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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
Main Authors: 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
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cited_by cdi_FETCH-LOGICAL-c328t-8cba57c16b05363146ee68fee771ad28bbd11cf17b2001721aa0a2b121659a233
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container_start_page 117789
container_title Fuel (Guildford)
container_volume 273
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 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%. 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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%. 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1873-7153
language eng
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source ScienceDirect Freedom Collection
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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