Valorisation of forestry waste by pyrolysis in an auger reactor

Pyrolysis of forestry waste has been carried out in an auger reactor to study the influence of operational variables on the reactor performance and the properties of the related products. Pine woodchips were used for the first time as raw material and fed continuously into the reactor. Ten experimen...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Waste management (Elmsford) 2011-06, Vol.31 (6), p.1339-1349
Hauptverfasser: Puy, Neus, Murillo, Ramón, Navarro, María V., López, José M., Rieradevall, Joan, Fowler, G., Aranguren, Ignacio, García, Tomás, Bartrolí, Jordi, Mastral, Ana M.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 1349
container_issue 6
container_start_page 1339
container_title Waste management (Elmsford)
container_volume 31
creator Puy, Neus
Murillo, Ramón
Navarro, María V.
López, José M.
Rieradevall, Joan
Fowler, G.
Aranguren, Ignacio
García, Tomás
Bartrolí, Jordi
Mastral, Ana M.
description Pyrolysis of forestry waste has been carried out in an auger reactor to study the influence of operational variables on the reactor performance and the properties of the related products. Pine woodchips were used for the first time as raw material and fed continuously into the reactor. Ten experiments were carried out under inert atmosphere at: (i) different reaction temperature (1073, 973, 873, 823 and 773 K); (ii) different solid residence time (5, 3, 2 and 1.5 min); and (iii) different biomass flow rate (3.9, 4.8 and 6.9 kg/h). Results show that the greatest yields for liquid production (59%) and optimum product characterisation were obtained at the lowest temperature studied (773 K) and applying solid residence times longer than 2 min. Regarding bio-oil properties, GC/MS qualitative identification show that the most abundant compounds are volatile polar compounds, phenols and benzenediols; and very few differences can be observed among the samples regardless of the pyrolysis operating conditions. On the whole, experimental results demonstrate that complete reaction of forest woodchips can be achieved in an auger reactor in most of the experimental conditions tested. Moreover, this study presents the initial steps for the future scaling up of the auger reactor with the aim of converting it into a mobile plant which will be able to remotely process biomass such as energy crops, forestry and agricultural wastes to obtain bio-oil that, in turn, can be used as energy vector to avoid high transport costs.
doi_str_mv 10.1016/j.wasman.2011.01.020
format Article
fullrecord <record><control><sourceid>proquest_osti_</sourceid><recordid>TN_cdi_osti_scitechconnect_21550375</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0956053X11000523</els_id><sourcerecordid>1777105291</sourcerecordid><originalsourceid>FETCH-LOGICAL-c484t-61494449656dd8890ecb3514c77b18b84debaeaddeb77919cd3064986e53746f3</originalsourceid><addsrcrecordid>eNqN0U2LFDEQBuAgijuu_gORBhG99JjKdy4rsvgFC15UvIV0uloz9HTGpEfpf2-GHvW2CAW5PKlU6iXkMdAtUFAvd9tfvuz9tGUUYEtrMXqHbMBo2zIh1V2yoVaqlkr-9YI8KGVHKQgD9D65YMA5l6A35NUXP6Yci59jmpo0NEPKWOa8NLX7jE23NIclp3EpsTRxanyt4zfMTUYf5pQfknuDHws-Op-X5PPbN5-u37c3H999uH590wZhxNwqEFYIYZVUfW-MpRi6OoAIWndgOiN67Dz6vh5aW7Ch51QJaxRKroUa-CV5uvZNZY6uhDhj-B7SNGGYHQMpKdeyquerOuT041j_4faxBBxHP2E6Fme0qqux7D-kYtpyQW2VL26VoLUGKpmFSsVKQ06lZBzcIce9z4sD6k6huZ1bQ3On0BytxWi99uT8wrHbY__30p-UKnh2Br4EPw7ZTyGWf06AUlVWd7U6rEn8jJhPi8IpYB_zaU99irdP8hvKV7TF</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1777105291</pqid></control><display><type>article</type><title>Valorisation of forestry waste by pyrolysis in an auger reactor</title><source>MEDLINE</source><source>Elsevier ScienceDirect Journals</source><creator>Puy, Neus ; Murillo, Ramón ; Navarro, María V. ; López, José M. ; Rieradevall, Joan ; Fowler, G. ; Aranguren, Ignacio ; García, Tomás ; Bartrolí, Jordi ; Mastral, Ana M.