Synthesis of carbon dioxide adsorbents by zeolitization of fly ash
Coal-combusting power plants are simultaneously among the main emitters of carbon dioxide and the main generator of solid by-products, such as fly ash (FA). An attempt to find a common solution for these environmental problems is reported in the present research work. This study describes a synthesi...
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Veröffentlicht in: | Journal of thermal analysis and calorimetry 2016-04, Vol.124 (1), p.101-106 |
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creator | Kalvachev, Yu Zgureva, D. Boycheva, S. Barbov, B. Petrova, N. |
description | Coal-combusting power plants are simultaneously among the main emitters of carbon dioxide and the main generator of solid by-products, such as fly ash (FA). An attempt to find a common solution for these environmental problems is reported in the present research work. This study describes a synthesis procedure for zeolite X by interaction of FA, originating from Bulgarian lignite coals with sodium hydroxide (NaOH), followed by hydrothermal treatment. The sorption capacity of the so-obtained zeolite with respect to carbon dioxide is estimated by using the thermogravimetric method. Ash residues, containing 52.66 mass% of SiO
2
and 23.37 mass% of Al
2
O
3
, were subjected to a dual-stage fusion-hydrothermal conversion. Coal ash and NaOH mixture at a ratio of 1:2 was sintered at 550 °C, and after dilution with water under continuous stirring, the reaction mixture was charged into an autoclave for hydrothermal reaction occurring for 2 h at 90 °C. The obtained zeolite X was characterized by scanning electron microscopy and X-ray diffraction, and it was subjected to thermogravimetric analysis before and after exposure to carbon dioxide flow. Determination of its adsorption capacity toward CO
2
was carried out at 22 °C, it was measured to be 60 mg g
−1
at this temperature, and the adsorption–desorption equilibrium was reached after 1 h under flow conditions (30 mL min
−1
). The sorption capacity of fly ash-based zeolite was compared to that of a reference zeolite X, synthesized from pure starting materials. |
doi_str_mv | 10.1007/s10973-015-5148-1 |
format | Article |
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2
and 23.37 mass% of Al
2
O
3
, were subjected to a dual-stage fusion-hydrothermal conversion. Coal ash and NaOH mixture at a ratio of 1:2 was sintered at 550 °C, and after dilution with water under continuous stirring, the reaction mixture was charged into an autoclave for hydrothermal reaction occurring for 2 h at 90 °C. The obtained zeolite X was characterized by scanning electron microscopy and X-ray diffraction, and it was subjected to thermogravimetric analysis before and after exposure to carbon dioxide flow. Determination of its adsorption capacity toward CO
2
was carried out at 22 °C, it was measured to be 60 mg g
−1
at this temperature, and the adsorption–desorption equilibrium was reached after 1 h under flow conditions (30 mL min
−1
). The sorption capacity of fly ash-based zeolite was compared to that of a reference zeolite X, synthesized from pure starting materials.</description><identifier>ISSN: 1388-6150</identifier><identifier>EISSN: 1588-2926</identifier><identifier>EISSN: 1572-8943</identifier><identifier>DOI: 10.1007/s10973-015-5148-1</identifier><language>eng</language><publisher>Dordrecht: Springer Netherlands</publisher><subject>Aluminum compounds ; Analytical Chemistry ; Byproducts ; Carbon dioxide ; Chemistry ; Chemistry and Materials Science ; Electric power-plants ; Fly ash ; Hydroxides ; Inorganic Chemistry ; Lignite ; Measurement Science and Instrumentation ; Physical Chemistry ; Polymer Sciences ; Power plants ; Scanning electron microscopy ; Sorption ; Synthesis ; Thermogravimetric analysis ; Zeolites</subject><ispartof>Journal of thermal analysis and calorimetry, 2016-04, Vol.124 (1), p.101-106</ispartof><rights>Akadémiai Kiadó, Budapest, Hungary 2015</rights><rights>COPYRIGHT 2016 Springer</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c431t-32d970e699d52da9100265daa12c464b494ef90c031b7db7f417688b1bb8674a3</citedby><cites>FETCH-LOGICAL-c431t-32d970e699d52da9100265daa12c464b494ef90c031b7db7f417688b1bb8674a3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s10973-015-5148-1$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s10973-015-5148-1$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,780,784,27923,27924,41487,42556,51318</link.rule.ids></links><search><creatorcontrib>Kalvachev, Yu</creatorcontrib><creatorcontrib>Zgureva, D.