Adsorption/Desorption Capability of Potassium-Type Zeolite Prepared from Coal Fly Ash for Removing of Hg2
The feasibility of using potassium-type zeolite (K-type zeolite) prepared from coal fly ash (CFA) for the removal of Hg2+ from aqueous media and the adsorption/desorption capabilities of various potassium-type zeolites were assessed in this study. Potassium-type zeolite samples were synthesized by h...
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creator | Kobayashi, Yuhei Ogata, Fumihiko Saenjum, Chalermpong Nakamura, Takehiro Kawasaki, Naohito |
description | The feasibility of using potassium-type zeolite (K-type zeolite) prepared from coal fly ash (CFA) for the removal of Hg2+ from aqueous media and the adsorption/desorption capabilities of various potassium-type zeolites were assessed in this study. Potassium-type zeolite samples were synthesized by hydrothermal treatment of CFA at different intervals (designated CFA, FA1, FA3, FA6, FA12, FA24, and FA48, based on the hours of treatment) using potassium hydroxide solution, and their physicochemical characteristics were evaluated. Additionally, the quantity of Hg2+ adsorbed was in the order CFA, FA1 < FA3 < FA6 < FA12 < FA24 < FA48, in the current experimental design. Therefore, the hydrothermal treatment time is important to enhance the adsorption capability of K-type zeolite. Moreover, the effects of pH, temperature, contact time, and coexistence on the adsorption of Hg2+ were elucidated. In addition, Hg2+ adsorption mechanism using FA48 was demonstrated. Our results indicated that Hg2+ was exchanged with K+ in the interlayer of FA48 (correlation coefficient = 0.946). Finally, adsorbed Hg2+ onto FA48 could be desorbed using a sodium hydroxide solution (desorption percentage was approximately 70%). Our results revealed that FA48 could be a potential adsorbent for the removal of Hg2+ from aqueous media. |
doi_str_mv | 10.3390/su13084269 |
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Potassium-type zeolite samples were synthesized by hydrothermal treatment of CFA at different intervals (designated CFA, FA1, FA3, FA6, FA12, FA24, and FA48, based on the hours of treatment) using potassium hydroxide solution, and their physicochemical characteristics were evaluated. Additionally, the quantity of Hg2+ adsorbed was in the order CFA, FA1 < FA3 < FA6 < FA12 < FA24 < FA48, in the current experimental design. Therefore, the hydrothermal treatment time is important to enhance the adsorption capability of K-type zeolite. Moreover, the effects of pH, temperature, contact time, and coexistence on the adsorption of Hg2+ were elucidated. In addition, Hg2+ adsorption mechanism using FA48 was demonstrated. Our results indicated that Hg2+ was exchanged with K+ in the interlayer of FA48 (correlation coefficient = 0.946). Finally, adsorbed Hg2+ onto FA48 could be desorbed using a sodium hydroxide solution (desorption percentage was approximately 70%). Our results revealed that FA48 could be a potential adsorbent for the removal of Hg2+ from aqueous media.</description><identifier>ISSN: 2071-1050</identifier><identifier>EISSN: 2071-1050</identifier><identifier>DOI: 10.3390/su13084269</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Adsorption ; Aqueous solutions ; Caustic soda ; Coal-fired power plants ; Coexistence ; Correlation coefficient ; Correlation coefficients ; Design of experiments ; Desorption ; Electricity distribution ; Experimental design ; Fly ash ; Hydrothermal treatment ; Interlayers ; Membrane filters ; Nuclear power plants ; Potash ; Potassium ; Potassium hydroxide ; Potassium hydroxides ; Sodium hydroxide ; Temperature effects ; Water conservation ; Zeolites</subject><ispartof>Sustainability, 2021-04, Vol.13 (8), p.4269</ispartof><rights>2021 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c291t-90f10c9a72aff3dd5b4666e29fda6cc8a7f5052dfea9d5dd5e686c451889a5e23</citedby><cites>FETCH-LOGICAL-c291t-90f10c9a72aff3dd5b4666e29fda6cc8a7f5052dfea9d5dd5e686c451889a5e23</cites><orcidid>0000-0002-2755-8341 ; 0000-0003-0229-5116 ; 0000-0002-9412-0868</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Kobayashi, Yuhei</creatorcontrib><creatorcontrib>Ogata, Fumihiko</creatorcontrib><creatorcontrib>Saenjum, Chalermpong</creatorcontrib><creatorcontrib>Nakamura, Takehiro</creatorcontrib><creatorcontrib>Kawasaki, Naohito</creatorcontrib><title>Adsorption/Desorption Capability of Potassium-Type Zeolite Prepared from Coal Fly Ash for Removing of Hg2</title><title>Sustainability</title><description>The feasibility of using potassium-type zeolite (K-type zeolite) prepared from coal fly ash (CFA) for the removal of Hg2+ from aqueous media and the adsorption/desorption capabilities of various potassium-type zeolites were assessed in this study. Potassium-type zeolite samples were synthesized by