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Halouani Kamel | University of Sfax - Academia.edu
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Since 1997, he taught in the Tunisian Universities, courses on Thermodynamics, Fluid Mechanics, Transport Phenomena, Thermo-Mechanics of multiphase systems, Energy Conversion systems: Fuel cells and renewable Energies, Thermochemical and Electrochemical conversion processes, Fuel Processing Engineering. Dr Halouani is known internationally as an expert in thermochemical biomass conversion (pyrolysis, gasification hydrothermal liquefaction), Fuel Cells Modeling and heat and mass transfer in energy conversion and production systems. <br /><br />His expertise in these areas was recognized locally and internationally with his several invitations as reviewer in International Journals: J of Power sources, Int. J. of Hydrogen Energy, Energy & Fuels, Energy, Fuel cells, Sensors, Electrical Power & Energy Systems, Environmental Progress and Sustainable Energy, Energy for Sustainable Development, Numerical Heat Transfer (A), Applied Thermal Engineering, Fluid Dynamics & Materials Processing, J. of Electroanalytical Chemistry, Canadian Journal of Chemical Engineering, Chemical Engineering Communications,Energy Conversion and Management,… <br /><br />He is member of scientific committees of several National and International Conferences in Energy Engineering and Heat and Mass Transfer and a Jury member of several Masters and Doctorates diploma in the field. <br /><br />In 2009, Dr Halouani was selected by the US State Department as a Fulbright Visiting Scholar in Virginia Tech Polytechnic Institute and State University, Blacksburg, VA, USA.<br /><br />Dr Halouani has organized, chaired and Co-chaired several National and International Congress, Conferences and Special Sessions on Renewable Energy Conversion, Hydrogen and Fuel Cell, Heat and Mass Transfer Engineering. He was also an invited Speaker at several national and international conferences. Dr Halouani has 2 patents, over 40 articles in peer-reviewed international journals and more than 60 communications and 20 Invited talks in prestigious international conferences and meetings. He advised 7 PhD Thesis and about 30 Masters and 40 Final Engineering Projects.<br /><span class="u-fw700">Phone: </span>+21698954415<br /><b>Address: </b>IPEIS, BP:1172, 3018 Sfax, Tunisia<br /><div class="js-profile-less-about u-linkUnstyled u-tcGrayDarker u-textDecorationUnderline u-displayNone">less</div></div></div><div class="ri-section"><div class="ri-section-header"><span>Interests</span><a class="ri-more-link js-profile-ri-list-card" data-click-track="profile-user-info-primary-research-interest" data-has-card-for-ri-list="44382641">View All (14)</a></div><div class="ri-tags-container"><a data-click-track="profile-user-info-expand-research-interests" data-has-card-for-ri-list="44382641" href="https://www.academia.edu/Documents/in/Bioenergy_and_Biofuels"><div id="js-react-on-rails-context" style="display:none" data-rails-context="{"inMailer":false,"i18nLocale":"en","i18nDefaultLocale":"en","href":"https://uus.academia.edu/HalouaniKamel","location":"/HalouaniKamel","scheme":"https","host":"uus.academia.edu","port":null,"pathname":"/HalouaniKamel","search":null,"httpAcceptLanguage":null,"serverSide":false}"></div> <div class="js-react-on-rails-component" style="display:none" data-component-name="Pill" data-props="{"color":"gray","children":["Bioenergy and Biofuels"]}" data-trace="false" data-dom-id="Pill-react-component-25c1b137-6693-4b02-9c37-c8ae27045001"></div> <div id="Pill-react-component-25c1b137-6693-4b02-9c37-c8ae27045001"></div> </a><a data-click-track="profile-user-info-expand-research-interests" data-has-card-for-ri-list="44382641" href="https://www.academia.edu/Documents/in/Biomass_Pyrolysis"><div class="js-react-on-rails-component" style="display:none" data-component-name="Pill" data-props="{"color":"gray","children":["Biomass Pyrolysis"]}" data-trace="false" data-dom-id="Pill-react-component-45007d80-faef-4da4-8418-f8e263215f76"></div> <div id="Pill-react-component-45007d80-faef-4da4-8418-f8e263215f76"></div> </a><a data-click-track="profile-user-info-expand-research-interests" data-has-card-for-ri-list="44382641" href="https://www.academia.edu/Documents/in/Pyrolysis_of_Scrap_tyres"><div class="js-react-on-rails-component" style="display:none" data-component-name="Pill" data-props="{"color":"gray","children":["Pyrolysis of Scrap tyres"]}" data-trace="false" data-dom-id="Pill-react-component-8ed6af2b-5e64-4558-b9bf-6017ff502157"></div> <div id="Pill-react-component-8ed6af2b-5e64-4558-b9bf-6017ff502157"></div> </a><a data-click-track="profile-user-info-expand-research-interests" data-has-card-for-ri-list="44382641" href="https://www.academia.edu/Documents/in/Biomass_Pyrolysis_Biochar_Activated_Carbon"><div