Kinetics of the dehydration of glycerol over acid catalysts with an investigation of deactivation mechanism by coke

[Display omitted] •Kinetics for dehydration of glycerol considering deactivation is investigated.•The deactivation behavior is analyzed quantitatively and qualitatively•Characteristics of used catalysts are analyzed with time on stream.•Effects of hierarchical structure for retardation of deactivati...

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Veröffentlicht in:Applied catalysis. B, Environmental Environmental, 2015-10, Vol.176-177, p.1-10
Hauptverfasser: Park, Hongseok, Yun, Yang Sik, Kim, Tae Yong, Lee, Kyung Rok, Baek, Jayeon, Yi, Jongheop
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container_title Applied catalysis. B, Environmental
container_volume 176-177
creator Park, Hongseok
Yun, Yang Sik
Kim, Tae Yong
Lee, Kyung Rok
Baek, Jayeon
Yi, Jongheop
description [Display omitted] •Kinetics for dehydration of glycerol considering deactivation is investigated.•The deactivation behavior is analyzed quantitatively and qualitatively•Characteristics of used catalysts are analyzed with time on stream.•Effects of hierarchical structure for retardation of deactivation. Kinetics for the dehydration of glycerol, taking deactivation into account, was investigated. HZSM-5 and ASPN-40 (aluminosilicophosphate nanosphere) catalysts were used in the studies. A kinetic model was established, based on the reaction mechanism, taking into account two parallel reactions (transformation of glycerol into acrolein or acetol) that occur over the acid sites. The results were consistent with experimental results using both catalysts. Based on the overall reaction, the apparent kinetic parameters were obtained and the results confirmed that the first dehydration step, which occurs over Brønsted acid sites, is the rate determining step. In addition, the structural features of catalysts appear to be one of the crucial factors that affect the kinetics of the reaction over acid sites. The HZSM-5 and ASPN-40 catalysts were deactivated to different degrees under same conditions. A kinetic equation for the deactivation, which is a function of product concentration, was found to be in good agreement with the experimental results. To elucidate the mechanism of catalyst deactivation, various characteristic analyses (BET, NH3-TPD, TPO, and 13C NMR) were employed. The changes in the properties of catalysts and the nature of the produced coke were analyzed. In the case of HZSM-5, the condensation of coke precursors is promoted within its narrow pore structures, which results in the rapid deactivation of the catalyst. In ASPN-40, less condensed carbonaceous compounds are observed and the deactivation is delayed due to the relatively uninterrupted diffusion of materials (reactants, products, or potential coke precursors).
doi_str_mv 10.1016/j.apcatb.2015.03.046
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Kinetics for the dehydration of glycerol, taking deactivation into account, was investigated. HZSM-5 and ASPN-40 (aluminosilicophosphate nanosphere) catalysts were used in the studies. A kinetic model was established, based on the reaction mechanism, taking into account two parallel reactions (transformation of glycerol into acrolein or acetol) that occur over the acid sites. The results were consistent with experimental results using both catalysts. Based on the overall reaction, the apparent kinetic parameters were obtained and the results confirmed that the first dehydration step, which occurs over Brønsted acid sites, is the rate determining step. In addition, the structural features of catalysts appear to be one of the crucial factors that affect the kinetics of the reaction over acid sites. The HZSM-5 and ASPN-40 catalysts were deactivated to different degrees under same conditions. A kinetic equation for the deactivation, which is a function of product concentration, was found to be in good agreement with the experimental results. To elucidate the mechanism of catalyst deactivation, various characteristic analyses (BET, NH3-TPD, TPO, and 13C NMR) were employed. The changes in the properties of catalysts and the nature of the produced coke were analyzed. In the case of HZSM-5, the condensation of coke precursors is promoted within its narrow pore structures, which results in the rapid deactivation of the catalyst. In ASPN-40, less condensed carbonaceous compounds are observed and the deactivation is delayed due to the relatively uninterrupted diffusion of materials (reactants, products, or potential coke precursors).