</creatorcontrib><creatorcontrib>Boycheva, S.</creatorcontrib><creatorcontrib>Barbov, B.</creatorcontrib><creatorcontrib>Petrova, N.</creatorcontrib><title>Synthesis of carbon dioxide adsorbents by zeolitization of fly ash</title><title>Journal of thermal analysis and calorimetry</title><addtitle>J Therm Anal Calorim</addtitle><description>Coal-combusting power plants are simultaneously among the main emitters of carbon dioxide and the main generator of solid by-products, such as fly ash (FA). An attempt to find a common solution for these environmental problems is reported in the present research work. This study describes a synthesis procedure for zeolite X by interaction of FA, originating from Bulgarian lignite coals with sodium hydroxide (NaOH), followed by hydrothermal treatment. The sorption capacity of the so-obtained zeolite with respect to carbon dioxide is estimated by using the thermogravimetric method. Ash residues, containing 52.66 mass% of SiO
2
and 23.37 mass% of Al
2
O
3
, were subjected to a dual-stage fusion-hydrothermal conversion. Coal ash and NaOH mixture at a ratio of 1:2 was sintered at 550 °C, and after dilution with water under continuous stirring, the reaction mixture was charged into an autoclave for hydrothermal reaction occurring for 2 h at 90 °C. The obtained zeolite X was characterized by scanning electron microscopy and X-ray diffraction, and it was subjected to thermogravimetric analysis before and after exposure to carbon dioxide flow. Determination of its adsorption capacity toward CO
2
was carried out at 22 °C, it was measured to be 60 mg g
−1
at this temperature, and the adsorption–desorption equilibrium was reached after 1 h under flow conditions (30 mL min
−1
). The sorption capacity of fly ash-based zeolite was compared to that of a reference zeolite X, synthesized from pure starting materials.</description><subject>Aluminum compounds</subject><subject>Analytical Chemistry</subject><subject>Byproducts</subject><subject>Carbon dioxide</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Electric power-plants</subject><subject>Fly ash</subject><subject>Hydroxides</subject><subject>Inorganic Chemistry</subject><subject>Lignite</subject><subject>Measurement Science and Instrumentation</subject><subject>Physical Chemistry</subject><subject>Polymer Sciences</subject><subject>Power plants</subject><subject>Scanning electron microscopy</subject><subject>Sorption</subject><subject>Synthesis</subject><subject>Thermogravimetric analysis</subject><subject>Zeolites</subject><issn>1388-6150</issn><issn>1588-2926</issn><issn>1572-8943</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNp9kU1LxDAQhosouH78AG896qGaSZO0Oa7ix4Ig-HEOSZOukW6zZrLg-uvNUi9eZA4zhOcZhrxFcQbkEghprhCIbOqKAK84sLaCvWIGvG0rKqnYz3OdZwGcHBZHiB-EECkJzIrrl-2Y3h16LENfdjqaMJbWhy9vXakthmjcmLA02_LbhcEn_62Tz0ym-2Fbanw_KQ56PaA7_e3Hxdvd7evNQ_X4dL-4mT9WHashVTW1siFOSGk5tVrms6ngVmugHRPMMMlcL0lHajCNNU3PoBFta8CYVjRM18fF-bR3HcPnxmFSK4-dGwY9urBBBS3lvG65kBm9nNClHpzyYx9S1F0u61a-C6PrfX6fMyaA5toJF3-EzCT3lZZ6g6gWL89_WZjYLgbE6Hq1jn6l41YBUbsw1BSGymGoXRgKskMnBzM7Ll1UH2ETx_xd_0g_-5mKag</recordid><startdate>20160401</startdate><enddate>20160401</enddate><creator>Kalvachev, Yu</creator><creator>Zgureva, D.</creator><creator>Boycheva, S.</creator><creator>Barbov, B.</creator><creator>Petrova, N.</creator><general>Springer Netherlands</general><general>Springer</general><scope>AAYXX</scope><scope>CITATION</scope><scope>ISR</scope><scope>7QF</scope><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>20160401</creationdate><title>Synthesis of carbon dioxide adsorbents by zeolitization of fly ash</title><author>Kalvachev, Yu ; Zgureva, D. ; Boycheva, S. ; Barbov, B. ; Petrova, N.