Porosity roles of micro-mesostructured ZSM-5 in catalytic fast pyrolysis of cellulolytic enzyme lignin for aromatics
[Display omitted] •Cellulolytic enzyme lignin was utilized to produce aromatic-rich bio-oil in the CFP process.•Three types of micro-mesostructured ZSM-5 (core-shell, hierarchical, composites) were synthesized.•The morphology and structural parameters of different mesoporous structures were compared...
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creator | Sun, Haoran Luo, Zhongyang Wang, Wenbo Li, Simin Xue, Shuang |
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•Cellulolytic enzyme lignin was utilized to produce aromatic-rich bio-oil in the CFP process.•Three types of micro-mesostructured ZSM-5 (core-shell, hierarchical, composites) were synthesized.•The morphology and structural parameters of different mesoporous structures were compared in detail.•The relationship between mesopore distribution and catalytic effect was analyzed.•ZMA was the optimum to balance the aromatic yield and the distribution of products.
Cellulolytic enzyme lignin could be utilized to produce aromatic-rich bio-oil in the catalytic fast pyrolysis (CFP) process, in which strong-acidic ZSM-5 is often used as the catalyst. The introduction of mesopores into conventional ZSM-5 catalysts can improve the diffusion of heavy components and thus enable the modulation of pyrolysis products. To investigate the effect of mesoporous structure parameters on the diffusion of heavy phenols and the regulation of pyrolysis products by different types of pore structures, three different mesoporous ZSM-5 were prepared (core-shell, hierarchical, composites), with textural properties being compared in detail. The structural parameters were adopted to analyze the relationship between mesopores distribution and catalytic performance, revealing the significant effect of equivalent mesopore size. Among the prepared catalysts, a micro-mesostructured composite zeolite (ZMA) with internal hierarchical pores and ununiform mesolayer shell had a suitable mesostructure, of which the interconnected meso-channels improved the accessibility of inner acidic sites. Also, it was optimum to balance aromatic yield (above 7.5 wt%) and the product distribution (MAHs/PAHs approaching 6), revealing that its moderate equivalent pore size maintained a certain shape-selectivity to suppress PAHs formation. It was further shown that the applicable catalyst to lignin ratio (C/L) ranges differed with various mesostructures, as ZMA and hierarchical samples were suitable for higher and lower ratios, respectively. |
doi_str_mv | 10.1016/j.enconman.2021.114753 |
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•Cellulolytic enzyme lignin was utilized to produce aromatic-rich bio-oil in the CFP process.•Three types of micro-mesostructured ZSM-5 (core-shell, hierarchical, composites) were synthesized.•The morphology and structural parameters of different mesoporous structures were compared in detail.•The relationship between mesopore distribution and catalytic effect was analyzed.•ZMA was the optimum to balance the aromatic yield and the distribution of products.
Cellulolytic enzyme lignin could be utilized to produce aromatic-rich bio-oil in the catalytic fast pyrolysis (CFP) process, in which strong-acidic ZSM-5 is often used as the catalyst. The introduction of mesopores into conventional ZSM-5 catalysts can improve the diffusion of heavy components and thus enable the modulation of pyrolysis products. To investigate the effect of mesoporous structure parameters on the diffusion of heavy phenols and the regulation of pyrolysis products by different types of pore structures, three different mesoporous ZSM-5 were prepared (core-shell, hierarchical, composites), with textural properties being compared in detail. The structural parameters were adopted to analyze the relationship between mesopores distribution and catalytic performance, revealing the significant effect of equivalent mesopore size. Among the prepared catalysts, a micro-mesostructured composite zeolite (ZMA) with internal hierarchical pores and ununiform mesolayer shell had a suitable mesostructure, of which the interconnected meso-channels improved the accessibility of inner acidic sites. Also, it was optimum to balance aromatic yield (above 7.5 wt%) and the product distribution (MAHs/PAHs approaching 6), revealing that its moderate equivalent pore size maintained a certain shape-selectivity to suppress PAHs formation. It was further shown that the applicable catalyst to lignin ratio (C/L) ranges differed with various mesostructures, as ZMA and hierarchical samples were suitable for higher and lower ratios, respectively.