Autothermal reforming of methane to synthesis gas: Modeling and simulation

Autothermal reforming (ATR), that is the combination of non-catalytic partial oxidation and adiabatic steam reforming, is an important process to produce synthesis gas (syngas) from natural gas. The main scope of this work is proposing a mathematical model considering an autothermal reformer consist...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:International journal of hydrogen energy 2009-02, Vol.34 (3), p.1292-1300
Hauptverfasser: Zahedi nezhad, M., Rowshanzamir, S., Eikani, M.H.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 1300
container_issue 3
container_start_page 1292
container_title International journal of hydrogen energy
container_volume 34
creator Zahedi nezhad, M.
Rowshanzamir, S.
Eikani, M.H.
description Autothermal reforming (ATR), that is the combination of non-catalytic partial oxidation and adiabatic steam reforming, is an important process to produce synthesis gas (syngas) from natural gas. The main scope of this work is proposing a mathematical model considering an autothermal reformer consisting of two distinct sections; a combustion section and a catalytic bed section. In the combustion section, temperature and composition were predicted using 108 simultaneous elementary reactions considering 28 species. The results were considered as initial conditions for the catalytic bed section. A one-dimensional heterogeneous reactor model was used for kinetic simulation of the second section. Results of the model were compared by ATR process published data.
doi_str_mv 10.1016/j.ijhydene.2008.11.091
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_901669443</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0360319908016121</els_id><sourcerecordid>901669443</sourcerecordid><originalsourceid>FETCH-LOGICAL-c440t-bad6a879206941dc9b9e1fb7cba7c43a382c7e20b561a3cc3f8458361d269bd73</originalsourceid><addsrcrecordid>eNqFkD1PwzAQhi0EEqXwF1AWxJTgi90kZqJCfKqIBWbLsS-toyQudorUf4-rFlamW567e9-HkEugGVAobtrMtqutwQGznNIqA8iogCMygaoUKeNVeUwmlBU0ZSDEKTkLoaUUSsrFhLzON6MbV-h71SUeG-d7OywT1yQ9jis1YDK6JGyHiAQbkqUKt8mbM9jtKDWYJNh-06nRuuGcnDSqC3hxmFPy-fjwcf-cLt6fXu7ni1RzTse0VqZQMVlOC8HBaFELhKYuda1KzZliVa5LzGk9K0AxrVlT8VnFCjB5IWpTsim53t9de_e1wTDK3gaNXRfTuk2QIkqJpzmLZLEntXchxHZy7W2v_FYClTt3spW_7uTOnQSQ0V1cvDq8UEGrrvFq0Db8becAPBrkkbvbcxj7flv0MmiLg0ZjPepRGmf_e_UDQr-I7w</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>901669443</pqid></control><display><type>article</type><title>Autothermal reforming of methane to synthesis gas: Modeling and simulation</title><source>Elsevier ScienceDirect Journals Complete</source><creator>Zahedi nezhad, M. ; Rowshanzamir, S. ; Eikani, M.H.</creator><creatorcontrib>Zahedi nezhad, M. ; Rowshanzamir, S. ; Eikani, M.H.</creatorcontrib><description>Autothermal reforming (ATR), that is the combination of non-catalytic partial oxidation and adiabatic steam reforming, is an important process to produce synthesis gas (syngas) from natural gas. The main scope of this work is proposing a mathematical model considering an autothermal reformer consisting of two distinct sections; a combustion section and a catalytic bed section. In the combustion section, temperature and composition were predicted using 108 simultaneous elementary reactions considering 28 species. The results were considered as initial conditions for the catalytic bed section. A one-dimensional heterogeneous reactor model was used for kinetic simulation of the second section. Results of the model were compared by ATR process published data.</description><identifier>ISSN: 0360-3199</identifier><identifier>EISSN: 1879-3487</identifier><identifier>DOI: 10.1016/j.ijhydene.2008.11.091</identifier><identifier>CODEN: IJHEDX</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Applied sciences ; Autothermal reforming ; Catalysis ; Catalysts ; Combustion ; Computer simulation ; Energy ; Exact sciences and technology ; Fuel processing. Carbochemistry and petrochemistry ; Fuels ; Gas processing ; Mathematical models ; Methane ; Modeling ; Reforming ; Synthesis gas</subject><ispartof>International journal of hydrogen energy, 2009-02, Vol.34 (3), p.1292-1300</ispartof><rights>2008 International Association for Hydrogen Energy</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c440t-bad6a879206941dc9b9e1fb7cba7c43a382c7e20b561a3cc3f8458361d269bd73</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.ijhydene.2008.11.091$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=21140014$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Zahedi nezhad, M.</creatorcontrib><creatorcontrib>Rowshanzamir, S.</creatorcontrib><creatorcontrib>Eikani, M.H.</creatorcontrib><title>Autothermal reforming of methane to synthesis gas: Modeling and simulation</title><title>International journal of hydrogen energy</title><description>Autothermal reforming (ATR), that is the combination of non-catalytic partial oxidation and adiabatic steam reforming, is an important process to produce synthesis gas (syngas) from natural gas. The main scope of this work is proposing a mathematical model considering an autothermal reformer consisting of two distinct sections; a combustion section and a catalytic bed section. In the combustion section, temperature and composition were predicted using 108 simultaneous elementary reactions considering 28 species. The results were considered as initial conditions for the catalytic bed section. A one-dimensional heterogeneous reactor model was used for kinetic simulation of the second section. Results of the model were compared by ATR process published data.