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Catalytic reforming of lignite pyrolysis volatiles over sulfated HZSM-5: Significance of the introduced extra-framework Al species
[Display omitted] •Sulfated HZSM-5 zeolite was prepared by dealumination, realumination and sulfation.•The introduced extra-framework Al affected the textural-acid properties of catalysts.•Sulfation of catalyst after re-introduced extra-framework Al enhanced LAs production.•The highest LAs and lowes...
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Published in: | Fuel (Guildford) 2020-08, Vol.273, p.117789, Article 117789 |
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container_title | Fuel (Guildford) |
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creator | Zhao, Jing-Ping Cao, Jing-Pei Wei, Fu Feng, Xiao-Bo Yao, Nai-Yu Zhao, Yun-Peng Zhao, Ming Zhao, Xiao-Yan Zhang, Jian-Li Wei, Xian-Yong |
description | [Display omitted]
•Sulfated HZSM-5 zeolite was prepared by dealumination, realumination and sulfation.•The introduced extra-framework Al affected the textural-acid properties of catalysts.•Sulfation of catalyst after re-introduced extra-framework Al enhanced LAs production.•The highest LAs and lowest coke yield were produced over SO42−/DHZ5-A.
Sulfated HZSM-5 zeolite prepared by dealumination, realumination and sulfation was used as the active mesoporous materials to promote the formation of light aromatics during catalytic reforming of volatiles from Shengli lignite pyrolysis. The results show that HCl-dealumination significantly increased the total pore volume (especially mesopores) and average pore size while reducing acid strength and amount of acid sites. The incorporation of the extra-framework Al species to HZSM-5 combined with SO42− to form superacidic surface sulfate complex exhibited an increase in the yield of light aromatics and a decrease in the yield of coke in comparison with that of original HZSM-5. Among the modified catalysts, SO42−/DHZ5-A (introduced the calcined Al2O3 after HCl-dealumination and modified with (NH4)2SO4) with the acidity enhancement by sulfation obtained the maximum light aromatics yield of 27.3 mg/g and the lowest coke yield of 2.7%. The relationship between the physic-chemical properties of catalysts and the product distribution was proposed to understand the formation of light aromatics. |
doi_str_mv | 10.1016/j.fuel.2020.117789 |
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•Sulfated HZSM-5 zeolite was prepared by dealumination, realumination and sulfation.•The introduced extra-framework Al affected the textural-acid properties of catalysts.•Sulfation of catalyst after re-introduced extra-framework Al enhanced LAs production.•The highest LAs and lowest coke yield were produced over SO42−/DHZ5-A.
Sulfated HZSM-5 zeolite prepared by dealumination, realumination and sulfation was used as the active mesoporous materials to promote the formation of light aromatics during catalytic reforming of volatiles from Shengli lignite pyrolysis. The results show that HCl-dealumination significantly increased the total pore volume (especially mesopores) and average pore size while reducing acid strength and amount of acid sites. The incorporation of the extra-framework Al species to HZSM-5 combined with SO42− to form superacidic surface sulfate complex exhibited an increase in the yield of light aromatics and a decrease in the yield of coke in comparison with that of original HZSM-5. Among the modified catalysts, SO42−/DHZ5-A (introduced the calcined Al2O3 after HCl-dealumination and modified with (NH4)2SO4) with the acidity enhancement by sulfation obtained the maximum light aromatics yield of 27.3 mg/g and the lowest coke yield of 2.7%. The relationship between the physic-chemical properties of catalysts and the product distribution was proposed to understand the formation of light aromatics.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2020.117789</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Acidity ; Aluminum oxide ; Ammonium sulfate ; Aromatic compounds ; Catalysts ; Chemical properties ; Coke ; Extra-framework Al ; Introduced species ; Light aromatics ; Lignite ; Lignite pyrolysis ; Pore size ; Porosity ; Pyrolysis ; Reforming ; Sulfation ; Volatile compounds ; Volatiles ; Yield ; Zeolites</subject><ispartof>Fuel (Guildford), 2020-08, Vol.273, p.117789, Article 117789</ispartof><rights>2020 Elsevier Ltd</rights><rights>Copyright Elsevier BV Aug 1, 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c328t-8cba57c16b05363146ee68fee771ad28bbd11cf17b2001721aa0a2b121659a233</citedby><cites>FETCH-LOGICAL-c328t-8cba57c16b05363146ee68fee771ad28bbd11cf17b2001721aa0a2b121659a233</cites><orcidid>0000-0002-4482-8884 ; 0000-0002-1544-7441 ; 0000-0001-8120-0060</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27922,27923</link.rule.ids></links><search><creatorcontrib>Zhao, Jing-Ping</creatorcontrib><creatorcontrib>Cao, Jing-Pei</creatorcontrib><creatorcontrib>Wei, Fu</creatorcontrib><creatorcontrib>Feng, Xiao-Bo</creatorcontrib><creatorcontrib>Yao, Nai-Yu</creatorcontrib><creatorcontrib>Zhao, Yun-Peng</creatorcontrib><creatorcontrib>Zhao, Ming</creatorcontrib><creatorcontrib>Zhao, Xiao-Yan</creatorcontrib><creatorcontrib>Zhang, Jian-Li</creatorcontrib><creatorcontrib>Wei, Xian-Yong</creatorcontrib><title>Catalytic reforming of lignite pyrolysis volatiles over sulfated HZSM-5: Significance of the introduced extra-framework Al species</title><title>Fuel (Guildford)</title><description>[Display omitted]
•Sulfated HZSM-5 zeolite was prepared by dealumination, realumination and sulfation.•The introduced extra-framework Al affected the textural-acid properties of catalysts.•Sulfation of catalyst after re-introduced extra-framework Al enhanced LAs production.•The highest LAs and lowest coke yield were produced over SO42−/DHZ5-A.