</description><identifier>ISSN: 0926-3373</identifier><identifier>EISSN: 1873-3883</identifier><identifier>DOI: 10.1016/j.apcatb.2015.03.046</identifier><language>eng</language><publisher>Elsevier B.V</publisher><subject>Acid catalysts ; Catalysis ; Catalysts ; Coke ; Deactivation ; Dehydration ; Dehydration of glycerol ; Glycerols ; Kinetics ; Mathematical models ; Reaction kinetics</subject><ispartof>Applied catalysis. 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B, Environmental</title><description>[Display omitted] •Kinetics for dehydration of glycerol considering deactivation is investigated.•The deactivation behavior is analyzed quantitatively and qualitatively•Characteristics of used catalysts are analyzed with time on stream.•Effects of hierarchical structure for retardation of deactivation. Kinetics for the dehydration of glycerol, taking deactivation into account, was investigated. HZSM-5 and ASPN-40 (aluminosilicophosphate nanosphere) catalysts were used in the studies. A kinetic model was established, based on the reaction mechanism, taking into account two parallel reactions (transformation of glycerol into acrolein or acetol) that occur over the acid sites. The results were consistent with experimental results using both catalysts. Based on the overall reaction, the apparent kinetic parameters were obtained and the results confirmed that the first dehydration step, which occurs over Brønsted acid sites, is the rate determining step. In addition, the structural features of catalysts appear to be one of the crucial factors that affect the kinetics of the reaction over acid sites. The HZSM-5 and ASPN-40 catalysts were deactivated to different degrees under same conditions. A kinetic equation for the deactivation, which is a function of product concentration, was found to be in good agreement with the experimental results. To elucidate the mechanism of catalyst deactivation, various characteristic analyses (BET, NH3-TPD, TPO, and 13C NMR) were employed. The changes in the properties of catalysts and the nature of the produced coke were analyzed. In the case of HZSM-5, the condensation of coke precursors is promoted within its narrow pore structures, which results in the rapid deactivation of the catalyst. In ASPN-40, less condensed carbonaceous compounds are observed and the deactivation is delayed due to the relatively uninterrupted diffusion of materials (reactants, products, or potential coke precursors).</description><subject>Acid catalysts</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Coke</subject><subject>Deactivation</subject><subject>Dehydration</subject><subject>Dehydration of glycerol</subject><subject>Glycerols</subject><subject>Kinetics</subject><subject>Mathematical models</subject><subject>Reaction kinetics</subject><issn>0926-3373</issn><issn>1873-3883</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><recordid>eNp9kD9PwzAQxS0EEqXwDRg8siTYsROnCxKq-CcqscBsOfa5cUnjYrtF-fakCmJkOt3pvXd3P4SuKckpodXtJlc7rVKTF4SWOWE54dUJmtFasIzVNTtFM7Ioqowxwc7RRYwbQkjBinqG4qvrITkdsbc4tYANtIMJKjnfH0frbtAQfIf9AQJW2hk8blLdEFPE3y61WPXY9QeIya3_XAaUTu4w9VvQrepd3OJmwNp_wiU6s6qLcPVb5-jj8eF9-Zyt3p5elverTDNRpWwBUBUVpaUhoLWli0ZQbnhjAUoOhS1ZYYmxnNuKc14qNaIQimtm68LWXLA5uplyd8F_7ccL5dZFDV2nevD7KKkQhIkxlIxSPkl18DEGsHIX3FaFQVIij4zlRk6M5ZGxJEyOjEfb3WSD8Y2DgyCjdtBrMC6ATtJ493_AD-ewiS8</recordid><startdate>20151001</startdate><enddate>20151001</enddate><creator>Park, Hongseok</creator><creator>Yun, Yang Sik</creator><creator>Kim, Tae Yong</creator><creator>Lee, Kyung Rok</creator><creator>Baek, Jayeon</creator><creator>Yi, Jongheop</creator><general>Elsevier B.V</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7SU</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>JG9</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20151001</creationdate><title>Kinetics