class="js-react-on-rails-component" style="display:none" data-component-name="Pill" data-props="{"color":"gray","children":["Biomass Pyrolysis, Biochar, Activated Carbon"]}" data-trace="false" data-dom-id="Pill-react-component-df0f8aa3-49e0-4ae9-a5c0-95af87f11c0c"></div> <div id="Pill-react-component-df0f8aa3-49e0-4ae9-a5c0-95af87f11c0c"></div> </a><a data-click-track="profile-user-info-expand-research-interests" data-has-card-for-ri-list="44382641" href="https://www.academia.edu/Documents/in/Fast_Pyrolysis"><div class="js-react-on-rails-component" style="display:none" data-component-name="Pill" data-props="{"color":"gray","children":["Fast Pyrolysis"]}" data-trace="false" data-dom-id="Pill-react-component-07347c97-5884-4d89-bf03-c0a9847b3130"></div> <div id="Pill-react-component-07347c97-5884-4d89-bf03-c0a9847b3130"></div> </a></div></div><div class="external-links-container"><ul class="profile-links new-profile js-UserInfo-social"><li class="left-most js-UserInfo-social-cv" data-broccoli-component="user-info.cv-button" data-click-track="profile-user-info-cv" data-cv-filename="CV-Kamel_Halouani-2022.pdf" data-placement="top" data-toggle="tooltip" href="/HalouaniKamel/CurriculumVitae"><button class="ds2-5-text-link ds2-5-text-link--small" style="font-size: 20px; letter-spacing: 0.8px"><span class="ds2-5-text-link__content">CV</span></button></li><li class="profile-profiles js-social-profiles-container"><i class="fa fa-spin fa-spinner"></i></li></ul></div></div></div><div class="right-panel-container"><div class="user-content-wrapper"><div class="uploads-container" id="social-redesign-work-container"><div class="upload-header"><h2 class="ds2-5-heading-sans-serif-xs">Uploads</h2></div><div class="documents-container backbone-social-profile-documents" style="width: 100%;"><div class="u-taCenter"></div><div class="profile--tab_content_container js-tab-pane tab-pane active" id="all"><div class="profile--tab_heading_container js-section-heading" data-section="Papers" id="Papers"><h3 class="profile--tab_heading_container">Papers by Halouani Kamel</h3></div><div class="js-work-strip profile--work_container" data-work-id="96244654"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/96244654/A_parametric_study_of_radiative_heat_transfer_in_pulverised_coal_furnaces"><img alt="Research paper thumbnail of A parametric study of radiative heat transfer in pulverised coal furnaces" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/96244654/A_parametric_study_of_radiative_heat_transfer_in_pulverised_coal_furnaces">A parametric study of radiative heat transfer in pulverised coal furnaces</a></div><div class="wp-workCard_item"><span>International Journal of Heat and Mass Transfer</span><span>, 2000</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. ...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. The absorption and scattering efficiencies and the phase function of coal, char and fly-ash particles are obtained from Lorenz-Mie theory and wavelength dependent optical ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="96244654"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="96244654"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 96244654; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=96244654]").text(description); $(".js-view-count[data-work-id=96244654]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 96244654; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='96244654']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 96244654, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=96244654]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":96244654,"title":"A parametric study of radiative heat transfer in pulverised coal furnaces","translated_title":"","metadata":{"abstract":"The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. The absorption and scattering efficiencies and the phase function of coal, char and fly-ash particles are obtained from Lorenz-Mie theory and wavelength dependent optical ...","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2000,"errors":{}},"publication_name":"International Journal of Heat and Mass Transfer"},"translated_abstract":"The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. The absorption and scattering efficiencies and the phase function of coal, char and fly-ash particles are obtained from Lorenz-Mie theory and wavelength dependent optical ...","internal_url":"https://www.academia.edu/96244654/A_parametric_study_of_radiative_heat_transfer_in_pulverised_coal_furnaces","translated_internal_url":"","created_at":"2023-02-03T10:06:45.243-08:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"A_parametric_study_of_radiative_heat_transfer_in_pulverised_coal_furnaces","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":504,"name":"Computational