</creator><creatorcontrib>Puy, Neus ; Murillo, Ramón ; Navarro, María V. ; López, José M. ; Rieradevall, Joan ; Fowler, G. ; Aranguren, Ignacio ; García, Tomás ; Bartrolí, Jordi ; Mastral, Ana M.</creatorcontrib><description>Pyrolysis of forestry waste has been carried out in an auger reactor to study the influence of operational variables on the reactor performance and the properties of the related products. Pine woodchips were used for the first time as raw material and fed continuously into the reactor. Ten experiments were carried out under inert atmosphere at: (i) different reaction temperature (1073, 973, 873, 823 and 773 K); (ii) different solid residence time (5, 3, 2 and 1.5 min); and (iii) different biomass flow rate (3.9, 4.8 and 6.9 kg/h). Results show that the greatest yields for liquid production (59%) and optimum product characterisation were obtained at the lowest temperature studied (773 K) and applying solid residence times longer than 2 min. Regarding bio-oil properties, GC/MS qualitative identification show that the most abundant compounds are volatile polar compounds, phenols and benzenediols; and very few differences can be observed among the samples regardless of the pyrolysis operating conditions. On the whole, experimental results demonstrate that complete reaction of forest woodchips can be achieved in an auger reactor in most of the experimental conditions tested. Moreover, this study presents the initial steps for the future scaling up of the auger reactor with the aim of converting it into a mobile plant which will be able to remotely process biomass such as energy crops, forestry and agricultural wastes to obtain bio-oil that, in turn, can be used as energy vector to avoid high transport costs.</description><identifier>ISSN: 0956-053X</identifier><identifier>EISSN: 1879-2456</identifier><identifier>DOI: 10.1016/j.wasman.2011.01.020</identifier><identifier>PMID: 21333517</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>09 BIOMASS FUELS ; AGRICULTURAL WASTES ; Agriculture, rearing and food industries wastes ; ALTERNATIVE FUELS ; Applied sciences ; AROMATICS ; ATMOSPHERES ; Augers ; Benzene Derivatives - analysis ; BIOFUELS ; BIOMASS ; CHEMICAL REACTIONS ; CHEMICAL REACTORS ; CHROMATOGRAPHY ; CONIFERS ; CONTROLLED ATMOSPHERES ; COST ; CROPS ; DECOMPOSITION ; Direct power generation ; ENERGY SOURCES ; Energy use ; Exact sciences and technology ; FLOW RATE ; FLUIDS ; Forestry ; FORESTS ; FUELS ; GAS CHROMATOGRAPHY ; Gas Chromatography-Mass Spectrometry ; HYDROXY COMPOUNDS ; Incineration ; INERT ATMOSPHERE ; LIQUIDS ; MASS SPECTROSCOPY ; MATERIALS ; ORGANIC COMPOUNDS ; ORGANIC WASTES ; Other wastes and particular components of wastes ; PHENOL ; PHENOLS ; Phenols - analysis ; PINES ; PINOPHYTA ; PLANTS ; POLAR COMPOUNDS ; Pollution ; PYROLYSIS ; RAW MATERIALS ; Reactors ; Refuse Disposal - instrumentation ; Refuse Disposal - methods ; RENEWABLE ENERGY SOURCES ; SEPARATION PROCESSES ; SOLID WASTES ; SPECTROSCOPY ; Temperature ; THERMOCHEMICAL PROCESSES ; Thermogravimetry ; Time Factors ; TRANSPORT ; TREES ; VOLATILITY ; Waste Products - analysis ; WASTES ; WOOD WASTES</subject><ispartof>Waste management (Elmsford), 2011-06, Vol.31 (6), p.1339-1349</ispartof><rights>2011 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><rights>Copyright © 2011 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c484t-61494449656dd8890ecb3514c77b18b84debaeaddeb77919cd3064986e53746f3</citedby><cites>FETCH-LOGICAL-c484t-61494449656dd8890ecb3514c77b18b84debaeaddeb77919cd3064986e53746f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0956053X11000523$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,776,780,881,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=24166335$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/21333517$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/21550375$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Puy, Neus</creatorcontrib><creatorcontrib>Murillo, Ramón</creatorcontrib><creatorcontrib>Navarro, María V.</creatorcontrib><creatorcontrib>López, José M.</creatorcontrib><creatorcontrib>Rieradevall, Joan</creatorcontrib><creatorcontrib>Fowler, G.</creatorcontrib><creatorcontrib>Aranguren, Ignacio</creatorcontrib><creatorcontrib>García, Tomás</creatorcontrib><creatorcontrib>Bartrolí, Jordi</creatorcontrib><creatorcontrib>Mastral, Ana M.</creatorcontrib><title>Valorisation of forestry waste by pyrolysis in an auger reactor</title><title>Waste management (Elmsford)</title><addtitle>Waste Manag</addtitle><description>Pyrolysis of forestry waste has been carried out in an auger reactor to study the influence of operational variables on the reactor performance and the properties of the related products. Pine woodchips were used for the first time as raw material and fed continuously into the reactor. Ten experiments were carried out under inert atmosphere at: (i) different reaction temperature (1073, 973, 873, 823 and 773 K); (ii) different solid residence time (5, 3, 2 and 1.5 min); and (iii) different biomass flow rate (3.9, 4.8 and 6.9 kg/h). Results show that the greatest yields for liquid production (59%) and optimum product characterisation were obtained at the lowest temperature studied (773 K) and applying solid residence times longer than 2 min. Regarding bio-oil properties, GC/MS qualitative identification show that the most abundant compounds are volatile polar compounds, phenols and benzenediols; and very few differences can be observed among the samples regardless of the pyrolysis operating conditions. On the whole, experimental results demonstrate that complete reaction of forest woodchips can be achieved in an auger reactor in most of the experimental conditions tested. Moreover, this study presents the initial steps for the future scaling up of the auger reactor with the aim of converting it into a mobile plant which will be able to remotely process biomass such as energy crops, forestry and agricultural wastes to obtain bio-oil that, in turn, can be used as energy vector to avoid high transport costs.</description><subject>09 BIOMASS FUELS</subject><subject>AGRICULTURAL WASTES</subject><subject>Agriculture, rearing and food industries wastes</subject><subject>ALTERNATIVE FUELS</subject><subject>Applied sciences</subject><subject>AROMATICS</subject><subject>ATMOSPHERES</subject><subject>Augers</subject><subject>Benzene Derivatives - analysis</subject><subject>BIOFUELS</subject><subject>BIOMASS</subject><subject>CHEMICAL REACTIONS</subject><subject>CHEMICAL REACTORS</subject><subject>CHROMATOGRAPHY</subject><subject>CONIFERS</subject><subject>CONTROLLED ATMOSPHERES</subject><subject>COST</subject><subject>CROPS</subject><subject>DECOMPOSITION</subject><subject>Direct