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Development of carbon dioxide adsorbent from rice husk char
This study was mainly concerned about the development of carbon dioxide (CO2) adsorbent from rice husk (RH). Several chemical treatments were used to produce activated rice husk char (RHAC) from RH. Initially the RH was refluxed with 3M of sodium hydroxide (NaOH) solution, activation followed by usi...
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Published in: | IOP conference series. Earth and environmental science 2016-06, Vol.36 (1), p.12022 |
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description | This study was mainly concerned about the development of carbon dioxide (CO2) adsorbent from rice husk (RH). Several chemical treatments were used to produce activated rice husk char (RHAC) from RH. Initially the RH was refluxed with 3M of sodium hydroxide (NaOH) solution, activation followed by using 0.5M of zinc chloride (ZnCl2) solution and finally acidic treatment by using 0.1M of hydrochloric acid (HCl). Then, the RHAC was functionalized by using 3-chloropropylamine hydrochloride (3-CPA) and noted as RHN. RHN samples were characterized with scanning electron microscopy (SEM), mercury intrusion porosimetry (MIP), fourier transform infrared spectroscopy (FTIR). Based on the SEM, the RHN sample had a large pore diameter compared to RH sample after being treated. Based on MIP data, the average pore diameter between RH and RHAC samples were increased significantly from 0.928 microns to 1.017 microns. The RHN sample also had higher total porosity (%) compared to RHAC and RH (58.45%, 47.82% and 45.57% respectively). The total specific surface area of the sample was much increasing from RHO to RHAC (29.17 m2 g and 62.94 m2 g respectively) and slightly being decreasing from RHAC to RHN (58.88 m2 g). FTIR result showed the present of weak band at 1587 cm-1 which demonstrating of the amine group present on the sample. The CO2 capture result showed that the decreasing of operating temperature can increase the breakthrough time of CO2 capture. On the contrary decreasing of CO2 gas flow rate can increase the breakthrough time of CO2 capture. The highest total amount of CO2 adsorbed was 25338.57 mg of CO2 g of RHN sample by using 100 mL min of gas flow rate at 30oC. Based on adsorption isotherm analysis, the Freundlich isotherm was the best isotherm to describe the CO2 adsorption on the sample. |
doi_str_mv | 10.1088/1755-1315/36/1/012022 |
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Several chemical treatments were used to produce activated rice husk char (RHAC) from RH. Initially the RH was refluxed with 3M of sodium hydroxide (NaOH) solution, activation followed by using 0.5M of zinc chloride (ZnCl2) solution and finally acidic treatment by using 0.1M of hydrochloric acid (HCl). Then, the RHAC was functionalized by using 3-chloropropylamine hydrochloride (3-CPA) and noted as RHN. RHN samples were characterized with scanning electron microscopy (SEM), mercury intrusion porosimetry (MIP), fourier transform infrared spectroscopy (FTIR). Based on the SEM, the RHN sample had a large pore diameter compared to RH sample after being treated. Based on MIP data, the average pore diameter between RH and RHAC samples were increased significantly from 0.928 microns to 1.017 microns. The RHN sample also had higher total porosity (%) compared to RHAC and RH (58.45%, 47.82% and 45.57% respectively). The total specific surface area of the sample was much increasing from RHO to RHAC (29.17 m2 g and 62.94 m2 g respectively) and slightly being decreasing from RHAC to RHN (58.88 m2 g). FTIR result showed the present of weak band at 1587 cm-1 which demonstrating of the amine group present on the sample. The CO2 capture result showed that the decreasing of operating temperature can increase the breakthrough time of CO2 capture. On the contrary decreasing of CO2 gas flow rate can increase the breakthrough time of CO2 capture. The highest total amount of CO2 adsorbed was 25338.57 mg of CO2 g of RHN sample by using 100 mL min of gas flow rate at 30oC. Based on adsorption isotherm analysis, the Freundlich isotherm was the best isotherm to describe the CO2 adsorption on the sample.</description><identifier>ISSN: 1755-1307</identifier><identifier>EISSN: 1755-1315</identifier><identifier>DOI: 10.1088/1755-1315/36/1/012022</identifier><language>eng</language><publisher>Bristol: IOP Publishing</publisher><subject>Adsorbents ; Adsorption ; Carbon dioxide ; Carbon sequestration ; Chemical treatment ; Flow rates ; Flow velocity ; Fourier analysis ; Fourier transforms ; Gas flow ; Hydrochloric acid ; Infrared spectroscopy ; Isotherms ; Mercury ; Operating temperature ; Porosity ; Rice ; Scanning electron microscopy ; Sodium hydroxide ; Zinc chloride</subject><ispartof>IOP conference series. Earth and environmental science, 2016-06, Vol.36 (1), p.12022</ispartof><rights>Published under licence by IOP Publishing Ltd</rights><rights>2016. This work is published under http://creativecommons.org/licenses/by/3.0/ (the “License”). 