Ex-situ catalytic fast pyrolysis of biomass over HZSM-5 in a two-stage fluidized-bed/fixed-bed combination reactor

•Ex-situ catalytic fast pyrolysis (CFP) was studied in a two-stage bench scale device.•Ex-situ and in-situ CFP gave a similar carbon yield of aromatics+olefins.•Ex-situ CFP produced significantly more olefins than in-situ CFP.•High pyrolysis temperature generated significantly less coke.•High cataly...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Bioresource technology 2017-11, Vol.243, p.1133-1140
Hauptverfasser: Hu, Changsong, Xiao, Rui, Zhang, Huiyan
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 1140
container_issue
container_start_page 1133
container_title Bioresource technology
container_volume 243
creator Hu, Changsong
Xiao, Rui
Zhang, Huiyan
description •Ex-situ catalytic fast pyrolysis (CFP) was studied in a two-stage bench scale device.•Ex-situ and in-situ CFP gave a similar carbon yield of aromatics+olefins.•Ex-situ CFP produced significantly more olefins than in-situ CFP.•High pyrolysis temperature generated significantly less coke.•High catalysis temperature led to a boost in ethylene and benzene selectivities. Ex-situ and in-situ catalytic fast pyrolysis (CFP) of biomass over HZSM-5 were compared in a two-stage fluidized-bed/fixed-bed combination reactor. Ex-situ CFP gave a similar carbon yield of aromatics+olefins (∼20%) with in-situ CFP but produced much more olefins (10.3% vs. 5.8%) and less char+coke (42.7% vs. 48.4%). The effects of weight hourly space velocity (WHSV), carrier gas flow rate, pyrolysis temperature and catalysis temperature on product distribution in ex-situ CFP were further studied. The maximum carbon yield of aromatics+olefins (21.7%) was obtained at pyrolysis temperature of 550°C and catalysis temperature of 600°C with the highest carrier gas flow rate (1.2L/min) and WHSV of 1.33h−1. Obviously less coke was generated at higher pyrolysis temperature. When catalysis temperature increased to 700°C, ethylene and benzene carbon selectivities boosted to 79.4% and 60.5%, respectively.
doi_str_mv 10.1016/j.biortech.2017.07.011
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1925515504</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0960852417310970</els_id><sourcerecordid>1925515504</sourcerecordid><originalsourceid>FETCH-LOGICAL-c519t-b7fe2c7f1d3d409881eab53ecdbdb827e4243946998d2d2a5bd96c457f068093</originalsourceid><addsrcrecordid>eNqFkE9P3DAQxa2qVVlovwLysRcvthPH8a0I0YIE4gCnXiz_GbdeJfHWdmC3n75BC1yRRpp3eG-e5ofQKaNrRll3tlnbmHIF92fNKZNrugxjH9CK9bIhXMnuI1pR1VHSC94eoeNSNpTShkn-GR3xXnYt43KF8uWOlFhn7Ew1w75Gh4MpFW_3OQ37EgtOAS9VoymLfISMr37d3xKB44QNrk-JlGp-Aw7DHH38B55Y8Gch7g4KuzTaOJka04QzGFdT_oI-BTMU-PqyT9DDj8uHiytyc_fz-uL8hjjBVCVWBuBOBuYb31LV9wyMFQ04b73tuYSWt41qO6V6zz03wnrVuVbIQLuequYEfTuc3eb0d4ZS9RiLg2EwE6S5aKa4EEwI2i7W7mB1OZWSIehtjqPJe82ofsatN_oVt37GrekyjC3B05eO2Y7g32KvfBfD94MBlkcfI2RdXITJgY8ZXNU-xfc6_gPgU5Wk</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1925515504</pqid></control><display><type>article</type><title>Ex-situ catalytic fast pyrolysis of biomass over HZSM-5 in a two-stage fluidized-bed/fixed-bed combination reactor</title><source>MEDLINE</source><source>Access via ScienceDirect (Elsevier)</source><creator>Hu, Changsong ; Xiao, Rui ; Zhang, Huiyan</creator><creatorcontrib>Hu, Changsong ; Xiao, Rui ; Zhang, Huiyan</creatorcontrib><description>•Ex-situ catalytic fast pyrolysis (CFP) was studied in a two-stage bench scale device.•Ex-situ and in-situ CFP gave a similar carbon yield of aromatics+olefins.•Ex-situ CFP produced significantly more olefins than in-situ CFP.•High pyrolysis temperature generated significantly less coke.