power generation</subject><subject>ENERGY SOURCES</subject><subject>Energy use</subject><subject>Exact sciences and technology</subject><subject>FLOW RATE</subject><subject>FLUIDS</subject><subject>Forestry</subject><subject>FORESTS</subject><subject>FUELS</subject><subject>GAS CHROMATOGRAPHY</subject><subject>Gas Chromatography-Mass Spectrometry</subject><subject>HYDROXY COMPOUNDS</subject><subject>Incineration</subject><subject>INERT ATMOSPHERE</subject><subject>LIQUIDS</subject><subject>MASS SPECTROSCOPY</subject><subject>MATERIALS</subject><subject>ORGANIC COMPOUNDS</subject><subject>ORGANIC WASTES</subject><subject>Other wastes and particular components of wastes</subject><subject>PHENOL</subject><subject>PHENOLS</subject><subject>Phenols - analysis</subject><subject>PINES</subject><subject>PINOPHYTA</subject><subject>PLANTS</subject><subject>POLAR COMPOUNDS</subject><subject>Pollution</subject><subject>PYROLYSIS</subject><subject>RAW MATERIALS</subject><subject>Reactors</subject><subject>Refuse Disposal - instrumentation</subject><subject>Refuse Disposal - methods</subject><subject>RENEWABLE ENERGY SOURCES</subject><subject>SEPARATION PROCESSES</subject><subject>SOLID WASTES</subject><subject>SPECTROSCOPY</subject><subject>Temperature</subject><subject>THERMOCHEMICAL PROCESSES</subject><subject>Thermogravimetry</subject><subject>Time Factors</subject><subject>TRANSPORT</subject><subject>TREES</subject><subject>VOLATILITY</subject><subject>Waste Products - analysis</subject><subject>WASTES</subject><subject>WOOD WASTES</subject><issn>0956-053X</issn><issn>1879-2456</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqN0U2LFDEQBuAgijuu_gORBhG99JjKdy4rsvgFC15UvIV0uloz9HTGpEfpf2-GHvW2CAW5PKlU6iXkMdAtUFAvd9tfvuz9tGUUYEtrMXqHbMBo2zIh1V2yoVaqlkr-9YI8KGVHKQgD9D65YMA5l6A35NUXP6Yci59jmpo0NEPKWOa8NLX7jE23NIclp3EpsTRxanyt4zfMTUYf5pQfknuDHws-Op-X5PPbN5-u37c3H999uH590wZhxNwqEFYIYZVUfW-MpRi6OoAIWndgOiN67Dz6vh5aW7Ch51QJaxRKroUa-CV5uvZNZY6uhDhj-B7SNGGYHQMpKdeyquerOuT041j_4faxBBxHP2E6Fme0qqux7D-kYtpyQW2VL26VoLUGKpmFSsVKQ06lZBzcIce9z4sD6k6huZ1bQ3On0BytxWi99uT8wrHbY__30p-UKnh2Br4EPw7ZTyGWf06AUlVWd7U6rEn8jJhPi8IpYB_zaU99irdP8hvKV7TF</recordid><startdate>20110601</startdate><enddate>20110601</enddate><creator>Puy, Neus</creator><creator>Murillo, Ramón</creator><creator>Navarro, María V.</creator><creator>López, José M.</creator><creator>Rieradevall, Joan</creator><creator>Fowler, G.</creator><creator>Aranguren, Ignacio</creator><creator>García, Tomás</creator><creator>Bartrolí, Jordi</creator><creator>Mastral, Ana M.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><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>7QQ</scope><scope>7SU</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>JG9</scope><scope>KR7</scope><scope>7X8</scope><scope>7ST</scope><scope>7TV</scope><scope>SOI</scope><scope>OTOTI</scope></search><sort><creationdate>20110601</creationdate><title>Valorisation of forestry waste by pyrolysis in an auger reactor</title><author>Puy, Neus ; Murillo, Ramón ; Navarro, María V. ; López, José M. ; Rieradevall, Joan ; Fowler, G. ; Aranguren, Ignacio ; García, Tomás ; Bartrolí, Jordi ; Mastral, Ana M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c484t-61494449656dd8890ecb3514c77b18b84debaeaddeb77919cd3064986e53746f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>09 BIOMASS FUELS</topic><topic>AGRICULTURAL WASTES</topic><topic>Agriculture, rearing and food industries wastes</topic><topic>ALTERNATIVE FUELS</topic><topic>Applied