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-c3542-570770c8aa282bf9426fd2d70dcc5a8865ced68362f186df39301f246a9c7e443</citedby><cites>FETCH-LOGICAL-c3542-570770c8aa282bf9426fd2d70dcc5a8865ced68362f186df39301f246a9c7e443</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.proquest.com/docview/2548512458?pq-origsite=primo$$EHTML$$P50$$Gproquest$$Hfree_for_read</linktohtml><link.rule.ids>314,780,784,25753,27924,27925,37012,44590</link.rule.ids></links><search><creatorcontrib>Abang, S</creatorcontrib><creatorcontrib>Janaun, J</creatorcontrib><creatorcontrib>Anisuzzaman, S M</creatorcontrib><creatorcontrib>Ikhwan, F S</creatorcontrib><title>Development of carbon dioxide adsorbent from rice husk char</title><title>IOP conference series. Earth and environmental science</title><addtitle>IOP Conf. Ser.: Earth Environ. Sci</addtitle><description>This study was mainly concerned about the development of carbon dioxide (CO2) adsorbent from rice husk (RH). Several chemical treatments were used to produce activated rice husk char (RHAC) from RH. Initially the RH was refluxed with 3M of sodium hydroxide (NaOH) solution, activation followed by using 0.5M of zinc chloride (ZnCl2) solution and finally acidic treatment by using 0.1M of hydrochloric acid (HCl). Then, the RHAC was functionalized by using 3-chloropropylamine hydrochloride (3-CPA) and noted as RHN. RHN samples were characterized with scanning electron microscopy (SEM), mercury intrusion porosimetry (MIP), fourier transform infrared spectroscopy (FTIR). Based on the SEM, the RHN sample had a large pore diameter compared to RH sample after being treated. Based on MIP data, the average pore diameter between RH and RHAC samples were increased significantly from 0.928 microns to 1.017 microns. The RHN sample also had higher total porosity (%) compared to RHAC and RH (58.45%, 47.82% and 45.57% respectively). The total specific surface area of the sample was much increasing from RHO to RHAC (29.17 m2 g and 62.94 m2 g respectively) and slightly being decreasing from RHAC to RHN (58.88 m2 g). FTIR result showed the present of weak band at 1587 cm-1 which demonstrating of the amine group present on the sample. The CO2 capture result showed that the decreasing of operating temperature can increase the breakthrough time of CO2 capture. On the contrary decreasing of CO2 gas flow rate can increase the breakthrough time of CO2 capture. The highest total amount of CO2 adsorbed was 25338.57 mg of CO2 g of RHN sample by using 100 mL min of gas flow rate at 30oC. Based on adsorption isotherm analysis, the Freundlich isotherm was the best isotherm to describe the CO2 adsorption on the sample.</description><subject>Adsorbents</subject><subject>Adsorption</subject><subject>Carbon dioxide</subject><subject>Carbon sequestration</subject><subject>Chemical treatment</subject><subject>Flow rates</subject><subject>Flow velocity</subject><subject>Fourier analysis</subject><subject>Fourier transforms</subject><subject>Gas flow</subject><subject>Hydrochloric acid</subject><subject>Infrared spectroscopy</subject><subject>Isotherms</subject><subject>Mercury</subject><subject>Operating temperature</subject><subject>Porosity</subject><subject>Rice</subject><subject>Scanning electron microscopy</subject><subject>Sodium hydroxide</subject><subject>Zinc chloride</subject><issn>1755-1307</issn><issn>1755-1315</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><sourceid>PIMPY</sourceid><recordid>eNqFkEtLAzEUhYMoWKs_QQi4cDVO3sngSur4gIILdR3SPOjUthmTVuy_d4aR6kJwdS_3nu9c7gHgHKMrjJQqseS8wBTzkooSlwgTRMgBGO3nh_seyWNwkvMCISEZrUbg-tZ_-GVsV369gTFAa9IsrqFr4mfjPDQuxzTrdyHFFUyN9XC-zW_Qzk06BUfBLLM_-65j8HpXv0weiunT_ePkZlpYyhkpuERSIquMIYrMQsWICI44iZy13CgluPVOKCpIwEq4QCuKcCBMmMpKzxgdg4vBt03xfevzRi_iNq27k5pwpjgmjKtOxQeVTTHn5INuU7Myaacx0n1Ous9A93loKjTWQ04dhweuie2P8X_M5R9MXT__Vum2--ULpEF0fw</recordid><startdate>20160601</startdate><enddate>20160601</enddate><creator>Abang, S</creator><creator>Janaun, J</creator><creator>Anisuzzaman, S M</creator><creator>Ikhwan, F S</creator><general>IOP Publishing</general><scope>O3W</scope><scope>TSCCA</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>ATCPS</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BHPHI</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>GNUQQ</scope><scope>HCIFZ</scope><scope>PATMY</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><scope>PYCSY</scope></search><sort><creationdate>20160601</creationdate><title>Development of carbon dioxide adsorbent from rice husk