Physics","url":"https://www.academia.edu/Documents/in/Computational_Physics"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":512,"name":"Mechanics","url":"https://www.academia.edu/Documents/in/Mechanics"},{"id":6263,"name":"Combustion","url":"https://www.academia.edu/Documents/in/Combustion"},{"id":6974,"name":"Monte Carlo","url":"https://www.academia.edu/Documents/in/Monte_Carlo"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":13958,"name":"Media","url":"https://www.academia.edu/Documents/in/Media"},{"id":33661,"name":"Heat and Mass Transfer","url":"https://www.academia.edu/Documents/in/Heat_and_Mass_Transfer"},{"id":80414,"name":"Mathematical Sciences","url":"https://www.academia.edu/Documents/in/Mathematical_Sciences"},{"id":173601,"name":"Fly Ash","url":"https://www.academia.edu/Documents/in/Fly_Ash"},{"id":181850,"name":"Approximation","url":"https://www.academia.edu/Documents/in/Approximation"},{"id":185380,"name":"Optical Properties","url":"https://www.academia.edu/Documents/in/Optical_Properties"},{"id":888646,"name":"Furnaces","url":"https://www.academia.edu/Documents/in/Furnaces"},{"id":923420,"name":"Enclosures","url":"https://www.academia.edu/Documents/in/Enclosures"},{"id":1136005,"name":"Particle Size Distribution","url":"https://www.academia.edu/Documents/in/Particle_Size_Distribution"},{"id":1234689,"name":"Char","url":"https://www.academia.edu/Documents/in/Char"},{"id":1333436,"name":"Monte Carlo Method","url":"https://www.academia.edu/Documents/in/Monte_Carlo_Method"},{"id":2003399,"name":"Parametric Study","url":"https://www.academia.edu/Documents/in/Parametric_Study"},{"id":2353926,"name":"Isotropy","url":"https://www.academia.edu/Documents/in/Isotropy"}],"urls":[{"id":28658521,"url":"https://api.elsevier.com/content/article/PII:S0017931099003476?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="96244575"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/96244575/Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface"><img alt="Research paper thumbnail of Investigation of the chemical and electrochemical behaviour of mass transfer at an archaeological bronze/soil interface" class="work-thumbnail" src="https://attachments.academia-assets.com/98197237/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/96244575/Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface">Investigation of the chemical and electrochemical behaviour of mass transfer at an archaeological bronze/soil interface</a></div><div class="wp-workCard_item"><span>Anti-Corrosion Methods and Materials</span><span>, 2003</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">This paper describes a study on the corrosion behaviour of archaeological bronze in simulated gro...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">This paper describes a study on the corrosion behaviour of archaeological bronze in simulated groundwater by means of a simulated occluded cell. The study revealed migration, enrichment and deposition patterns of ions in the environment and the cations produced by anodic dissolution during localised corrosion of bronze. The cycle voltametry technique was utilised for the first time on the study of electrochemical behaviour of the bronze/simulated occluded solution interface. The potential and current peaks of oxidation‐reduction at the cathode and anode in the occluded solutions at various time intervals facilitated a study of the corrosion products formation processes and their formation speeds.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="ab1245bc5bf39554f82d3688527483ca" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":98197237,"asset_id":96244575,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/98197237/download_file?st=MTczMjUxMzY4Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="96244575"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="96244575"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 96244575; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=96244575]").text(description); $(".js-view-count[data-work-id=96244575]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 96244575; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='96244575']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 96244575, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "ab1245bc5bf39554f82d3688527483ca" } } $('.js-work-strip[data-work-id=96244575]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":96244575,"title":"Investigation of the chemical and electrochemical behaviour of mass transfer at an archaeological bronze/soil interface","translated_title":"","metadata":{"abstract":"This paper describes a study on the corrosion behaviour of archaeological bronze in simulated groundwater by means of a simulated occluded cell. The study revealed migration, enrichment and deposition patterns of ions in the