of the dehydration of glycerol over acid catalysts with an investigation of deactivation mechanism by coke</title><author>Park, Hongseok ; Yun, Yang Sik ; Kim, Tae Yong ; Lee, Kyung Rok ; Baek, Jayeon ; Yi, Jongheop</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c376t-9ee626115d0eccf19b714d4bfee54e2f532f0df44f64445aa0167a4c3f82f8473</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><topic>Acid catalysts</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Coke</topic><topic>Deactivation</topic><topic>Dehydration</topic><topic>Dehydration of glycerol</topic><topic>Glycerols</topic><topic>Kinetics</topic><topic>Mathematical models</topic><topic>Reaction kinetics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Park, Hongseok</creatorcontrib><creatorcontrib>Yun, Yang Sik</creatorcontrib><creatorcontrib>Kim, Tae Yong</creatorcontrib><creatorcontrib>Lee, Kyung Rok</creatorcontrib><creatorcontrib>Baek, Jayeon</creatorcontrib><creatorcontrib>Yi, Jongheop</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Environmental Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Applied catalysis. B, Environmental</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Park, Hongseok</au><au>Yun, Yang Sik</au><au>Kim, Tae Yong</au><au>Lee, Kyung Rok</au><au>Baek, Jayeon</au><au>Yi, Jongheop</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetics of the dehydration of glycerol over acid catalysts with an investigation of deactivation mechanism by coke</atitle><jtitle>Applied catalysis. B, Environmental</jtitle><date>2015-10-01</date><risdate>2015</risdate><volume>176-177</volume><spage>1</spage><epage>10</epage><pages>1-10</pages><issn>0926-3373</issn><eissn>1873-3883</eissn><abstract>[Display omitted] •Kinetics for dehydration of glycerol considering deactivation is investigated.•The deactivation behavior is analyzed quantitatively and qualitatively•Characteristics of used catalysts are analyzed with time on stream.•Effects of hierarchical structure for retardation of deactivation. Kinetics for the dehydration of glycerol, taking deactivation into account, was investigated. HZSM-5 and ASPN-40 (aluminosilicophosphate nanosphere) catalysts were used in the studies. A kinetic model was established, based on the reaction mechanism, taking into account two parallel reactions (transformation of glycerol into acrolein or acetol) that occur over the acid sites. The results were consistent with experimental results using both catalysts. Based on the overall reaction, the apparent kinetic parameters were obtained and the results confirmed that the first dehydration step, which occurs over Brønsted acid sites, is the rate determining step. In addition, the structural features of catalysts appear to be one of the crucial factors that affect the kinetics of the reaction over acid sites. The HZSM-5 and ASPN-40 catalysts were deactivated to different degrees under same conditions. A kinetic equation for the deactivation, which is a function of product concentration, was found to be in good agreement with the experimental results. To elucidate the mechanism of catalyst deactivation, various characteristic analyses (BET, NH3-TPD, TPO, and 13C NMR) were employed. The changes in the properties of catalysts and the nature of the produced coke were analyzed. In the case of HZSM-5, the condensation of coke precursors is promoted within its narrow pore structures, which results in the rapid deactivation of the catalyst. In ASPN-40, less condensed carbonaceous compounds are observed and the deactivation is delayed due to the relatively uninterrupted diffusion of materials (reactants, products, or potential coke precursors).</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.apcatb.2015.03.046</doi><tpages>10</tpages></addata></record>
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subjects Acid catalysts
Catalysis
Catalysts
Coke
Deactivation
Dehydration
Dehydration of glycerol
Glycerols
Kinetics
Mathematical models
Reaction kinetics
title Kinetics of the dehydration of glycerol over acid catalysts with an investigation of deactivation mechanism by coke
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