sciences</topic><topic>AROMATICS</topic><topic>ATMOSPHERES</topic><topic>Augers</topic><topic>Benzene Derivatives - analysis</topic><topic>BIOFUELS</topic><topic>BIOMASS</topic><topic>CHEMICAL REACTIONS</topic><topic>CHEMICAL REACTORS</topic><topic>CHROMATOGRAPHY</topic><topic>CONIFERS</topic><topic>CONTROLLED ATMOSPHERES</topic><topic>COST</topic><topic>CROPS</topic><topic>DECOMPOSITION</topic><topic>Direct power generation</topic><topic>ENERGY SOURCES</topic><topic>Energy use</topic><topic>Exact sciences and technology</topic><topic>FLOW RATE</topic><topic>FLUIDS</topic><topic>Forestry</topic><topic>FORESTS</topic><topic>FUELS</topic><topic>GAS CHROMATOGRAPHY</topic><topic>Gas Chromatography-Mass Spectrometry</topic><topic>HYDROXY COMPOUNDS</topic><topic>Incineration</topic><topic>INERT ATMOSPHERE</topic><topic>LIQUIDS</topic><topic>MASS SPECTROSCOPY</topic><topic>MATERIALS</topic><topic>ORGANIC COMPOUNDS</topic><topic>ORGANIC WASTES</topic><topic>Other wastes and particular components of wastes</topic><topic>PHENOL</topic><topic>PHENOLS</topic><topic>Phenols - analysis</topic><topic>PINES</topic><topic>PINOPHYTA</topic><topic>PLANTS</topic><topic>POLAR COMPOUNDS</topic><topic>Pollution</topic><topic>PYROLYSIS</topic><topic>RAW MATERIALS</topic><topic>Reactors</topic><topic>Refuse Disposal - instrumentation</topic><topic>Refuse Disposal - methods</topic><topic>RENEWABLE ENERGY SOURCES</topic><topic>SEPARATION PROCESSES</topic><topic>SOLID WASTES</topic><topic>SPECTROSCOPY</topic><topic>Temperature</topic><topic>THERMOCHEMICAL PROCESSES</topic><topic>Thermogravimetry</topic><topic>Time Factors</topic><topic>TRANSPORT</topic><topic>TREES</topic><topic>VOLATILITY</topic><topic>Waste Products - analysis</topic><topic>WASTES</topic><topic>WOOD WASTES</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Puy, Neus</creatorcontrib><creatorcontrib>Murillo, Ramón</creatorcontrib><creatorcontrib>Navarro, María V.</creatorcontrib><creatorcontrib>López, José M.</creatorcontrib><creatorcontrib>Rieradevall, Joan</creatorcontrib><creatorcontrib>Fowler, G.</creatorcontrib><creatorcontrib>Aranguren, Ignacio</creatorcontrib><creatorcontrib>García, Tomás</creatorcontrib><creatorcontrib>Bartrolí, Jordi</creatorcontrib><creatorcontrib>Mastral, Ana M.</creatorcontrib><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Ceramic Abstracts</collection><collection>Environmental Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>MEDLINE - Academic</collection><collection>Environment Abstracts</collection><collection>Pollution Abstracts</collection><collection>Environment Abstracts</collection><collection>OSTI.GOV</collection><jtitle>Waste management (Elmsford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Puy, Neus</au><au>Murillo, Ramón</au><au>Navarro, María V.</au><au>López, José M.</au><au>Rieradevall, Joan</au><au>Fowler, G.</au><au>Aranguren, Ignacio</au><au>García, Tomás</au><au>Bartrolí, Jordi</au><au>Mastral, Ana M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Valorisation of forestry waste by pyrolysis in an auger reactor</atitle><jtitle>Waste management (Elmsford)</jtitle><addtitle>Waste Manag</addtitle><date>2011-06-01</date><risdate>2011</risdate><volume>31</volume><issue>6</issue><spage>1339</spage><epage>1349</epage><pages>1339-1349</pages><issn>0956-053X</issn><eissn>1879-2456</eissn><abstract>Pyrolysis of forestry waste has been carried out in an auger reactor to study the influence of operational variables on the reactor performance and the properties of the related