environment and the cations produced by anodic dissolution during localised corrosion of bronze. The cycle voltametry technique was utilised for the first time on the study of electrochemical behaviour of the bronze/simulated occluded solution interface. The potential and current peaks of oxidation‐reduction at the cathode and anode in the occluded solutions at various time intervals facilitated a study of the corrosion products formation processes and their formation speeds.","publisher":"Emerald","publication_date":{"day":null,"month":null,"year":2003,"errors":{}},"publication_name":"Anti-Corrosion Methods and Materials"},"translated_abstract":"This paper describes a study on the corrosion behaviour of archaeological bronze in simulated groundwater by means of a simulated occluded cell. The study revealed migration, enrichment and deposition patterns of ions in the environment and the cations produced by anodic dissolution during localised corrosion of bronze. The cycle voltametry technique was utilised for the first time on the study of electrochemical behaviour of the bronze/simulated occluded solution interface. The potential and current peaks of oxidation‐reduction at the cathode and anode in the occluded solutions at various time intervals facilitated a study of the corrosion products formation processes and their formation speeds.","internal_url":"https://www.academia.edu/96244575/Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface","translated_internal_url":"","created_at":"2023-02-03T10:04:49.155-08:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":98197237,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/98197237/thumbnails/1.jpg","file_name":"j.jpowsour.2015.01.17120230203-1-1ew4lzc.pdf","download_url":"https://www.academia.edu/attachments/98197237/download_file?st=MTczMjUxMzY4Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Investigation_of_the_chemical_and_electr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/98197237/j.jpowsour.2015.01.17120230203-1-1ew4lzc-libre.pdf?1675450622=\u0026response-content-disposition=attachment%3B+filename%3DInvestigation_of_the_chemical_and_electr.pdf\u0026Expires=1732517282\u0026Signature=UWM-j~UfYRgJsvMZftmW5FOi~-FXtYB4XYYzpfuQcEluAJ1v8-DELhq4nSv8WJmqQPdX1nSA~pam0w~FTnc96Mh8j3AFSVzrTiq7pqTwFiIfITej-sqSSEzDceOd9KyytUiDYVyczgQdHxQMcXpxA8bYaPezy4~UJhsGoSiDW6X-178kMQZl22zixjrvG4eghIlhtfTJ8sU28GDYrf4QO-yBGseYjyLj3OvqZ1u-a82bPrRn1gc~zQqsIKXwbgcTbgq3vuJ6czxfU0t3SI3OC50ATlakkTV8elR04SZCB3LkekOlCUYTKbVhZ~s2F9nvRZJwZhFP04OK5TlbnhRRVg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface","translated_slug":"","page_count":12,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":98197237,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/98197237/thumbnails/1.jpg","file_name":"j.jpowsour.2015.01.17120230203-1-1ew4lzc.pdf","download_url":"https://www.academia.edu/attachments/98197237/download_file?st=MTczMjUxMzY4Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Investigation_of_the_chemical_and_electr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/98197237/j.jpowsour.2015.01.17120230203-1-1ew4lzc-libre.pdf?1675450622=\u0026response-content-disposition=attachment%3B+filename%3DInvestigation_of_the_chemical_and_electr.pdf\u0026Expires=1732517282\u0026Signature=UWM-j~UfYRgJsvMZftmW5FOi~-FXtYB4XYYzpfuQcEluAJ1v8-DELhq4nSv8WJmqQPdX1nSA~pam0w~FTnc96Mh8j3AFSVzrTiq7pqTwFiIfITej-sqSSEzDceOd9KyytUiDYVyczgQdHxQMcXpxA8bYaPezy4~UJhsGoSiDW6X-178kMQZl22zixjrvG4eghIlhtfTJ8sU28GDYrf4QO-yBGseYjyLj3OvqZ1u-a82bPrRn1gc~zQqsIKXwbgcTbgq3vuJ6czxfU0t3SI3OC50ATlakkTV8elR04SZCB3LkekOlCUYTKbVhZ~s2F9nvRZJwZhFP04OK5TlbnhRRVg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":6309,"name":"Metallurgy","url":"https://www.academia.edu/Documents/in/Metallurgy"},{"id":92948,"name":"Bronze","url":"https://www.academia.edu/Documents/in/Bronze"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"}],"urls":[{"id":28658480,"url":"http://www.emeraldinsight.com/doi/full-xml/10.1108/00035590310492234"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814518"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814518/Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier"><img alt="Research paper thumbnail of Comprehensive experimental investigation and numerical modeling of the combined partial oxidation-gasification zone in a pilot downdraft air-blown gasifier" class="work-thumbnail" src="https://attachments.academia-assets.com/93550641/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814518/Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier">Comprehensive experimental investigation and numerical modeling of the combined partial oxidation-gasification zone in a pilot downdraft air-blown gasifier</a></div><div class="wp-workCard_item"><span>Energy Conversion and Management</span><span>, 