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c431t-32d970e699d52da9100265daa12c464b494ef90c031b7db7f417688b1bb8674a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Aluminum compounds</topic><topic>Analytical Chemistry</topic><topic>Byproducts</topic><topic>Carbon dioxide</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Electric power-plants</topic><topic>Fly ash</topic><topic>Hydroxides</topic><topic>Inorganic Chemistry</topic><topic>Lignite</topic><topic>Measurement Science and Instrumentation</topic><topic>Physical Chemistry</topic><topic>Polymer Sciences</topic><topic>Power plants</topic><topic>Scanning electron microscopy</topic><topic>Sorption</topic><topic>Synthesis</topic><topic>Thermogravimetric analysis</topic><topic>Zeolites</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kalvachev, Yu</creatorcontrib><creatorcontrib>Zgureva, D.</creatorcontrib><creatorcontrib>Boycheva, S.</creatorcontrib><creatorcontrib>Barbov, B.</creatorcontrib><creatorcontrib>Petrova, N.</creatorcontrib><collection>CrossRef</collection><collection>Gale In Context: Science</collection><collection>Aluminium Industry Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Journal of thermal analysis and calorimetry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kalvachev, Yu</au><au>Zgureva, D.</au><au>Boycheva, S.</au><au>Barbov, B.</au><au>Petrova, N.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Synthesis of carbon dioxide adsorbents by zeolitization of fly ash</atitle><jtitle>Journal of thermal analysis and calorimetry</jtitle><stitle>J Therm Anal Calorim</stitle><date>2016-04-01</date><risdate>2016</risdate><volume>124</volume><issue>1</issue><spage>101</spage><epage>106</epage><pages>101-106</pages><issn>1388-6150</issn><eissn>1588-2926</eissn><eissn>1572-8943</eissn><abstract>Coal-combusting power plants are simultaneously among the main emitters of carbon dioxide and the main generator of solid by-products, such as fly ash (FA). An attempt to find a common solution for these environmental problems is reported in the present research work. This study describes a synthesis procedure for zeolite X by interaction of FA, originating from Bulgarian lignite coals with sodium hydroxide (NaOH), followed by hydrothermal treatment. The sorption capacity of the so-obtained zeolite with respect to carbon dioxide is estimated by using the thermogravimetric method. Ash residues, containing 52.66 mass% of SiO
2
and 23.37 mass% of Al
2
O
3
, were subjected to a dual-stage fusion-hydrothermal conversion. Coal ash and NaOH mixture at a ratio of 1:2 was sintered at 550 °C, and after dilution with water under continuous stirring, the reaction mixture was charged into an autoclave for hydrothermal reaction occurring for 2 h at 90 °C. The obtained zeolite X was characterized by scanning electron microscopy and X-ray diffraction, and it was subjected to thermogravimetric analysis before and after exposure to carbon dioxide flow. Determination of its adsorption capacity toward CO
2
was carried out at 22 °C, it was measured to be 60 mg g
−1
at this temperature, and the adsorption–desorption equilibrium was reached after 1 h under flow conditions (30 mL min
−1
). The sorption capacity of fly ash-based zeolite was compared to that of a reference zeolite X, synthesized from pure starting materials.</abstract><cop>Dordrecht</cop><pub>Springer Netherlands</pub><doi>10.1007/s10973-015-5148-1</doi><tpages>6</tpages></addata></record> |
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subjects | Aluminum compounds Analytical Chemistry Byproducts Carbon dioxide Chemistry Chemistry and Materials Science Electric power-plants Fly ash Hydroxides Inorganic Chemistry Lignite Measurement Science and Instrumentation Physical Chemistry Polymer Sciences Power plants Scanning electron microscopy Sorption Synthesis Thermogravimetric analysis Zeolites |
title | Synthesis of carbon dioxide adsorbents by zeolitization of fly ash |
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