</description><identifier>ISSN: 0196-8904</identifier><identifier>EISSN: 1879-2227</identifier><identifier>DOI: 10.1016/j.enconman.2021.114753</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Aromatic compounds ; Aromatics ; Catalysts ; Catalytic fast pyrolysis ; Channel pores ; Composite zeolite ; Diffusion ; Enzymes ; Equivalence ; Hierarchical ZSM-5 ; Lignin ; Mesostructure ; Parameters ; Phenols ; Pore size ; Porosity ; Pyrolysis ; Pyrolysis products ; Selectivity ; Zeolites</subject><ispartof>Energy conversion and management, 2021-11, Vol.247, p.114753, Article 114753</ispartof><rights>2021 Elsevier Ltd</rights><rights>Copyright Elsevier Science Ltd. Nov 1, 2021</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c340t-fd5391470790240f1e7a2647cdb7acc1ca52ecc354be4d550ec729975b4d4a083</citedby><cites>FETCH-LOGICAL-c340t-fd5391470790240f1e7a2647cdb7acc1ca52ecc354be4d550ec729975b4d4a083</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.enconman.2021.114753$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>Sun, Haoran</creatorcontrib><creatorcontrib>Luo, Zhongyang</creatorcontrib><creatorcontrib>Wang, Wenbo</creatorcontrib><creatorcontrib>Li, Simin</creatorcontrib><creatorcontrib>Xue, Shuang</creatorcontrib><title>Porosity roles of micro-mesostructured ZSM-5 in catalytic fast pyrolysis of cellulolytic enzyme lignin for aromatics</title><title>Energy conversion and management</title><description>[Display omitted]
•Cellulolytic enzyme lignin was utilized to produce aromatic-rich bio-oil in the CFP process.•Three types of micro-mesostructured ZSM-5 (core-shell, hierarchical, composites) were synthesized.•The morphology and structural parameters of different mesoporous structures were compared in detail.•The relationship between mesopore distribution and catalytic effect was analyzed.•ZMA was the optimum to balance the aromatic yield and the distribution of products.
Cellulolytic enzyme lignin could be utilized to produce aromatic-rich bio-oil in the catalytic fast pyrolysis (CFP) process, in which strong-acidic ZSM-5 is often used as the catalyst. The introduction of mesopores into conventional ZSM-5 catalysts can improve the diffusion of heavy components and thus enable the modulation of pyrolysis products. To investigate the effect of mesoporous structure parameters on the diffusion of heavy phenols and the regulation of pyrolysis products by different types of pore structures, three different mesoporous ZSM-5 were prepared (core-shell, hierarchical, composites), with textural properties being compared in detail. The structural parameters were adopted to analyze the relationship between mesopores distribution and catalytic performance, revealing the significant effect of equivalent mesopore size. Among the prepared catalysts, a micro-mesostructured composite zeolite (ZMA) with internal hierarchical pores and ununiform mesolayer shell had a suitable mesostructure, of which the interconnected meso-channels improved the accessibility of inner acidic sites. Also, it was optimum to balance aromatic yield (above 7.5 wt%) and the product distribution (MAHs/PAHs approaching 6), revealing that its moderate equivalent pore size maintained a certain shape-selectivity to suppress PAHs formation. It was further shown that the applicable catalyst to lignin ratio (C/L) ranges differed with various mesostructures, as ZMA and hierarchical samples were suitable for higher and lower ratios, respectively.</description><subject>Aromatic compounds</subject><subject>Aromatics</subject><subject>Catalysts</subject><subject>Catalytic fast pyrolysis</subject><subject>Channel pores</subject><subject>Composite zeolite</subject><subject>Diffusion</subject><subject>Enzymes</subject><subject>Equivalence</subject><subject>Hierarchical ZSM-5</subject><subject>Lignin</subject><subject>Mesostructure</subject><subject>Parameters</subject><subject>Phenols</subject><subject>Pore size</subject><subject>Porosity</subject><subject>Pyrolysis</subject><subject>Pyrolysis products</subject><subject>Selectivity</subject><subject>Zeolites</subject><issn>0196-8904</issn><issn>1879-2227</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNqFkEFr3DAQhUVpoZtN_0IR5GxnJEvW-tawpElgQwJpL70IrTwuMra1keSC--urxMm5MDCHed8b3iPkK4OSAasv-xIn66fRTCUHzkrGhJLVB7JhO9UUnHP1kWyANXWxa0B8Jmcx9gBQSag3JD364KNLCw1-wEh9R0dngy9GjD6mMNs0B2zpr6f7QlI3UWuSGZbkLO1MTPS0ZG6J7pW0OAzz4NczTn-XEengfk8Z63ygJvjR5FM8J586M0T88ra35Of36x_72-LwcHO3vzoUthKQiq6VVZPDgGqAC-gYKsNroWx7VMZaZo3kaG0lxRFFKyWgVbxplDyKVhjYVVtysfqegn-eMSbd-zlM-aXmsqlYHpBZVa-qHDvGgJ0-BTeasGgG-qVh3ev3hvVLw3ptOIPfVhBzhj8Og47WZSW2LqBNuvXufxb_AKIHig0</recordid><startdate>20211101</startdate><enddate>20211101</enddate><creator>Sun, Haoran</creator><creator>Luo, Zhongyang</creator><creator>Wang, Wenbo</creator><creator>Li, Simin</creator><creator>Xue, Shuang</creator><general>Elsevier