•High catalysis temperature led to a boost in ethylene and benzene selectivities. Ex-situ and in-situ catalytic fast pyrolysis (CFP) of biomass over HZSM-5 were compared in a two-stage fluidized-bed/fixed-bed combination reactor. Ex-situ CFP gave a similar carbon yield of aromatics+olefins (∼20%) with in-situ CFP but produced much more olefins (10.3% vs. 5.8%) and less char+coke (42.7% vs. 48.4%). The effects of weight hourly space velocity (WHSV), carrier gas flow rate, pyrolysis temperature and catalysis temperature on product distribution in ex-situ CFP were further studied. The maximum carbon yield of aromatics+olefins (21.7%) was obtained at pyrolysis temperature of 550°C and catalysis temperature of 600°C with the highest carrier gas flow rate (1.2L/min) and WHSV of 1.33h−1. Obviously less coke was generated at higher pyrolysis temperature. When catalysis temperature increased to 700°C, ethylene and benzene carbon selectivities boosted to 79.4% and 60.5%, respectively.</description><identifier>ISSN: 0960-8524</identifier><identifier>EISSN: 1873-2976</identifier><identifier>DOI: 10.1016/j.biortech.2017.07.011</identifier><identifier>PMID: 28764127</identifier><language>eng</language><publisher>England: Elsevier Ltd</publisher><subject>Alkenes ; Biomass ; Catalysis ; Catalytic fast pyrolysis ; Ex-situ ; Fluidized bed ; Hot Temperature ; HZSM-5 ; Olefins ; Temperature</subject><ispartof>Bioresource technology, 2017-11, Vol.243, p.1133-1140</ispartof><rights>2017 Elsevier Ltd</rights><rights>Copyright © 2017 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c519t-b7fe2c7f1d3d409881eab53ecdbdb827e4243946998d2d2a5bd96c457f068093</citedby><cites>FETCH-LOGICAL-c519t-b7fe2c7f1d3d409881eab53ecdbdb827e4243946998d2d2a5bd96c457f068093</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.biortech.2017.07.011$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/28764127$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Hu, Changsong</creatorcontrib><creatorcontrib>Xiao, Rui</creatorcontrib><creatorcontrib>Zhang, Huiyan</creatorcontrib><title>Ex-situ catalytic fast pyrolysis of biomass over HZSM-5 in a two-stage fluidized-bed/fixed-bed combination reactor</title><title>Bioresource technology</title><addtitle>Bioresour Technol</addtitle><description>•Ex-situ catalytic fast pyrolysis (CFP) was studied in a two-stage bench scale device.•Ex-situ and in-situ CFP gave a similar carbon yield of aromatics+olefins.•Ex-situ CFP produced significantly more olefins than in-situ CFP.•High pyrolysis temperature generated significantly less coke.•High catalysis temperature led to a boost in ethylene and benzene selectivities. Ex-situ and in-situ catalytic fast pyrolysis (CFP) of biomass over HZSM-5 were compared in a two-stage fluidized-bed/fixed-bed combination reactor. Ex-situ CFP gave a similar carbon yield of aromatics+olefins (∼20%) with in-situ CFP but produced much more olefins (10.3% vs. 5.8%) and less char+coke (42.7% vs. 48.4%). The effects of weight hourly space velocity (WHSV), carrier gas flow rate, pyrolysis temperature and catalysis temperature on product distribution in ex-situ CFP were further studied. The maximum carbon yield of aromatics+olefins (21.7%) was obtained at pyrolysis temperature of 550°C and catalysis temperature of 600°C with the highest carrier gas flow rate (1.2L/min) and WHSV of 1.33h−1. Obviously less coke was generated at higher pyrolysis temperature. When catalysis temperature increased to 700°C, ethylene and benzene carbon selectivities boosted to 79.4% and 60.5%, respectively.</description><subject>Alkenes</subject><subject>Biomass</subject><subject>Catalysis</subject><subject>Catalytic fast pyrolysis</subject><subject>Ex-situ</subject><subject>Fluidized bed</subject><subject>Hot Temperature</subject><subject>HZSM-5</subject><subject>Olefins</subject><subject>Temperature</subject><issn>0960-8524</issn><issn>1873-2976</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkE9P3DAQxa2qVVlovwLysRcvthPH8a0I0YIE4gCnXiz_GbdeJfHWdmC3n75BC1yRRpp3eG-e5ofQKaNrRll3tlnbmHIF92fNKZNrugxjH9CK9bIhXMnuI1pR1VHSC94eoeNSNpTShkn-GR3xXnYt43KF8uWOlFhn7Ew1w75Gh4MpFW_3OQ37EgtOAS9VoymLfISMr37d3xKB44QNrk-JlGp-Aw7DHH38B55Y8Gch7g4KuzTaOJka04QzGFdT_oI-BTMU-PqyT9DDj8uHiytyc_fz-uL8hjjBVCVWBuBOBuYb31LV9wyMFQ04b73tuYSWt41qO6V6zz03wnrVuVbIQLuequYEfTuc3eb0d4ZS9RiLg2EwE6S5aKa4EEwI2i7W7mB1OZWSIehtjqPJe82ofsatN_oVt37GrekyjC3B05eO2Y7g32KvfBfD94MBlkcfI2RdXITJgY8ZXNU-xfc6_gPgU5Wk</recordid><startdate>20171101</startdate><enddate>20171101</enddate><creator>Hu, Changsong</creator><creator>Xiao, Rui</creator><creator>Zhang, Huiyan</creator><general>Elsevier