hydrothermal treatment of CFA at different intervals (designated CFA, FA1, FA3, FA6, FA12, FA24, and FA48, based on the hours of treatment) using potassium hydroxide solution, and their physicochemical characteristics were evaluated. Additionally, the quantity of Hg2+ adsorbed was in the order CFA, FA1 < FA3 < FA6 < FA12 < FA24 < FA48, in the current experimental design. Therefore, the hydrothermal treatment time is important to enhance the adsorption capability of K-type zeolite. Moreover, the effects of pH, temperature, contact time, and coexistence on the adsorption of Hg2+ were elucidated. In addition, Hg2+ adsorption mechanism using FA48 was demonstrated. Our results indicated that Hg2+ was exchanged with K+ in the interlayer of FA48 (correlation coefficient = 0.946). Finally, adsorbed Hg2+ onto FA48 could be desorbed using a sodium hydroxide solution (desorption percentage was approximately 70%). Our results revealed that FA48 could be a potential adsorbent for the removal of Hg2+ from aqueous media.</description><subject>Adsorption</subject><subject>Aqueous solutions</subject><subject>Caustic soda</subject><subject>Coal-fired power plants</subject><subject>Coexistence</subject><subject>Correlation coefficient</subject><subject>Correlation coefficients</subject><subject>Design of experiments</subject><subject>Desorption</subject><subject>Electricity distribution</subject><subject>Experimental design</subject><subject>Fly ash</subject><subject>Hydrothermal treatment</subject><subject>Interlayers</subject><subject>Membrane filters</subject><subject>Nuclear power plants</subject><subject>Potash</subject><subject>Potassium</subject><subject>Potassium hydroxide</subject><subject>Potassium hydroxides</subject><subject>Sodium hydroxide</subject><subject>Temperature effects</subject><subject>Water conservation</subject><subject>Zeolites</subject><issn>2071-1050</issn><issn>2071-1050</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><sourceid>ABUWG</sourceid><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><recordid>eNpNUF9LwzAcDKLgmHvxEwR8E-ryp8max1GdEwYOmS--lKz5ZWa0S01aod9-HVP0Xu7gjjs4hG4peeBckWnsKCdZyqS6QCNGZjShRJDLf_oaTWLckwGcU0XlCLm5iT40rfOH6SP8SpzrRm9d5doee4vXvtUxuq5ONn0D-AP84ABeB2h0AINt8DXOva7wourxPH5i6wN-g9p_u8Pu1LDcsRt0ZXUVYfLDY_S-eNrky2T1-vySz1dJyRRtE0UsJaXSM6at5caIbSqlBKas0bIsMz2zgghmLGhlxOCDzGSZCpplSgtgfIzuzr1N8F8dxLbY-y4chsmCCcmoSrmQQ-r-nCqDjzGALZrgah36gpLi9Gbx9yY_AvGVZ7U</recordid><startdate>20210412</startdate><enddate>20210412</enddate><creator>Kobayashi, Yuhei</creator><creator>Ogata, Fumihiko</creator><creator>Saenjum, Chalermpong</creator><creator>Nakamura, Takehiro</creator><creator>Kawasaki, Naohito</creator><general>MDPI AG</general><scope>AAYXX</scope><scope>CITATION</scope><scope>4U-</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><orcidid>https://orcid.org/0000-0002-2755-8341</orcidid><orcidid>https://orcid.org/0000-0003-0229-5116</orcidid><orcidid>https://orcid.org/0000-0002-9412-0868</orcidid></search><sort><creationdate>20210412</creationdate><title>Adsorption/Desorption Capability of Potassium-Type Zeolite Prepared from Coal Fly Ash for Removing of Hg2</title><author>Kobayashi, Yuhei ; 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Potassium-type zeolite samples were synthesized by hydrothermal treatment of CFA at different intervals (designated CFA, FA1, FA3, FA6, FA12, FA24, and FA48, based on the hours of treatment) using potassium hydroxide solution, and their physicochemical characteristics were evaluated. Additionally, the quantity of Hg2+ adsorbed was in the order CFA, FA1 < FA3 < FA6 < FA12 < FA24 < FA48, in the current experimental design. Therefore, the hydrothermal treatment time is important to enhance the adsorption capability of K-type zeolite. Moreover, the effects of pH, temperature, contact time, and coexistence on the adsorption of Hg2+ were elucidated. In addition, Hg2+ adsorption mechanism using FA48 was demonstrated. Our results indicated that Hg2+ was exchanged with K+ in the interlayer of FA48 (correlation coefficient = 0.946). Finally, adsorbed Hg2+ onto FA48 could be desorbed using a sodium hydroxide solution (desorption percentage was approximately 70%). 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subjects | Adsorption Aqueous solutions Caustic soda Coal-fired power plants Coexistence Correlation coefficient Correlation coefficients Design of experiments Desorption Electricity distribution Experimental design Fly ash Hydrothermal treatment Interlayers Membrane filters Nuclear power plants Potash Potassium Potassium hydroxide Potassium hydroxides Sodium hydroxide Temperature effects Water conservation Zeolites |
title | Adsorption/Desorption Capability of Potassium-Type Zeolite Prepared from Coal Fly Ash for Removing of Hg2 |
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