2017</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="4b98b63406b69de8c9e51b8cbfa2f12d" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550641,"asset_id":89814518,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550641/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814518"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814518"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814518; 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dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "4b98b63406b69de8c9e51b8cbfa2f12d" } } $('.js-work-strip[data-work-id=89814518]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814518,"title":"Comprehensive experimental investigation and numerical modeling of the combined partial oxidation-gasification zone in a pilot downdraft air-blown gasifier","translated_title":"","metadata":{"publisher":"Elsevier BV","grobid_abstract":"A pilot downdraft gasifier is investigated experimentally using almond shell biomass as feedstock. Experimental temperature profiles along the different zones of the gasifier are measured and overlapping regions between the different gasifier stratified zones is proved: we identified two main zones (dryingpyrolysis zone and partial oxidation-reduction zone) instead of four stratified zones as proposed in the literature. In light of this experimental finding, a two dimensional mathematical model is developed for the combined partial oxidation-reduction zone based on conservation equations coupled to the heterogeneous and homogeneous chemistry. Partial oxidation and thermal cracking mechanisms of tar are proposed based on the available kinetic data. The model is developed for the quasi-steady state period of the experiment and used to simulate the heat and mass transport fields within the computational domain, analyze the interaction between the heterogeneous and homogeneous reactions and evaluate the performance of the gasifier in terms of tar conversion and syngas composition. Validation against the mean experimental temperature data and the producer gas composition at the outlet of the reactor are presented and a satisfactory agreement is observed. The influence of pyrolysis gas composition, air flow rate and bed porosity on the process and its outputs is also investigated.","publication_date":{"day":null,"month":null,"year":2017,"errors":{}},"publication_name":"Energy Conversion and Management","grobid_abstract_attachment_id":93550641},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814518/Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier","translated_internal_url":"","created_at":"2022-11-02T12:34:17.316-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550641,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550641/thumbnails/1.jpg","file_name":"j.enconman.2017.04.04020221102-1-16hms5e.pdf","download_url":"https://www.academia.edu/attachments/93550641/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Comprehensive_experimental_investigation.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550641/j.enconman.2017.04.04020221102-1-16hms5e-libre.pdf?1667418941=\u0026response-content-disposition=attachment%3B+filename%3DComprehensive_experimental_investigation.pdf\u0026Expires=1732517283\u0026Signature=LzmAnY6ixQbKWErjkynrLt3H72YBqO-KnT2pogsffPhFnhs1YaWoJOanJdn663Nuhhaii~RYZgvg7hbCDgmm0bVhrlDeAuUZ54~h4VE2SAyn6Fhrpa7RLtAhlzB7-6wsaVmjBmtezzS8AEvgASvILNq6-m0KsHw1eSzQIWVI2Vo8xUmSf02t78-zTfjuB7A931NLCowT0~vg1xNY4nOcrYi2HCR-XxeDmQGVEplmPPg~jZ5a8NkU4JMrfKWHzwKDN46AAe~uOXhiSMu1LvxlMwEefIu7eC30Hl0Xl4QxUHqUDQimFeR-Z7F~4UF7dDLGMv2a~6qJywjq-DgzNRWuPg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier","translated_slug":"","page_count":19,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550641,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550641/thumbnails/1.jpg","file_name":"j.enconman.2017.04.04020221102-1-16hms5e.pdf","download_url":"https://www.academia.edu/attachments/93550641/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Comprehensive_experimental_investigation.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550641/j.enconman.2017.04.04020221102-1-16hms5e-libre.pdf?1667418941=\u0026response-content-disposition=attachment%3B+filename%3DComprehensive_experimental_investigation.pdf\u0026Expires=1732517283\u0026Signature=LzmAnY6ixQbKWErjkynrLt3H72YBqO-KnT2pogsffPhFnhs1YaWoJOanJdn663Nuhhaii~RYZgvg7hbCDgmm0bVhrlDeAuUZ54~h4VE2SAyn6Fhrpa7RLtAhlzB7-6wsaVmjBmtezzS8AEvgASvILNq6-m0KsHw1eSzQIWVI2Vo8xUmSf02t78-zTfjuB7A931NLCowT0~vg1xNY4nOcrYi2HCR-XxeDmQGVEplmPPg~jZ5a8NkU4JMrfKWHzwKDN46AAe~uOXhiSMu1LvxlMwEefIu7eC30Hl0Xl4QxUHqUDQimFeR-Z7F~4UF7dDLGMv2a~6qJywjq-DgzNRWuPg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":872370,"name":"Syngas","url":"https://www.academia.edu/Documents/in/Syngas"},{"id":1237788,"name":"Electrical And Electronic Engineering","url":"https://www.academia.edu/Documents/in/Electrical_And_Electronic_Engineering"}],"urls":[{"id":25459350,"url":"https://api.elsevier.com/content/article/PII:S0196890417303497?