCl2 on the vaporization of Cs, alkali chlorides (NaCl and KCl) were found to exhibit the best performance.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2020.119905</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Aluminosilicates ; Aluminum silicates ; Ashes ; Atmosphere ; Calcium chloride ; Cesium ; Cesium vaporization ; Chemical reactions ; Decomposition ; Decomposition reactions ; Heat treatment ; Heat treatments ; Heating furnaces ; Hydrogen chloride ; Incineration ash ; KCl ; Magnesium chloride ; NaCl ; Potassium chloride ; Reaction mechanisms ; Simulation ; Sodium chloride ; Thermal treatment ; Thermodynamic equilibrium ; Vapor phases ; Vaporization</subject><ispartof>Fuel (Guildford), 2021-04, Vol.289, p.119905, Article 119905</ispartof><rights>2020 Elsevier Ltd</rights><rights>Copyright Elsevier BV Apr 1, 2021</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c328t-824d1373825c9939e708be0242b28658a02197788b7c6bde037a8dabe116f4e43</citedby><cites>FETCH-LOGICAL-c328t-824d1373825c9939e708be0242b28658a02197788b7c6bde037a8dabe116f4e43</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.fuel.2020.119905$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3536,27903,27904,45974</link.rule.ids></links><search><creatorcontrib>Jiao, Facun</creatorcontrib><creatorcontrib>Wu, Chengli</creatorcontrib><creatorcontrib>Liu, Tao</creatorcontrib><creatorcontrib>Li, Hanxu</creatorcontrib><creatorcontrib>Dong, Zhongbing</creatorcontrib><creatorcontrib>Ninomiya, Yoshihiko</creatorcontrib><title>Reaction mechanisms underpinning the removal of Cs from simulated Cs-contaminated ash during thermal treatment with NaCl or KCl</title><title>Fuel (Guildford)</title><description>•Vaporization of Cs in ash during thermal treatment with NaCl or KCl was investigated.•Interactions between Cs and Cl-bearing solid species were responsible for Cs vaporization.•An N2 atmosphere facilitated the vaporization of Cs relative to an air atmosphere. The vaporization mechanism of cesium (Cs) in simulated Cs-contaminated ash during thermal treatment with the addition of NaCl or KCl was systemically examined in a laboratory-scale horizontal electrical-heating furnace. A thermodynamic equilibrium calculation was performed to predict the distribution of Cs and Cl in the solid and gas phases under different experimental conditions. The results indicated that Cs vaporized following heat treatment of the simulated ash with the addition of NaCl or KCl. The vaporization ratio of Cs increased as the reaction temperature. As the content of NaCl or KCl was increased, the vaporization ratio also increased at &gt; 1000 °C; whereas, it initially increased but then decreased at 900 °C. Both NaCl and KCl underwent direct vaporization and decomposition via chemical reactions with silicate/aluminosilicates in the ash, thus releasing HCl/Cl2. The interactions between Cs and solid Cl-bearing species (e.g. NaCl, Na2AlCl6, and KCl) formed CsCl and were responsible for the vaporization of Cs. Nevertheless, the release of HCl/Cl2 from the decomposition of NaCl and KCl had an insignificant effect on the vaporization of Cs. Compared to an air atmosphere, N2 facilitated the vaporization of Cs because the vaporization and/or decomposition of NaCl, Na2AlCl6, and KCl were delayed under the N2 atmosphere, which in turn enhanced the chlorination of Cs. By comparing the effect of adding NaCl, KCl, CaCl2, or MgCl2 on the vaporization of Cs, alkali chlorides (NaCl and KCl) were found to exhibit the best performance.