Pyrolysis of pine wood in a slowly heating fixed-bed reactor: Potassium carbonate versus calcium hydroxide as a catalyst

Catalytic pyrolysis of pine wood was carried out in a fixed-bed reactor heated slowly from room temperature to 700 °C under a stream of purging argon to examine the effects of the physically mixed K 2CO 3 or Ca(OH) 2 on the pyrolysis behaviors. K 2CO 3 demonstrated a stronger catalysis for decomposi...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Fuel processing technology 2010-08, Vol.91 (8), p.942-950
Hauptverfasser: Wang, Zhenya, Wang, Fu, Cao, Jianqin, Wang, Jie
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 950
container_issue 8
container_start_page 942
container_title Fuel processing technology
container_volume 91
creator Wang, Zhenya
Wang, Fu
Cao, Jianqin
Wang, Jie
description Catalytic pyrolysis of pine wood was carried out in a fixed-bed reactor heated slowly from room temperature to 700 °C under a stream of purging argon to examine the effects of the physically mixed K 2CO 3 or Ca(OH) 2 on the pyrolysis behaviors. K 2CO 3 demonstrated a stronger catalysis for decomposition of hemicellulose, cellulose and lignin constituents, leading to the reduced yield of liquid product in conjunction with the increased yields of gaseous and char products because of the promoted secondary reactions of liquid product. With the addition of 17.7 wt.% of K 2CO 3, none of saccharides, aldehydes and alcohols was formed and the formation of acids, furans and guaiacols was substantially reduced, whereas the yields of alkanes and phenols were increased. Potassium led to an increase in the cumulative yields of H 2, CO 2 and CO at 700 °C. Ca(OH) 2 somewhat promoted the decomposition of cellulose and lignin constituents, and the effect of Ca(OH) 2 on the yields of liquid and char was opposite to that of K 2CO 3. With the addition of 22.2 wt.% Ca(OH) 2, some groups of liquid product such as acids and aldehydes disappeared completely and the yields of saccharides, furans and guaiacols were somewhat reduced, while the yield of alcohols was remarkably increased in contrast to the result of K 2CO 3. The addition of Ca(OH) 2 did not significantly change the total yield of gaseous product at 700 °C but enhanced the yield of H 2.
doi_str_mv 10.1016/j.fuproc.2009.09.015
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_753682103</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0378382009002926</els_id><sourcerecordid>753682103</sourcerecordid><originalsourceid>FETCH-LOGICAL-c434t-87f11421f767e72597f49f580ae895469b980244f936ac35ba678f6c02b142173</originalsourceid><addsrcrecordid>eNp9UE2LFDEQDaLguPoPPOQinnrMR3cn8SDIsn7AgnvQc0inK26Gns6YSu9O_3vTzOJRKCioeq_eq0fIW872nPH-w2EfllNOfi8YM_utePeM7LhWslFc6-dkx6TSjdSCvSSvEA-Msa4zakfOd2tO04oRaQr0FGegjymNNM7UUZzS47TSe3Alzr9piGcYmwFGmsH5kvJHepeKQ4zLkXqXhzS7AvQBMi5YB5PfFvfrmNM5jkAd1pveFVf1ymvyIrgJ4c1TvyK_vtz8vP7W3P74-v36823jW9mWRqvAeSt4UL0CJarn0JrQaeZAm67tzWA0E20bjOydl93geqVD75kYNpqSV-T95W4N6M8CWOwxoodpcjOkBa3qZK8FZ7Ii2wvS54SYIdhTjkeXV8uZ3XK2B3vJ2W452614V2nvngQc1p9DdrOP-I8rhDFK9puRTxcc1G8fImSLPsLsYYwZfLFjiv8X-gu-T5ZR</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>753682103</pqid></control><display><type>article</type><title>Pyrolysis of pine wood in a slowly heating fixed-bed reactor: Potassium carbonate versus calcium hydroxide as a catalyst</title><source>Access via ScienceDirect (Elsevier)</source><creator>Wang, Zhenya ; Wang, Fu ; Cao, Jianqin ; Wang, Jie</creator><creatorcontrib>Wang, Zhenya ; Wang, Fu ; Cao, Jianqin ; Wang, Jie</creatorcontrib><description>Catalytic pyrolysis of pine wood was carried out in a fixed-bed reactor heated slowly from room temperature to 700 °C under a stream of purging argon to examine the effects of the physically mixed K 2CO 3 or Ca(OH) 2 on the pyrolysis behaviors. K 2CO 3 demonstrated a stronger catalysis for decomposition of hemicellulose, cellulose and lignin constituents, leading to the reduced yield of liquid product in conjunction with the increased yields of gaseous and char products because of the promoted secondary reactions of liquid product. With the addition of 17.7 wt.