</description><subject>Applied sciences</subject><subject>Autothermal reforming</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Combustion</subject><subject>Computer simulation</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuel processing. Carbochemistry and petrochemistry</subject><subject>Fuels</subject><subject>Gas processing</subject><subject>Mathematical models</subject><subject>Methane</subject><subject>Modeling</subject><subject>Reforming</subject><subject>Synthesis gas</subject><issn>0360-3199</issn><issn>1879-3487</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNqFkD1PwzAQhi0EEqXwF1AWxJTgi90kZqJCfKqIBWbLsS-toyQudorUf4-rFlamW567e9-HkEugGVAobtrMtqutwQGznNIqA8iogCMygaoUKeNVeUwmlBU0ZSDEKTkLoaUUSsrFhLzON6MbV-h71SUeG-d7OywT1yQ9jis1YDK6JGyHiAQbkqUKt8mbM9jtKDWYJNh-06nRuuGcnDSqC3hxmFPy-fjwcf-cLt6fXu7ni1RzTse0VqZQMVlOC8HBaFELhKYuda1KzZliVa5LzGk9K0AxrVlT8VnFCjB5IWpTsim53t9de_e1wTDK3gaNXRfTuk2QIkqJpzmLZLEntXchxHZy7W2v_FYClTt3spW_7uTOnQSQ0V1cvDq8UEGrrvFq0Db8becAPBrkkbvbcxj7flv0MmiLg0ZjPepRGmf_e_UDQr-I7w</recordid><startdate>20090201</startdate><enddate>20090201</enddate><creator>Zahedi nezhad, M.</creator><creator>Rowshanzamir, S.</creator><creator>Eikani, M.H.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>8FD</scope><scope>L7M</scope></search><sort><creationdate>20090201</creationdate><title>Autothermal reforming of methane to synthesis gas: Modeling and simulation</title><author>Zahedi nezhad, M. ; Rowshanzamir, S. ; Eikani, M.H.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c440t-bad6a879206941dc9b9e1fb7cba7c43a382c7e20b561a3cc3f8458361d269bd73</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Applied sciences</topic><topic>Autothermal reforming</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Combustion</topic><topic>Computer simulation</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fuel processing. Carbochemistry and petrochemistry</topic><topic>Fuels</topic><topic>Gas processing</topic><topic>Mathematical models</topic><topic>Methane</topic><topic>Modeling</topic><topic>Reforming</topic><topic>Synthesis gas</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Zahedi nezhad, M.</creatorcontrib><creatorcontrib>Rowshanzamir, S.</creatorcontrib><creatorcontrib>Eikani, M.H.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Electronics &amp; Communications Abstracts</collection><collection>Technology Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>International journal of hydrogen energy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Zahedi nezhad, M.</au><au>Rowshanzamir, S.</au><au>Eikani, M.H.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Autothermal reforming of methane to synthesis gas: Modeling and simulation</atitle><jtitle>International journal of hydrogen energy</jtitle><date>2009-02-01</date><risdate>2009</risdate><volume>34</volume><issue>3</issue><spage>1292</spage><epage>1300</epage><pages>1292-1300</pages><issn>0360-3199</issn><eissn>1879-3487</eissn><coden>IJHEDX</coden><abstract>Autothermal reforming (ATR), that is the combination of non-catalytic partial oxidation and adiabatic steam reforming, is an important process to produce synthesis gas (syngas) from natural gas. The main scope of this work is proposing a mathematical model considering an autothermal reformer consisting of two distinct sections; a combustion section and a catalytic bed section. In the combustion section, temperature and composition were predicted using 108 simultaneous elementary reactions considering 28 species. The results were considered as initial conditions for the catalytic bed section. A one-dimensional heterogeneous reactor model was used for kinetic simulation of the second section. Results of the model were compared by ATR process published data.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijhydene.2008.11.091</doi><tpages>9</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0360-3199
ispartof International journal of hydrogen energy, 2009-02, Vol.34 (3), p.1292-1300
issn 0360-3199
1879-3487
language eng
recordid cdi_proquest_miscellaneous_901669443
source Elsevier ScienceDirect Journals Complete
subjects Applied sciences
Autothermal reforming
Catalysis
Catalysts
Combustion
Computer simulation
Energy
Exact sciences and technology
Fuel processing. Carbochemistry and petrochemistry
Fuels
Gas processing
Mathematical models
Methane
Modeling
Reforming
Synthesis gas
title Autothermal reforming of methane to synthesis gas: Modeling and simulation
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-04T09%3A39%3A00IST&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=Autothermal%20reforming%20of%20methane%20to%20synthesis%20gas:%20Modeling%20and%20simulation&rft.jtitle=International%20journal%20of%20hydrogen%20energy&rft.au=Zahedi%20nezhad,%20M.&rft.date=2009-02-01&rft.volume=34&rft.issue=3&rft.spage=1292&rft.epage=1300&rft.pages=1292-1300&rft.issn=0360-3199&rft.eissn=1879-3487&rft.coden=IJHEDX&rft_id=info:doi/10.1016/j.ijhydene.2008.11.091&rft_dat=%3Cproquest_cross%3E901669443%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=901669443&rft_id=info:pmid/&rft_els_id=S0360319908016121&rfr_iscdi=true