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Heterogeneous thermochemical decomposition under direct irradiation
Radiative heat transfer within a chemical reacting system directly exposed to an external source of high-flux radiation is considered. The endothermic decomposition of CaCO 3(s) into CaO(s) and CO 2(g) is selected as the model heterogeneous reaction. Its interfacial kinetic parameters are determined...
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Published in: | International journal of heat and mass transfer 2004-04, Vol.47 (8), p.1907-1916 |
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container_end_page | 1916 |
container_issue | 8 |
container_start_page | 1907 |
container_title | International journal of heat and mass transfer |
container_volume | 47 |
creator | Lipinski, W. Steinfeld, A. |
description | Radiative heat transfer within a chemical reacting system directly exposed to an external source of high-flux radiation is considered. The endothermic decomposition of CaCO
3(s) into CaO(s) and CO
2(g) is selected as the model heterogeneous reaction. Its interfacial kinetic parameters are determined by thermogravimetric measurements assuming a contracting geometry rate law and an Arrhenius temperature dependence law. Experimentation using an Argon arc as the radiation source was carried out in which powder samples were subjected to radiative power fluxes in the range 400–930 kW/m
2. Temperature distributions and reaction extent were recorded as a function of time. A 3D transient heat transfer model that links conduction–convection–radiation heat transfer to the chemical kinetics is formulated using wavelength and chemical composition dependent material properties and assuming the Rosseland diffusion approximation for the internal radiative transport. Monte-Carlo ray tracing is employed to obtain the radiative flux distribution at the boundaries. The unsteady energy equation is solved by finite volume technique. The model is validated by comparing the computed temperature and reaction extent variation with time to the values experimentally measured. |
doi_str_mv | 10.1016/j.ijheatmasstransfer.2003.10.010 |
format | article |
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3(s) into CaO(s) and CO
2(g) is selected as the model heterogeneous reaction. Its interfacial kinetic parameters are determined by thermogravimetric measurements assuming a contracting geometry rate law and an Arrhenius temperature dependence law. Experimentation using an Argon arc as the radiation source was carried out in which powder samples were subjected to radiative power fluxes in the range 400–930 kW/m
2. Temperature distributions and reaction extent were recorded as a function of time. A 3D transient heat transfer model that links conduction–convection–radiation heat transfer to the chemical kinetics is formulated using wavelength and chemical composition dependent material properties and assuming the Rosseland diffusion approximation for the internal radiative transport. Monte-Carlo ray tracing is employed to obtain the radiative flux distribution at the boundaries. The unsteady energy equation is solved by finite volume technique. The model is validated by comparing the computed temperature and reaction extent variation with time to the values experimentally measured.</description><identifier>ISSN: 0017-9310</identifier><identifier>EISSN: 1879-2189</identifier><identifier>DOI: 10.1016/j.ijheatmasstransfer.2003.10.010</identifier><identifier>CODEN: IJHMAK</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Heat transfer ; Theoretical studies. Data and constants. Metering</subject><ispartof>International journal of heat and mass transfer, 2004-04, Vol.47 (8), p.1907-1916</ispartof><rights>2003 Elsevier Ltd</rights><rights>2004 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c401t-bba1a60989677a2ebb0cf3673c67b237b3613535f855a50c344098e39e7885eb3</citedby><cites>FETCH-LOGICAL-c401t-bba1a60989677a2ebb0cf3673c67b237b3613535f855a50c344098e39e7885eb3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27923,27924</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=15556708$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Lipinski, W.</creatorcontrib><creatorcontrib>Steinfeld, A.</creatorcontrib><title>Heterogeneous thermochemical decomposition under direct irradiation</title><title>International journal of heat and mass transfer</title><description>Radiative heat transfer within a chemical reacting system directly exposed to an external source of high-flux radiation is considered. The endothermic decomposition of CaCO
3(s) into CaO(s) and CO