char</title><author>Abang, S ; Janaun, J ; Anisuzzaman, S M ; Ikhwan, F S</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3542-570770c8aa282bf9426fd2d70dcc5a8865ced68362f186df39301f246a9c7e443</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Adsorbents</topic><topic>Adsorption</topic><topic>Carbon dioxide</topic><topic>Carbon sequestration</topic><topic>Chemical treatment</topic><topic>Flow rates</topic><topic>Flow velocity</topic><topic>Fourier analysis</topic><topic>Fourier transforms</topic><topic>Gas flow</topic><topic>Hydrochloric acid</topic><topic>Infrared spectroscopy</topic><topic>Isotherms</topic><topic>Mercury</topic><topic>Operating temperature</topic><topic>Porosity</topic><topic>Rice</topic><topic>Scanning electron microscopy</topic><topic>Sodium hydroxide</topic><topic>Zinc chloride</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Abang, S</creatorcontrib><creatorcontrib>Janaun, J</creatorcontrib><creatorcontrib>Anisuzzaman, S M</creatorcontrib><creatorcontrib>Ikhwan, F S</creatorcontrib><collection>Open Access: IOP Publishing Free Content</collection><collection>IOPscience (Open Access)</collection><collection>CrossRef</collection><collection>ProQuest Central (Alumni)</collection><collection>ProQuest Central</collection><collection>Agricultural & Environmental Science Collection</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Natural Science Collection</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>ProQuest Central Student</collection><collection>SciTech Premium Collection</collection><collection>Environmental Science Database</collection><collection>Publicly Available Content Database</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>ProQuest Central China</collection><collection>Environmental Science Collection</collection><jtitle>IOP conference series. Earth and environmental science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Abang, S</au><au>Janaun, J</au><au>Anisuzzaman, S M</au><au>Ikhwan, F S</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Development of carbon dioxide adsorbent from rice husk char</atitle><jtitle>IOP conference series. Earth and environmental science</jtitle><addtitle>IOP Conf. Ser.: Earth Environ. Sci</addtitle><date>2016-06-01</date><risdate>2016</risdate><volume>36</volume><issue>1</issue><spage>12022</spage><pages>12022-</pages><issn>1755-1307</issn><eissn>1755-1315</eissn><abstract>This study was mainly concerned about the development of carbon dioxide (CO2) adsorbent from rice husk (RH). Several chemical treatments were used to produce activated rice husk char (RHAC) from RH. Initially the RH was refluxed with 3M of sodium hydroxide (NaOH) solution, activation followed by using 0.5M of zinc chloride (ZnCl2) solution and finally acidic treatment by using 0.1M of hydrochloric acid (HCl). Then, the RHAC was functionalized by using 3-chloropropylamine hydrochloride (3-CPA) and noted as RHN. RHN samples were characterized with scanning electron microscopy (SEM), mercury intrusion porosimetry (MIP), fourier transform infrared spectroscopy (FTIR). Based on the SEM, the RHN sample had a large pore diameter compared to RH sample after being treated. Based on MIP data, the average pore diameter between RH and RHAC samples were increased significantly from 0.928 microns to 1.017 microns. The RHN sample also had higher total porosity (%) compared to RHAC and RH (58.45%, 47.82% and 45.57% respectively). The total specific surface area of the sample was much increasing from RHO to RHAC (29.17 m2 g and 62.94 m2 g respectively) and slightly being decreasing from RHAC to RHN (58.88 m2 g). FTIR result showed the present of weak band at 1587 cm-1 which demonstrating of the amine group present on the sample. The CO2 capture result showed that the decreasing of operating temperature can increase the breakthrough time of CO2 capture. On the contrary decreasing of CO2 gas flow rate can increase the breakthrough time of CO2 capture. The highest total amount of CO2 adsorbed was 25338.57 mg of CO2 g of RHN sample by using 100 mL min of gas flow rate at 30oC. Based on adsorption isotherm analysis, the Freundlich isotherm was the best isotherm to describe the CO2 adsorption on the sample.</abstract><cop>Bristol</cop><pub>IOP Publishing</pub><doi>10.1088/1755-1315/36/1/012022</doi><tpages>9</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Adsorbents Adsorption Carbon dioxide Carbon sequestration Chemical treatment Flow rates Flow velocity Fourier analysis Fourier transforms Gas flow Hydrochloric acid Infrared spectroscopy Isotherms Mercury Operating temperature Porosity Rice Scanning electron microscopy Sodium hydroxide Zinc chloride |
title | Development of carbon dioxide adsorbent from rice husk char |
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