Ltd</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope></search><sort><creationdate>20211101</creationdate><title>Porosity roles of micro-mesostructured ZSM-5 in catalytic fast pyrolysis of cellulolytic enzyme lignin for aromatics</title><author>Sun, Haoran ; Luo, Zhongyang ; Wang, Wenbo ; Li, Simin ; Xue, Shuang</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c340t-fd5391470790240f1e7a2647cdb7acc1ca52ecc354be4d550ec729975b4d4a083</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Aromatic compounds</topic><topic>Aromatics</topic><topic>Catalysts</topic><topic>Catalytic fast pyrolysis</topic><topic>Channel pores</topic><topic>Composite zeolite</topic><topic>Diffusion</topic><topic>Enzymes</topic><topic>Equivalence</topic><topic>Hierarchical ZSM-5</topic><topic>Lignin</topic><topic>Mesostructure</topic><topic>Parameters</topic><topic>Phenols</topic><topic>Pore size</topic><topic>Porosity</topic><topic>Pyrolysis</topic><topic>Pyrolysis products</topic><topic>Selectivity</topic><topic>Zeolites</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Sun, Haoran</creatorcontrib><creatorcontrib>Luo, Zhongyang</creatorcontrib><creatorcontrib>Wang, Wenbo</creatorcontrib><creatorcontrib>Li, Simin</creatorcontrib><creatorcontrib>Xue, Shuang</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>Energy conversion and management</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Sun, Haoran</au><au>Luo, Zhongyang</au><au>Wang, Wenbo</au><au>Li, Simin</au><au>Xue, Shuang</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Porosity roles of micro-mesostructured ZSM-5 in catalytic fast pyrolysis of cellulolytic enzyme lignin for aromatics</atitle><jtitle>Energy conversion and management</jtitle><date>2021-11-01</date><risdate>2021</risdate><volume>247</volume><spage>114753</spage><pages>114753-</pages><artnum>114753</artnum><issn>0196-8904</issn><eissn>1879-2227</eissn><abstract>[Display omitted]
•Cellulolytic enzyme lignin was utilized to produce aromatic-rich bio-oil in the CFP process.•Three types of micro-mesostructured ZSM-5 (core-shell, hierarchical, composites) were synthesized.•The morphology and structural parameters of different mesoporous structures were compared in detail.•The relationship between mesopore distribution and catalytic effect was analyzed.•ZMA was the optimum to balance the aromatic yield and the distribution of products.
Cellulolytic enzyme lignin could be utilized to produce aromatic-rich bio-oil in the catalytic fast pyrolysis (CFP) process, in which strong-acidic ZSM-5 is often used as the catalyst. The introduction of mesopores into conventional ZSM-5 catalysts can improve the diffusion of heavy components and thus enable the modulation of pyrolysis products. To investigate the effect of mesoporous structure parameters on the diffusion of heavy phenols and the regulation of pyrolysis products by different types of pore structures, three different mesoporous ZSM-5 were prepared (core-shell, hierarchical, composites), with textural properties being compared in detail. The structural parameters were adopted to analyze the relationship between mesopores distribution and catalytic performance, revealing the significant effect of equivalent mesopore size. Among the prepared catalysts, a micro-mesostructured composite zeolite (ZMA) with internal hierarchical pores and ununiform mesolayer shell had a suitable mesostructure, of which the interconnected meso-channels improved the accessibility of inner acidic sites. Also, it was optimum to balance aromatic yield (above 7.5 wt%) and the product distribution (MAHs/PAHs approaching 6), revealing that its moderate equivalent pore size maintained a certain shape-selectivity to suppress PAHs formation. It was further shown that the applicable catalyst to lignin ratio (C/L) ranges differed with various mesostructures, as ZMA and hierarchical samples were suitable for higher and lower ratios, respectively.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.enconman.2021.114753</doi></addata></record> |
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subjects | Aromatic compounds Aromatics Catalysts Catalytic fast pyrolysis Channel pores Composite zeolite Diffusion Enzymes Equivalence Hierarchical ZSM-5 Lignin Mesostructure Parameters Phenols Pore size Porosity Pyrolysis Pyrolysis products Selectivity Zeolites |
title | Porosity roles of micro-mesostructured ZSM-5 in catalytic fast pyrolysis of cellulolytic enzyme lignin for aromatics |
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