2(g) is selected as the model heterogeneous reaction. Its interfacial kinetic parameters are determined by thermogravimetric measurements assuming a contracting geometry rate law and an Arrhenius temperature dependence law. Experimentation using an Argon arc as the radiation source was carried out in which powder samples were subjected to radiative power fluxes in the range 400–930 kW/m
2. Temperature distributions and reaction extent were recorded as a function of time. A 3D transient heat transfer model that links conduction–convection–radiation heat transfer to the chemical kinetics is formulated using wavelength and chemical composition dependent material properties and assuming the Rosseland diffusion approximation for the internal radiative transport. Monte-Carlo ray tracing is employed to obtain the radiative flux distribution at the boundaries. The unsteady energy equation is solved by finite volume technique. The model is validated by comparing the computed temperature and reaction extent variation with time to the values experimentally measured.</description><subject>Applied sciences</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Heat transfer</subject><subject>Theoretical studies. Data and constants. Metering</subject><issn>0017-9310</issn><issn>1879-2189</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2004</creationdate><recordtype>article</recordtype><recordid>eNqNkMFOwzAMhiMEEmPwDr2AuHQ4TZO0N9AEDDSJC5yjNHVZqrYZSYfE25OySRy4cLIsf_ptf4RcU1hQoOKmXdh2g3rsdQij10No0C8yABbHC6BwRGa0kGWa0aI8JjMAKtOSUTglZyG0Uwu5mJHlCkf07h0HdLuQjBv0vTMb7K3RXVKjcf3WBTtaNyS7oUaf1NajGRPrva6tngbn5KTRXcCLQ52Tt4f71-UqXb88Pi3v1qnJgY5pVWmqBZRFKaTUGVYVmIYJyYyQVcZkxQRlnPGm4FxzMCzPI4ysRFkUHCs2J1f73K13HzsMo-ptMNh1-ud4lRUZZLkoI3i7B413IXhs1NbbXvsvRUFN9lSr_tpTk72JiPZixOVhlw7RRBMZY8NvDudcSCgi97znMD7-aWNKMBYHg3tNqnb2_0u_AQKSktk</recordid><startdate>20040401</startdate><enddate>20040401</enddate><creator>Lipinski, W.</creator><creator>Steinfeld, A.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope></search><sort><creationdate>20040401</creationdate><title>Heterogeneous thermochemical decomposition under direct irradiation</title><author>Lipinski, W. ; Steinfeld, A.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c401t-bba1a60989677a2ebb0cf3673c67b237b3613535f855a50c344098e39e7885eb3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2004</creationdate><topic>Applied sciences</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Heat transfer</topic><topic>Theoretical studies. Data and constants. Metering</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Lipinski, W.</creatorcontrib><creatorcontrib>Steinfeld, A.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><jtitle>International journal of heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Lipinski, W.</au><au>Steinfeld, A.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Heterogeneous thermochemical decomposition under direct irradiation</atitle><jtitle>International journal of heat and mass transfer</jtitle><date>2004-04-01</date><risdate>2004</risdate><volume>47</volume><issue>8</issue><spage>1907</spage><epage>1916</epage><pages>1907-1916</pages><issn>0017-9310</issn><eissn>1879-2189</eissn><coden>IJHMAK</coden><abstract>Radiative heat transfer within a chemical reacting system directly exposed to an external source of high-flux radiation is considered. The endothermic decomposition of CaCO
3(s) into CaO(s) and CO
2(g) is selected as the model heterogeneous reaction. Its interfacial kinetic parameters are determined by thermogravimetric measurements assuming a contracting geometry rate law and an Arrhenius temperature dependence law. Experimentation using an Argon arc as the radiation source was carried out in which powder samples were subjected to radiative power fluxes in the range 400–930 kW/m
2. Temperature distributions and reaction extent were recorded as a function of time. A 3D transient heat transfer model that links conduction–convection–radiation heat transfer to the chemical kinetics is formulated using wavelength and chemical composition dependent material properties and assuming the Rosseland diffusion approximation for the internal radiative transport. Monte-Carlo ray tracing is employed to obtain the radiative flux distribution at the boundaries. The unsteady energy equation is solved by finite volume technique. The model is validated by comparing the computed temperature and reaction extent variation with time to the values experimentally measured.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijheatmasstransfer.2003.10.010</doi><tpages>10</tpages></addata></record> |
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subjects | Applied sciences Energy Energy. Thermal use of fuels Exact sciences and technology Heat transfer Theoretical studies. Data and constants. Metering |
title | Heterogeneous thermochemical decomposition under direct irradiation |
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