</description><subject>Aluminosilicates</subject><subject>Aluminum silicates</subject><subject>Ashes</subject><subject>Atmosphere</subject><subject>Calcium chloride</subject><subject>Cesium</subject><subject>Cesium vaporization</subject><subject>Chemical reactions</subject><subject>Decomposition</subject><subject>Decomposition reactions</subject><subject>Heat treatment</subject><subject>Heat treatments</subject><subject>Heating furnaces</subject><subject>Hydrogen chloride</subject><subject>Incineration ash</subject><subject>KCl</subject><subject>Magnesium chloride</subject><subject>NaCl</subject><subject>Potassium chloride</subject><subject>Reaction mechanisms</subject><subject>Simulation</subject><subject>Sodium chloride</subject><subject>Thermal treatment</subject><subject>Thermodynamic equilibrium</subject><subject>Vapor phases</subject><subject>Vaporization</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNp9kEtr3DAUhUVIIZOkfyArQdee6GFbMnRTTB6loYWQrIUsX2c0WNJUkqdklb9eTWfWXV3u4XznXg5CN5SsKaHt7XY9LTCvGWFFoF1HmjO0olLwStCGn6MVKa6K8ZZeoMuUtoQQIZt6hT6eQZtsg8cOzEZ7m1zCix8h7qz31r_hvAEcwYW9nnGYcJ_wFIPDybpl1hnGolQm-Kyd9f92nTZ4XOKJja5wOYLODnzGf2ze4J-6L1kR_-jna_Rp0nOCz6d5hV7v7176x-rp18P3_ttTZTiTuZKsHikXXLLGdB3vQBA5AGE1G5hsG6kJo50QUg7CtMMIhAstRz0Ape1UQ82v0Jdj7i6G3wukrLZhib6cVKzu6pqIklVc7OgyMaQUYVK7aJ2O74oSdShabdWhaHUoWh2LLtDXIwTl_72FqJKx4A2MNoLJagz2f_hfQzWHUg</recordid><startdate>20210401</startdate><enddate>20210401</enddate><creator>Jiao, Facun</creator><creator>Wu, Chengli</creator><creator>Liu, Tao</creator><creator>Li, Hanxu</creator><creator>Dong, Zhongbing</creator><creator>Ninomiya, Yoshihiko</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope></search><sort><creationdate>20210401</creationdate><title>Reaction mechanisms underpinning the removal of Cs from simulated Cs-contaminated ash during thermal treatment with NaCl or KCl</title><author>Jiao, Facun ; 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The vaporization mechanism of cesium (Cs) in simulated Cs-contaminated ash during thermal treatment with the addition of NaCl or KCl was systemically examined in a laboratory-scale horizontal electrical-heating furnace. A thermodynamic equilibrium calculation was performed to predict the distribution of Cs and Cl in the solid and gas phases under different experimental conditions. The results indicated that Cs vaporized following heat treatment of the simulated ash with the addition of NaCl or KCl. The vaporization ratio of Cs increased as the reaction temperature. As the content of NaCl or KCl was increased, the vaporization ratio also increased at &gt; 1000 °C; whereas, it initially increased but then decreased at 900 °C. Both NaCl and KCl underwent direct vaporization and decomposition via chemical reactions with silicate/aluminosilicates in the ash, thus releasing HCl/Cl2. The interactions between Cs and solid Cl-bearing species (e.g. NaCl, Na2AlCl6, and KCl) formed CsCl and were responsible for the vaporization of Cs. Nevertheless, the release of HCl/Cl2 from the decomposition of NaCl and KCl had an insignificant effect on the vaporization of Cs. Compared to an air atmosphere, N2 facilitated the vaporization of Cs because the vaporization and/or decomposition of NaCl, Na2AlCl6, and KCl were delayed under the N2 atmosphere, which in turn enhanced the chlorination of Cs. By comparing the effect of adding NaCl, KCl, CaCl2, or MgCl2 on the vaporization of Cs, alkali chlorides (NaCl and KCl) were found to exhibit the best performance.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2020.119905</doi></addata></record>
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subjects Aluminosilicates
Aluminum silicates
Ashes
Atmosphere
Calcium chloride
Cesium
Cesium vaporization
Chemical reactions
Decomposition
Decomposition reactions
Heat treatment
Heat treatments
Heating furnaces
Hydrogen chloride
Incineration ash
KCl
Magnesium chloride
NaCl
Potassium chloride
Reaction mechanisms
Simulation
Sodium chloride
Thermal treatment
Thermodynamic equilibrium
Vapor phases
Vaporization
title Reaction mechanisms underpinning the removal of Cs from simulated Cs-contaminated ash during thermal treatment with NaCl or KCl
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