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Energy balance model of a SOFC cogenerator operated with biogas
A small cogeneration system based on a Solid Oxide Fuel Cell (SOFC) fed on the renewable energy source biogas is presented. An existing farm biogas production site (35 m 3 per day), currently equipped with a SOFC demonstration stack, is taken for reference. A process flow diagram was defined in a so...
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Published in: | Journal of power sources 2003-05, Vol.118 (1), p.375-383 |
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container_title | Journal of power sources |
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creator | Van herle, Jan Maréchal, F. Leuenberger, S. Favrat, D. |
description | A small cogeneration system based on a Solid Oxide Fuel Cell (SOFC) fed on the renewable energy source biogas is presented. An existing farm biogas production site (35
m
3 per day), currently equipped with a SOFC demonstration stack, is taken for reference. A process flow diagram was defined in a software package allowing to vary system operating parameters like the fuel inlet composition, reforming technology, stack temperature and stack current (or fuel conversion). For system reforming simplicity, a base case parameter set was defined as the fuel inlet of 60% CH
4:40% CO
2 mixed with air in a 1:1 ratio, together with 800
°C operating temperature and 80% fuel conversion. A model stack, consisting of 100 series elements of anode supported electrolyte cells of 100
cm
2 each, was calculated to deliver 3.1
kW
el and 5.16
kW
th from an input of 1.5
N
m
3/h of biogas (8.95
kW LHV), corresponding to 33.8 and 57.6% electrical and thermal efficiencies (Lower Heating Values (LHVs)), respectively. The incidence on the efficiencies of the model system was examined by the variation of a number of parameters such as the CO
2 content in the biogas, the amount of air addition to the biogas stream, the addition of steam to the fuel inlet, the air excess ratio
λ and the stack operating temperature, and the results discussed. |
doi_str_mv | 10.1016/S0378-7753(03)00103-4 |
format | article |
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m
3 per day), currently equipped with a SOFC demonstration stack, is taken for reference. A process flow diagram was defined in a software package allowing to vary system operating parameters like the fuel inlet composition, reforming technology, stack temperature and stack current (or fuel conversion). For system reforming simplicity, a base case parameter set was defined as the fuel inlet of 60% CH
4:40% CO
2 mixed with air in a 1:1 ratio, together with 800
°C operating temperature and 80% fuel conversion. A model stack, consisting of 100 series elements of anode supported electrolyte cells of 100
cm
2 each, was calculated to deliver 3.1
kW
el and 5.16
kW
th from an input of 1.5
N
m
3/h of biogas (8.95
kW LHV), corresponding to 33.8 and 57.6% electrical and thermal efficiencies (Lower Heating Values (LHVs)), respectively. The incidence on the efficiencies of the model system was examined by the variation of a number of parameters such as the CO
2 content in the biogas, the amount of air addition to the biogas stream, the addition of steam to the fuel inlet, the air excess ratio
λ and the stack operating temperature, and the results discussed.</description><identifier>ISSN: 0378-7753</identifier><identifier>EISSN: 1873-2755</identifier><identifier>DOI: 10.1016/S0378-7753(03)00103-4</identifier><identifier>CODEN: JPSODZ</identifier><language>eng</language><publisher>Lausanne: Elsevier B.V</publisher><subject>Applied sciences ; Biogas fuel ; Combined power plants ; Efficiency ; Energy ; Energy balance ; Energy. Thermal use of fuels ; Equipments for energy generation and conversion: thermal, electrical, mechanical energy, etc ; Exact sciences and technology ; Fuel cells ; Installations for energy generation and conversion: thermal and electrical energy ; SOFC stack model</subject><ispartof>Journal of power sources, 2003-05, Vol.118 (1), p.375-383</ispartof><rights>2003 Elsevier Science B.V.</rights><rights>2003 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c420t-820086055a7db73ac8a85249fa86764cd817a783ab10ceb7bc45b0e750a612863</citedby><cites>FETCH-LOGICAL-c420t-820086055a7db73ac8a85249fa86764cd817a783ab10ceb7bc45b0e750a612863</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,780,784,789,790,23930,23931,25140,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=14863389$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Van herle, Jan</creatorcontrib><creatorcontrib>Maréchal, F.</creatorcontrib><creatorcontrib>Leuenberger, S.</creatorcontrib><creatorcontrib>Favrat, D.</creatorcontrib><title>Energy balance model of a SOFC cogenerator operated with biogas</title><title>Journal of power sources</title><description>A small cogeneration system based on a Solid Oxide Fuel Cell (SOFC) fed on the renewable energy source biogas is presented. An existing farm biogas production site (35
m
3 per day), currently equipped with a SOFC demonstration stack, is taken for reference. A process flow diagram was defined in a software package allowing to vary system operating parameters like the fuel inlet composition, reforming technology, stack temperature and stack current (or fuel conversion). For system reforming simplicity, a base case parameter set was defined as the fuel inlet of 60% CH
4:40% CO
2 mixed with air in a 1:1 ratio, together with 800
°C operating temperature and 80% fuel conversion. A model stack, consisting of 100 series elements of anode supported electrolyte cells of 100
cm
2 each, was calculated to deliver 3.1
kW
el and 5.16
kW
th from an input of 1.5