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); 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Design</span><span>, 2016</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="395a6ce3f2488ad4e1db938a86833ca9" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550639,"asset_id":89814517,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550639/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814517"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814517"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814517; 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Cell performance was determined (350 mW/cm² at 750 °C) in operating conditions propitious to carbon deposition. Cell performance with methanol was slightly higher than with hydrogen. Different reactants distribution adjacent to the double conducting electrolyte may explain the improved cell output. Better performance with methanol could be also consequence of the improved electronic conductivity in the presence of carbon deposits. Results indicated that catalytic decomposition of methanol in the anodic three phase boundaries is dependent of temperature and governed by a complex anodic electrochemical dynamics. Anode gases were analyzed and a process scheme including H 2 /CO/CH 3 OH has been proposed. An experimental protocol using a switch between hydrogen and methanol feed was elucidated and a series of chemical reactions was proposed inducing the coking removing from anode. For a pre-feasibility assessment of the experimental cell, performance comparison with Delphi Gen 3 cell fed by diesel used as element in an auxiliary power unit was proposed. Obtained results are encouraging to go down the thorny and long-pathway to make the APU-SOFC technology viable for the eco-transportation sector.","publication_date":{"day":null,"month":null,"year":2016,"errors":{}},"publication_name":"Materials \u0026amp; Design","grobid_abstract_attachment_id":93550639},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814517/Bio_methanol_fueled_intermediate_temperature_solid_oxide_fuel_cell_A_future_solution_as_component_in_auxiliary_power_unit_for_eco_transportation","translated_internal_url":"","created_at":"2022-11-02T12:34:17.122-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550639,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550639/thumbnails/1.jpg","file_name":"S0264127516302064.pdf","download_url":"https://www.academia.edu/attachments/93550639/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Bio_methanol_fueled_intermediate_tempera.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550639/S0264127516302064-libre.pdf?1667418927=\u0026response-content-disposition=attachment%3B+filename%3DBio_methanol_fueled_intermediate_tempera.pdf\u0026Expires=1732517283\u0026Signature=U4jDJuIVZxeR3pZ9tMnNbqhF3iRvutisQxYkk68WK3tEiS4rW4zO6BqiXKqMZz9oF4nvQCPEAgzvCAcRd24nGvzuoQcRbeDun6GPDh7Avxb5RgoczgfV82k8VxmAcS~QweJ1QfR-Ipll3LVAxPpoDDxto6OvQrTunQotSp0aQSMp9dbsw~HuXfP-wpHVO1LEbFdJXb-lBO~xNlsy4jutNmaGltC7ly49~kYfGZQUX3Gl-UgTpPziu8IK~xurjYA~gdpjZR6Ew8fJ~Uv~AVCyr8bjlfH55y2Wuz1JvnSvSWhvM88suJTDH1bYgp9SQcA5zltToKXp1jWNjuQ2NigXow__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Bio_methanol_fueled_intermediate_temperature_solid_oxide_fuel_cell_A_future_solution_as_component_in_auxiliary_power_unit_for_eco_transportation","translated_slug":"","page_count":27,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550639,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550639/thumbnails/1.jpg","file_name":"S0264127516302064.pdf","download_url":"https://www.academia.edu/attachments/93550639/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Bio_methanol_fueled_intermediate_tempera.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550639/S0264127516302064-libre.pdf?1667418927=\u0026response-content-disposition=attachment%3B+filename%3DBio_methanol_fueled_intermediate_tempera.pdf\u0026Expires=1732517283\u0026Signature=U4jDJuIVZxeR3pZ9tMnNbqhF3iRvutisQxYkk68WK3tEiS4rW4zO6BqiXKqMZz9oF4nvQCPEAgzvCAcRd24nGvzuoQcRbeDun6GPDh7Avxb5RgoczgfV82k8VxmAcS~QweJ1QfR-Ipll3LVAxPpoDDxto6OvQrTunQotSp0aQSMp9dbsw~HuXfP-wpHVO1LEbFdJXb-lBO~xNlsy4jutNmaGltC7ly49~kYfGZQUX3Gl-UgTpPziu8IK~xurjYA~gdpjZR6Ew8fJ~Uv~AVCyr8bjlfH55y2Wuz1JvnSvSWhvM88suJTDH1bYgp9SQcA5zltToKXp1jWNjuQ2NigXow__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":3771,"name":"Hydrogen","url":"https://www.academia.edu/Documents/in/Hydrogen"},{"id":112334,"name":"Methanol","url":"https://www.academia.edu/Documents/in/Methanol"},{"id":146840,"name":"Solid oxide fuel cell","url":"https://www.academia.edu/Documents/in/Solid_oxide_fuel_cell"},{"id":170389,"name":"Materials Design","url":"https://www.academia.edu/Documents/in/Materials_Design"},{"id":386271,"name":"Oxide","url":"https://www.academia.edu/Documents/in/Oxide"},{"id":1131651,"name":"Anode","url":"https://www.academia.edu/Documents/in/Anode"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"}],"urls":[{"id":25459349,"url":"https://api.elsevier.com/content/article/PII:S0264127516302064?