Ltd</general><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope></search><sort><creationdate>20171101</creationdate><title>Ex-situ catalytic fast pyrolysis of biomass over HZSM-5 in a two-stage fluidized-bed/fixed-bed combination reactor</title><author>Hu, Changsong ; Xiao, Rui ; Zhang, Huiyan</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c519t-b7fe2c7f1d3d409881eab53ecdbdb827e4243946998d2d2a5bd96c457f068093</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Alkenes</topic><topic>Biomass</topic><topic>Catalysis</topic><topic>Catalytic fast pyrolysis</topic><topic>Ex-situ</topic><topic>Fluidized bed</topic><topic>Hot Temperature</topic><topic>HZSM-5</topic><topic>Olefins</topic><topic>Temperature</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Hu, Changsong</creatorcontrib><creatorcontrib>Xiao, Rui</creatorcontrib><creatorcontrib>Zhang, Huiyan</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><jtitle>Bioresource technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Hu, Changsong</au><au>Xiao, Rui</au><au>Zhang, Huiyan</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Ex-situ catalytic fast pyrolysis of biomass over HZSM-5 in a two-stage fluidized-bed/fixed-bed combination reactor</atitle><jtitle>Bioresource technology</jtitle><addtitle>Bioresour Technol</addtitle><date>2017-11-01</date><risdate>2017</risdate><volume>243</volume><spage>1133</spage><epage>1140</epage><pages>1133-1140</pages><issn>0960-8524</issn><eissn>1873-2976</eissn><abstract>•Ex-situ catalytic fast pyrolysis (CFP) was studied in a two-stage bench scale device.•Ex-situ and in-situ CFP gave a similar carbon yield of aromatics+olefins.•Ex-situ CFP produced significantly more olefins than in-situ CFP.•High pyrolysis temperature generated significantly less coke.•High catalysis temperature led to a boost in ethylene and benzene selectivities. Ex-situ and in-situ catalytic fast pyrolysis (CFP) of biomass over HZSM-5 were compared in a two-stage fluidized-bed/fixed-bed combination reactor. Ex-situ CFP gave a similar carbon yield of aromatics+olefins (∼20%) with in-situ CFP but produced much more olefins (10.3% vs. 5.8%) and less char+coke (42.7% vs. 48.4%). The effects of weight hourly space velocity (WHSV), carrier gas flow rate, pyrolysis temperature and catalysis temperature on product distribution in ex-situ CFP were further studied. The maximum carbon yield of aromatics+olefins (21.7%) was obtained at pyrolysis temperature of 550°C and catalysis temperature of 600°C with the highest carrier gas flow rate (1.2L/min) and WHSV of 1.33h−1. Obviously less coke was generated at higher pyrolysis temperature. When catalysis temperature increased to 700°C, ethylene and benzene carbon selectivities boosted to 79.4% and 60.5%, respectively.</abstract><cop>England</cop><pub>Elsevier Ltd</pub><pmid>28764127</pmid><doi>10.1016/j.biortech.2017.07.011</doi><tpages>8</tpages><oa>free_for_read</oa></addata></record>
fulltext fulltext
identifier ISSN: 0960-8524
ispartof Bioresource technology, 2017-11, Vol.243, p.1133-1140
issn 0960-8524
1873-2976
language eng
recordid cdi_proquest_miscellaneous_1925515504
source MEDLINE; Access via ScienceDirect (Elsevier)
subjects Alkenes
Biomass
Catalysis
Catalytic fast pyrolysis
Ex-situ
Fluidized bed
Hot Temperature
HZSM-5
Olefins
Temperature
title Ex-situ catalytic fast pyrolysis of biomass over HZSM-5 in a two-stage fluidized-bed/fixed-bed combination reactor
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-28T10%3A55%3A48IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Ex-situ%20catalytic%20fast%20pyrolysis%20of%20biomass%20over%20HZSM-5%20in%20a%20two-stage%20fluidized-bed/fixed-bed%20combination%20reactor&rft.jtitle=Bioresource%20technology&rft.au=Hu,%20Changsong&rft.date=2017-11-01&rft.volume=243&rft.spage=1133&rft.epage=1140&rft.pages=1133-1140&rft.issn=0960-8524&rft.eissn=1873-2976&rft_id=info:doi/10.1016/j.biortech.2017.07.011&rft_dat=%3Cproquest_cross%3E1925515504%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1925515504&rft_id=info:pmid/28764127&rft_els_id=S0960852417310970&rfr_iscdi=true