N
m
3/h of biogas (8.95
kW LHV), corresponding to 33.8 and 57.6% electrical and thermal efficiencies (Lower Heating Values (LHVs)), respectively. The incidence on the efficiencies of the model system was examined by the variation of a number of parameters such as the CO
2 content in the biogas, the amount of air addition to the biogas stream, the addition of steam to the fuel inlet, the air excess ratio
λ and the stack operating temperature, and the results discussed.</description><subject>Applied sciences</subject><subject>Biogas fuel</subject><subject>Combined power plants</subject><subject>Efficiency</subject><subject>Energy</subject><subject>Energy balance</subject><subject>Energy. Thermal use of fuels</subject><subject>Equipments for energy generation and conversion: thermal, electrical, mechanical energy, etc</subject><subject>Exact sciences and technology</subject><subject>Fuel cells</subject><subject>Installations for energy generation and conversion: thermal and electrical energy</subject><subject>SOFC stack model</subject><issn>0378-7753</issn><issn>1873-2755</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2003</creationdate><recordtype>article</recordtype><recordid>eNqFkEtLAzEQgIMoWKs_QchF0cPqZPPsqUhpVSj0UD2HbDZbI9umJlul_960FT0KAzOHb14fQpcE7ggQcT8HKlUhJac3QG8BCNCCHaEeUZIWpeT8GPV-kVN0ltI7ZIpI6KHheOXiYosr05qVdXgZatfi0GCD57PJCNuwcJkwXYg4rHeFq_GX795w5cPCpHN00pg2uYuf3Eevk_HL6KmYzh6fRw_TwrISukKVAEoA50bWlaTGKqN4yQaNUUIKZmtFpJGKmoqAdZWsLOMVOMnBCFIqQfvo-jB3HcPHxqVOL32yrs1Xu7BJmjAhSqYGGeQH0MaQUnSNXke_NHGrCeidLr3XpXcuNOTY6dIs9139LDDJmraJWYdPf80sH0H384cHzuVvP72LOlnvsrraR2c7XQf_z6ZvWed8zA</recordid><startdate>20030525</startdate><enddate>20030525</enddate><creator>Van herle, Jan</creator><creator>Maréchal, F.</creator><creator>Leuenberger, S.</creator><creator>Favrat, D.</creator><general>Elsevier B.V</general><general>Elsevier Sequoia</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope></search><sort><creationdate>20030525</creationdate><title>Energy balance model of a SOFC cogenerator operated with biogas</title><author>Van herle, Jan ; Maréchal, F. ; Leuenberger, S. ; Favrat, D.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c420t-820086055a7db73ac8a85249fa86764cd817a783ab10ceb7bc45b0e750a612863</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2003</creationdate><topic>Applied sciences</topic><topic>Biogas fuel</topic><topic>Combined power plants</topic><topic>Efficiency</topic><topic>Energy</topic><topic>Energy balance</topic><topic>Energy. Thermal use of fuels</topic><topic>Equipments for energy generation and conversion: thermal, electrical, mechanical energy, etc</topic><topic>Exact sciences and technology</topic><topic>Fuel cells</topic><topic>Installations for energy generation and conversion: thermal and electrical energy</topic><topic>SOFC stack model</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Van herle, Jan</creatorcontrib><creatorcontrib>Maréchal, F.</creatorcontrib><creatorcontrib>Leuenberger, S.</creatorcontrib><creatorcontrib>Favrat, D.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><jtitle>Journal of power sources</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Van herle, Jan</au><au>Maréchal, F.</au><au>Leuenberger, S.</au><au>Favrat, D.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Energy balance model of a SOFC cogenerator operated with biogas</atitle><jtitle>Journal of power sources</jtitle><date>2003-05-25</date><risdate>2003</risdate><volume>118</volume><issue>1</issue><spage>375</spage><epage>383</epage><pages>375-383</pages><issn>0378-7753</issn><eissn>1873-2755</eissn><coden>JPSODZ</coden><abstract>A small cogeneration system based on a Solid Oxide Fuel Cell (SOFC) fed on the renewable energy source biogas is presented. An existing farm biogas production site (35
m
3 per day), currently equipped with a SOFC demonstration stack, is taken for reference. A process flow diagram was defined in a software package allowing to vary system operating parameters like the fuel inlet composition, reforming technology, stack temperature and stack current (or fuel conversion). For system reforming simplicity, a base case parameter set was defined as the fuel inlet of 60% CH
4:40% CO
2 mixed with air in a 1:1 ratio, together with 800
°C operating temperature and 80% fuel conversion. A model stack, consisting of 100 series elements of anode supported electrolyte cells of 100
cm
2 each, was calculated to deliver 3.1
kW
el and 5.16
kW
th from an input of 1.5
N
m
3/h of biogas (8.95
kW LHV), corresponding to 33.8 and 57.6% electrical and thermal efficiencies (Lower Heating Values (LHVs)), respectively. The incidence on the efficiencies of the model system was examined by the variation of a number of parameters such as the CO
2 content in the biogas, the amount of air addition to the biogas stream, the addition of steam to the fuel inlet, the air excess ratio
λ and the stack operating temperature, and the results discussed.</abstract><cop>Lausanne</cop><pub>Elsevier B.V</pub><doi>10.1016/S0378-7753(03)00103-4</doi><tpages>9</tpages></addata></record> |
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language | eng |
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source | ScienceDirect Freedom Collection |
subjects | Applied sciences Biogas fuel Combined power plants Efficiency Energy Energy balance Energy. Thermal use of fuels Equipments for energy generation and conversion: thermal, electrical, mechanical energy, etc Exact sciences and technology Fuel cells Installations for energy generation and conversion: thermal and electrical energy SOFC stack model |
title | Energy balance model of a SOFC cogenerator operated with biogas |
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