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); 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The tube wall is subject to a constant heat flux density. Heat and mass transfer through the liquid are described by classical equations of continuity, momentum and energy. An overall good agreement was obtained with the experimental data of local heat transfer coefficient and pressure drop in the literature.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814514"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814514"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814514; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814514]").text(description); $(".js-view-count[data-work-id=89814514]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814514; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814514']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814514, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814514]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814514,"title":"Environmentally Friendly Refrigerants HFC refrigerants condensation inside smooth horizontal tubes","translated_title":"","metadata":{"abstract":"A theoretical analysis of heat transfer and pressures drop during the condensation of pure HFC refrigerants (and HCFC22) inside a horizontal smooth tube is developed. 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Indeed, 70% of the initial mass of anhydrous wood are found in the vapor as aerosols, ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814513"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814513"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814513; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814513]").text(description); $(".js-view-count[data-work-id=89814513]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814513; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814513']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814513, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814513]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814513,"title":"Depollution of atmospheric emissions of wood pyrolysis furnaces","translated_title":"","metadata":{"abstract":"The wood carbonization in Tunisia consists essentially of traditional activity using charcoaling stacks and pits characterized by high atmospheric pollution and poor energy conversion. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814512"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814512/Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_%C3%89tude_thermom%C3%A9canique_de_la_condensation_des_fluides_frigorig%C3%A8nes_purs_et_m%C3%A9langes_az%C3%A9otropes_et_quasi_az%C3%A9otropes_%C3%A0_lint%C3%A9rieur_dune_conduite_horizontale"><img alt="Research paper thumbnail of Thermomechanical study of the condensation of pure and mixed azeotropic and non-azeotropic refrigerating fluids in a horizontal tube | Étude thermomécanique de la condensation des fluides frigorigènes purs et mélanges azéotropes et quasi-azéotropes à l'intérieur d'une conduite horizontale" class="work-thumbnail" src="https://attachments.academia-assets.com/93550640/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814512/Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_%C3%89tude_thermom%C3%A9canique_de_la_condensation_des_fluides_frigorig%C3%A8nes_purs_et_m%C3%A9langes_az%C3%A9otropes_et_quasi_az%C3%A9otropes_%C3%A0_lint%C3%A9rieur_dune_conduite_horizontale">Thermomechanical study of the condensation of pure and mixed azeotropic and non-azeotropic refrigerating fluids in a horizontal tube | Étude thermomécanique de la condensation des fluides frigorigènes purs et mélanges azéotropes et quasi-azéotropes à l'intérieur d'une conduite horizontale</a></div><div class="wp-workCard_item"><span>Mecanique et Industries</span><span>, 2003</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="1143dadf3360db9da935b60f602f3a96" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550640,"asset_id":89814512,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550640/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814512"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814512"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814512; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814512]").text(description); $(".js-view-count[data-work-id=89814512]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814512; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814512']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814512, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "1143dadf3360db9da935b60f602f3a96" } } $('.js-work-strip[data-work-id=89814512]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814512,"title":"Thermomechanical