% of K 2CO 3, none of saccharides, aldehydes and alcohols was formed and the formation of acids, furans and guaiacols was substantially reduced, whereas the yields of alkanes and phenols were increased. Potassium led to an increase in the cumulative yields of H 2, CO 2 and CO at 700 °C. Ca(OH) 2 somewhat promoted the decomposition of cellulose and lignin constituents, and the effect of Ca(OH) 2 on the yields of liquid and char was opposite to that of K 2CO 3. With the addition of 22.2 wt.% Ca(OH) 2, some groups of liquid product such as acids and aldehydes disappeared completely and the yields of saccharides, furans and guaiacols were somewhat reduced, while the yield of alcohols was remarkably increased in contrast to the result of K 2CO 3. The addition of Ca(OH) 2 did not significantly change the total yield of gaseous product at 700 °C but enhanced the yield of H 2.</description><identifier>ISSN: 0378-3820</identifier><identifier>EISSN: 1873-7188</identifier><identifier>DOI: 10.1016/j.fuproc.2009.09.015</identifier><identifier>CODEN: FPTEDY</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Ca(OH) 2 ; Catalytic pyrolysis ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Fuels ; K 2CO 3 ; Pine wood</subject><ispartof>Fuel processing technology, 2010-08, Vol.91 (8), p.942-950</ispartof><rights>2009 Elsevier B.V.</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c434t-87f11421f767e72597f49f580ae895469b980244f936ac35ba678f6c02b142173</citedby><cites>FETCH-LOGICAL-c434t-87f11421f767e72597f49f580ae895469b980244f936ac35ba678f6c02b142173</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.fuproc.2009.09.015$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>309,310,314,780,784,789,790,3550,23930,23931,25140,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=22997367$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Wang, Zhenya</creatorcontrib><creatorcontrib>Wang, Fu</creatorcontrib><creatorcontrib>Cao, Jianqin</creatorcontrib><creatorcontrib>Wang, Jie</creatorcontrib><title>Pyrolysis of pine wood in a slowly heating fixed-bed reactor: Potassium carbonate versus calcium hydroxide as a catalyst</title><title>Fuel processing technology</title><description>Catalytic pyrolysis of pine wood was carried out in a fixed-bed reactor heated slowly from room temperature to 700 °C under a stream of purging argon to examine the effects of the physically mixed K 2CO 3 or Ca(OH) 2 on the pyrolysis behaviors. K 2CO 3 demonstrated a stronger catalysis for decomposition of hemicellulose, cellulose and lignin constituents, leading to the reduced yield of liquid product in conjunction with the increased yields of gaseous and char products because of the promoted secondary reactions of liquid product. With the addition of 17.7 wt.% of K 2CO 3, none of saccharides, aldehydes and alcohols was formed and the formation of acids, furans and guaiacols was substantially reduced, whereas the yields of alkanes and phenols were increased. Potassium led to an increase in the cumulative yields of H 2, CO 2 and CO at 700 °C. Ca(OH) 2 somewhat promoted the decomposition of cellulose and lignin constituents, and the effect of Ca(OH) 2 on the yields of liquid and char was opposite to that of K 2CO 3. With the addition of 22.2 wt.% Ca(OH) 2, some groups of liquid product such as acids and aldehydes disappeared completely and the yields of saccharides, furans and guaiacols were somewhat reduced, while the yield of alcohols was remarkably increased in contrast to the result of K 2CO 3. The addition of Ca(OH) 2 did not significantly change the total yield of gaseous product at 700 °C but enhanced the yield of H 2.</description><subject>Applied sciences</subject><subject>Ca(OH) 2</subject><subject>Catalytic pyrolysis</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>K 2CO 3</subject><subject>Pine wood</subject><issn>0378-3820</issn><issn>1873-7188</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNp9UE2LFDEQDaLguPoPPOQinnrMR3cn8SDIsn7AgnvQc0inK26Gns6YSu9O_3vTzOJRKCioeq_eq0fIW872nPH-w2EfllNOfi8YM_utePeM7LhWslFc6-dkx6TSjdSCvSSvEA-Msa4zakfOd2tO04oRaQr0FGegjymNNM7UUZzS47TSe3Alzr9piGcYmwFGmsH5kvJHepeKQ4zLkXqXhzS7AvQBMi5YB5PfFvfrmNM5jkAd1pveFVf1ymvyIrgJ4c1TvyK_vtz8vP7W3P74-v36823jW9mWRqvAeSt4UL0CJarn0JrQaeZAm67tzWA0E20bjOydl93geqVD75kYNpqSV-T95W4N6M8CWOwxoodpcjOkBa3qZK8FZ7Ii2wvS54SYIdhTjkeXV8uZ3XK2B3vJ2W452614V2nvngQc1p9DdrOP-I8rhDFK9puRTxcc1G8fImSLPsLsYYwZfLFjiv8X-gu-T5ZR</recordid><startdate>20100801</startdate><enddate>20100801</enddate><creator>Wang, Zhenya</creator><creator>Wang, Fu</creator><creator>Cao, Jianqin</creator><creator>Wang, Jie</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope></search><sort><creationdate>20100801</creationdate><title>Pyrolysis