Sulfated HZSM-5 zeolite prepared by dealumination, realumination and sulfation was used as the active mesoporous materials to promote the formation of light aromatics during catalytic reforming of volatiles from Shengli lignite pyrolysis. The results show that HCl-dealumination significantly increased the total pore volume (especially mesopores) and average pore size while reducing acid strength and amount of acid sites. The incorporation of the extra-framework Al species to HZSM-5 combined with SO42− to form superacidic surface sulfate complex exhibited an increase in the yield of light aromatics and a decrease in the yield of coke in comparison with that of original HZSM-5. Among the modified catalysts, SO42−/DHZ5-A (introduced the calcined Al2O3 after HCl-dealumination and modified with (NH4)2SO4) with the acidity enhancement by sulfation obtained the maximum light aromatics yield of 27.3 mg/g and the lowest coke yield of 2.7%. The relationship between the physic-chemical properties of catalysts and the product distribution was proposed to understand the formation of light aromatics.</description><subject>Acidity</subject><subject>Aluminum oxide</subject><subject>Ammonium sulfate</subject><subject>Aromatic compounds</subject><subject>Catalysts</subject><subject>Chemical properties</subject><subject>Coke</subject><subject>Extra-framework Al</subject><subject>Introduced species</subject><subject>Light aromatics</subject><subject>Lignite</subject><subject>Lignite pyrolysis</subject><subject>Pore size</subject><subject>Porosity</subject><subject>Pyrolysis</subject><subject>Reforming</subject><subject>Sulfation</subject><subject>Volatile compounds</subject><subject>Volatiles</subject><subject>Yield</subject><subject>Zeolites</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9kD9v2zAQxYmgAeK6-QKZCHSWw6P-UC66BEbbFHDQIcmShaCoY0qXFl2ScqI1n7wU3DnTAYf33t37EXIFbAUMmuvdyozoVpzxvAAh2vUZWUArykJAXX4gC5ZVBS8buCAfY9wxxkRbVwvytlFJuSlZTQMaH_Z2eKbeUGefB5uQHqbg3RRtpEfvVLIOI_VHDDSOzqiEPb19ur8r6i_0fnYYq9WgcU5Iv5HaIQXfjzrL8DUFVZig9vjiwx9642g8oLYYP5Fzo1zEy_9zSR6_f3vY3BbbXz9-bm62hS55m4pWd6oWGpqO1WVTQtUgNq1BFAJUz9uu6wG0AdHxXFZwUIop3gGHpl4rXpZL8vmUewj-74gxyZ0fw5BPSl5VrFqzVrCs4ieVDj7GzEQegt2rMElgcmYtd3JmLWfW8sQ6m76eTJj_P1oMMuZmGURvA-oke2_fs_8D_umJXA</recordid><startdate>20200801</startdate><enddate>20200801</enddate><creator>Zhao, Jing-Ping</creator><creator>Cao, Jing-Pei</creator><creator>Wei, Fu</creator><creator>Feng, Xiao-Bo</creator><creator>Yao, Nai-Yu</creator><creator>Zhao, Yun-Peng</creator><creator>Zhao, Ming</creator><creator>Zhao, Xiao-Yan</creator><creator>Zhang, Jian-Li</creator><creator>Wei, Xian-Yong</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope><orcidid>https://orcid.org/0000-0002-4482-8884</orcidid><orcidid>https://orcid.org/0000-0002-1544-7441</orcidid><orcidid>https://orcid.org/0000-0001-8120-0060</orcidid></search><sort><creationdate>20200801</creationdate><title>Catalytic reforming of lignite pyrolysis volatiles over sulfated HZSM-5: Significance of the introduced extra-framework Al species</title><author>Zhao, Jing-Ping ; Cao, Jing-Pei ; Wei, Fu ; Feng, Xiao-Bo ; Yao, Nai-Yu ; Zhao, Yun-Peng ; Zhao, Ming ; Zhao, Xiao-Yan ; Zhang, Jian-Li ; Wei, Xian-Yong</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c328t-8cba57c16b05363146ee68fee771ad28bbd11cf17b2001721aa0a2b121659a233</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Acidity</topic><topic>Aluminum oxide</topic><topic>Ammonium sulfate</topic><topic>Aromatic compounds</topic><topic>Catalysts</topic><topic>Chemical properties</topic><topic>Coke</topic><topic>Extra-framework Al</topic><topic>Introduced species</topic><topic>Light aromatics</topic><topic>Lignite</topic><topic>Lignite pyrolysis</topic><topic>Pore