products. Pine woodchips were used for the first time as raw material and fed continuously into the reactor. Ten experiments were carried out under inert atmosphere at: (i) different reaction temperature (1073, 973, 873, 823 and 773 K); (ii) different solid residence time (5, 3, 2 and 1.5 min); and (iii) different biomass flow rate (3.9, 4.8 and 6.9 kg/h). Results show that the greatest yields for liquid production (59%) and optimum product characterisation were obtained at the lowest temperature studied (773 K) and applying solid residence times longer than 2 min. Regarding bio-oil properties, GC/MS qualitative identification show that the most abundant compounds are volatile polar compounds, phenols and benzenediols; and very few differences can be observed among the samples regardless of the pyrolysis operating conditions. On the whole, experimental results demonstrate that complete reaction of forest woodchips can be achieved in an auger reactor in most of the experimental conditions tested. Moreover, this study presents the initial steps for the future scaling up of the auger reactor with the aim of converting it into a mobile plant which will be able to remotely process biomass such as energy crops, forestry and agricultural wastes to obtain bio-oil that, in turn, can be used as energy vector to avoid high transport costs.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><pmid>21333517</pmid><doi>10.1016/j.wasman.2011.01.020</doi><tpages>11</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0956-053X
ispartof Waste management (Elmsford), 2011-06, Vol.31 (6), p.1339-1349
issn 0956-053X
1879-2456
language eng
recordid cdi_osti_scitechconnect_21550375
source MEDLINE; Elsevier ScienceDirect Journals
subjects 09 BIOMASS FUELS
AGRICULTURAL WASTES
Agriculture, rearing and food industries wastes
ALTERNATIVE FUELS
Applied sciences
AROMATICS
ATMOSPHERES
Augers
Benzene Derivatives - analysis
BIOFUELS
BIOMASS
CHEMICAL REACTIONS
CHEMICAL REACTORS
CHROMATOGRAPHY
CONIFERS
CONTROLLED ATMOSPHERES
COST
CROPS
DECOMPOSITION
Direct power generation
ENERGY SOURCES
Energy use
Exact sciences and technology
FLOW RATE
FLUIDS
Forestry
FORESTS
FUELS
GAS CHROMATOGRAPHY
Gas Chromatography-Mass Spectrometry
HYDROXY COMPOUNDS
Incineration
INERT ATMOSPHERE
LIQUIDS
MASS SPECTROSCOPY
MATERIALS
ORGANIC COMPOUNDS
ORGANIC WASTES
Other wastes and particular components of wastes
PHENOL
PHENOLS
Phenols - analysis
PINES
PINOPHYTA
PLANTS
POLAR COMPOUNDS
Pollution
PYROLYSIS
RAW MATERIALS
Reactors
Refuse Disposal - instrumentation
Refuse Disposal - methods
RENEWABLE ENERGY SOURCES
SEPARATION PROCESSES
SOLID WASTES
SPECTROSCOPY
Temperature
THERMOCHEMICAL PROCESSES
Thermogravimetry
Time Factors
TRANSPORT
TREES
VOLATILITY
Waste Products - analysis
WASTES
WOOD WASTES
title Valorisation of forestry waste by pyrolysis in an auger reactor
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-05T11%3A59%3A13IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_osti_&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Valorisation%20of%20forestry%20waste%20by%20pyrolysis%20in%20an%20auger%20reactor&rft.jtitle=Waste%20management%20(Elmsford)&rft.au=Puy,%20Neus&rft.date=2011-06-01&rft.volume=31&rft.issue=6&rft.spage=1339&rft.epage=1349&rft.pages=1339-1349&rft.issn=0956-053X&rft.eissn=1879-2456&rft_id=info:doi/10.1016/j.wasman.2011.01.020&rft_dat=%3Cproquest_osti_%3E1777105291%3C/proquest_osti_%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1777105291&rft_id=info:pmid/21333517&rft_els_id=S0956053X11000523&rfr_iscdi=true