of pine wood in a slowly heating fixed-bed reactor: Potassium carbonate versus calcium hydroxide as a catalyst</title><author>Wang, Zhenya ; Wang, Fu ; Cao, Jianqin ; Wang, Jie</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c434t-87f11421f767e72597f49f580ae895469b980244f936ac35ba678f6c02b142173</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Applied sciences</topic><topic>Ca(OH) 2</topic><topic>Catalytic pyrolysis</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Fuels</topic><topic>K 2CO 3</topic><topic>Pine wood</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Wang, Zhenya</creatorcontrib><creatorcontrib>Wang, Fu</creatorcontrib><creatorcontrib>Cao, Jianqin</creatorcontrib><creatorcontrib>Wang, Jie</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><jtitle>Fuel processing technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Wang, Zhenya</au><au>Wang, Fu</au><au>Cao, Jianqin</au><au>Wang, Jie</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Pyrolysis of pine wood in a slowly heating fixed-bed reactor: Potassium carbonate versus calcium hydroxide as a catalyst</atitle><jtitle>Fuel processing technology</jtitle><date>2010-08-01</date><risdate>2010</risdate><volume>91</volume><issue>8</issue><spage>942</spage><epage>950</epage><pages>942-950</pages><issn>0378-3820</issn><eissn>1873-7188</eissn><coden>FPTEDY</coden><abstract>Catalytic pyrolysis of pine wood was carried out in a fixed-bed reactor heated slowly from room temperature to 700 °C under a stream of purging argon to examine the effects of the physically mixed K 2CO 3 or Ca(OH) 2 on the pyrolysis behaviors. K 2CO 3 demonstrated a stronger catalysis for decomposition of hemicellulose, cellulose and lignin constituents, leading to the reduced yield of liquid product in conjunction with the increased yields of gaseous and char products because of the promoted secondary reactions of liquid product. With the addition of 17.7 wt.% of K 2CO 3, none of saccharides, aldehydes and alcohols was formed and the formation of acids, furans and guaiacols was substantially reduced, whereas the yields of alkanes and phenols were increased. Potassium led to an increase in the cumulative yields of H 2, CO 2 and CO at 700 °C. Ca(OH) 2 somewhat promoted the decomposition of cellulose and lignin constituents, and the effect of Ca(OH) 2 on the yields of liquid and char was opposite to that of K 2CO 3. With the addition of 22.2 wt.% Ca(OH) 2, some groups of liquid product such as acids and aldehydes disappeared completely and the yields of saccharides, furans and guaiacols were somewhat reduced, while the yield of alcohols was remarkably increased in contrast to the result of K 2CO 3. The addition of Ca(OH) 2 did not significantly change the total yield of gaseous product at 700 °C but enhanced the yield of H 2.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.fuproc.2009.09.015</doi><tpages>9</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0378-3820
ispartof Fuel processing technology, 2010-08, Vol.91 (8), p.942-950
issn 0378-3820
1873-7188
language eng
recordid cdi_proquest_miscellaneous_753682103
source Access via ScienceDirect (Elsevier)
subjects Applied sciences
Ca(OH) 2
Catalytic pyrolysis
Energy
Energy. Thermal use of fuels
Exact sciences and technology
Fuels
K 2CO 3
Pine wood
title Pyrolysis of pine wood in a slowly heating fixed-bed reactor: Potassium carbonate versus calcium hydroxide as a catalyst
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-21T09%3A51%3A55IST&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=Pyrolysis%20of%20pine%20wood%20in%20a%20slowly%20heating%20fixed-bed%20reactor:%20Potassium%20carbonate%20versus%20calcium%20hydroxide%20as%20a%20catalyst&rft.jtitle=Fuel%20processing%20technology&rft.au=Wang,%20Zhenya&rft.date=2010-08-01&rft.volume=91&rft.issue=8&rft.spage=942&rft.epage=950&rft.pages=942-950&rft.issn=0378-3820&rft.eissn=1873-7188&rft.coden=FPTEDY&rft_id=info:doi/10.1016/j.fuproc.2009.09.015&rft_dat=%3Cproquest_cross%3E753682103%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=753682103&rft_id=info:pmid/&rft_els_id=S0378382009002926&rfr_iscdi=true