size</topic><topic>Porosity</topic><topic>Pyrolysis</topic><topic>Reforming</topic><topic>Sulfation</topic><topic>Volatile compounds</topic><topic>Volatiles</topic><topic>Yield</topic><topic>Zeolites</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Zhao, Jing-Ping</creatorcontrib><creatorcontrib>Cao, Jing-Pei</creatorcontrib><creatorcontrib>Wei, Fu</creatorcontrib><creatorcontrib>Feng, Xiao-Bo</creatorcontrib><creatorcontrib>Yao, Nai-Yu</creatorcontrib><creatorcontrib>Zhao, Yun-Peng</creatorcontrib><creatorcontrib>Zhao, Ming</creatorcontrib><creatorcontrib>Zhao, Xiao-Yan</creatorcontrib><creatorcontrib>Zhang, Jian-Li</creatorcontrib><creatorcontrib>Wei, Xian-Yong</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation 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>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Fuel (Guildford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Zhao, Jing-Ping</au><au>Cao, Jing-Pei</au><au>Wei, Fu</au><au>Feng, Xiao-Bo</au><au>Yao, Nai-Yu</au><au>Zhao, Yun-Peng</au><au>Zhao, Ming</au><au>Zhao, Xiao-Yan</au><au>Zhang, Jian-Li</au><au>Wei, Xian-Yong</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Catalytic reforming of lignite pyrolysis volatiles over sulfated HZSM-5: Significance of the introduced extra-framework Al species</atitle><jtitle>Fuel (Guildford)</jtitle><date>2020-08-01</date><risdate>2020</risdate><volume>273</volume><spage>117789</spage><pages>117789-</pages><artnum>117789</artnum><issn>0016-2361</issn><eissn>1873-7153</eissn><abstract>[Display omitted]
•Sulfated HZSM-5 zeolite was prepared by dealumination, realumination and sulfation.•The introduced extra-framework Al affected the textural-acid properties of catalysts.•Sulfation of catalyst after re-introduced extra-framework Al enhanced LAs production.•The highest LAs and lowest coke yield were produced over SO42−/DHZ5-A.
Sulfated HZSM-5 zeolite prepared by dealumination, realumination and sulfation was used as the active mesoporous materials to promote the formation of light aromatics during catalytic reforming of volatiles from Shengli lignite pyrolysis. The results show that HCl-dealumination significantly increased the total pore volume (especially mesopores) and average pore size while reducing acid strength and amount of acid sites. The incorporation of the extra-framework Al species to HZSM-5 combined with SO42− to form superacidic surface sulfate complex exhibited an increase in the yield of light aromatics and a decrease in the yield of coke in comparison with that of original HZSM-5. Among the modified catalysts, SO42−/DHZ5-A (introduced the calcined Al2O3 after HCl-dealumination and modified with (NH4)2SO4) with the acidity enhancement by sulfation obtained the maximum light aromatics yield of 27.3 mg/g and the lowest coke yield of 2.7%. The relationship between the physic-chemical properties of catalysts and the product distribution was proposed to understand the formation of light aromatics.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2020.117789</doi><orcidid>https://orcid.org/0000-0002-4482-8884</orcidid><orcidid>https://orcid.org/0000-0002-1544-7441</orcidid><orcidid>https://orcid.org/0000-0001-8120-0060</orcidid></addata></record> |
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subjects | Acidity Aluminum oxide Ammonium sulfate Aromatic compounds Catalysts Chemical properties Coke Extra-framework Al Introduced species Light aromatics Lignite Lignite pyrolysis Pore size Porosity Pyrolysis Reforming Sulfation Volatile compounds Volatiles Yield Zeolites |
title | Catalytic reforming of lignite pyrolysis volatiles over sulfated HZSM-5: Significance of the introduced extra-framework Al species |
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