study of the condensation of pure and mixed azeotropic and non-azeotropic refrigerating fluids in a horizontal tube | Étude thermomécanique de la condensation des fluides frigorigènes purs et mélanges azéotropes et quasi-azéotropes à l'intérieur d'une conduite horizontale","translated_title":"","metadata":{"grobid_abstract":"Un modèle physique est proposé pour l'étude de l'écoulement diphasique et du transfert thermique lors de la condensation en film et en régime stratifié à l'intérieur d'un tube lisse horizontal des réfrigérants purs R22, R134a, R32, R125 et des mélanges ; azéotrope (R32/R125) (60/40 %) et quasi-azéotrope R410a (R32/R125) (50/50 %). À partir de ce modèle, est élaborée la formulation mathématique en se basant sur les équations de conservation et des bilans à l'interface liquide-vapeur. Les résultats numériques, relatifs au transfert thermique, montrent un accord satisfaisant avec les données expérimentales disponibles dans la littérature. 2003 Éditions scientifiques et médicales Elsevier SAS. Tous droits réservés.","publication_date":{"day":null,"month":null,"year":2003,"errors":{}},"publication_name":"Mecanique et Industries","grobid_abstract_attachment_id":93550640},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814512/Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_%C3%89tude_thermom%C3%A9canique_de_la_condensation_des_fluides_frigorig%C3%A8nes_purs_et_m%C3%A9langes_az%C3%A9otropes_et_quasi_az%C3%A9otropes_%C3%A0_lint%C3%A9rieur_dune_conduite_horizontale","translated_internal_url":"","created_at":"2022-11-02T12:34:16.452-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550640,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550640/thumbnails/1.jpg","file_name":"s1296-2139_2803_2900036-820221102-1-2m7bx4.pdf","download_url":"https://www.academia.edu/attachments/93550640/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermomechanical_study_of_the_condensati.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550640/s1296-2139_2803_2900036-820221102-1-2m7bx4-libre.pdf?1667418924=\u0026response-content-disposition=attachment%3B+filename%3DThermomechanical_study_of_the_condensati.pdf\u0026Expires=1732517283\u0026Signature=YuPufRCO8tir--c5IhzkmAUuctyHW4J9L-UzivgjtRokL-d3Nce6VogpPELE5fw~fblYHKqSkbvNjd9u6LE7yIo~dvQivn~g7pB75DQOF-68LLpr~ycMz42rG-26r1wTcgVt1Ig8CGPOiB~wDhs7BQoOGaswesUehZDsmYUC2L2VtuzZweMASZHFYbtHbf9jGnOjlP9di-NSlr9Lks-dGqX2O8rbNVuiVtadSC8qc~exWkSSClN~fbheZbArzV1aySqvnJ03TokXlE10sA6~Bh31ITPc0mPUSOMfWF29pDptrtnn~1~GhSqgHIrqBx~Mx1zfAN6HglOTHDn9hUI-IA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_Étude_thermomécanique_de_la_condensation_des_fluides_frigorigènes_purs_et_mélanges_azéotropes_et_quasi_azéotropes_à_lintérieur_dune_conduite_horizontale","translated_slug":"","page_count":9,"language":"fr","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550640,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550640/thumbnails/1.jpg","file_name":"s1296-2139_2803_2900036-820221102-1-2m7bx4.pdf","download_url":"https://www.academia.edu/attachments/93550640/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermomechanical_study_of_the_condensati.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550640/s1296-2139_2803_2900036-820221102-1-2m7bx4-libre.pdf?1667418924=\u0026response-content-disposition=attachment%3B+filename%3DThermomechanical_study_of_the_condensati.pdf\u0026Expires=1732517283\u0026Signature=YuPufRCO8tir--c5IhzkmAUuctyHW4J9L-UzivgjtRokL-d3Nce6VogpPELE5fw~fblYHKqSkbvNjd9u6LE7yIo~dvQivn~g7pB75DQOF-68LLpr~ycMz42rG-26r1wTcgVt1Ig8CGPOiB~wDhs7BQoOGaswesUehZDsmYUC2L2VtuzZweMASZHFYbtHbf9jGnOjlP9di-NSlr9Lks-dGqX2O8rbNVuiVtadSC8qc~exWkSSClN~fbheZbArzV1aySqvnJ03TokXlE10sA6~Bh31ITPc0mPUSOMfWF29pDptrtnn~1~GhSqgHIrqBx~Mx1zfAN6HglOTHDn9hUI-IA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":522,"name":"Thermodynamics","url":"https://www.academia.edu/Documents/in/Thermodynamics"},{"id":8066,"name":"Two Phase Flow","url":"https://www.academia.edu/Documents/in/Two_Phase_Flow"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":184965,"name":"Theoretical Analysis","url":"https://www.academia.edu/Documents/in/Theoretical_Analysis"},{"id":634545,"name":"Condensation","url":"https://www.academia.edu/Documents/in/Condensation"},{"id":1120502,"name":"Experimental Data","url":"https://www.academia.edu/Documents/in/Experimental_Data"},{"id":1444222,"name":"Refrigerant","url":"https://www.academia.edu/Documents/in/Refrigerant"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814511"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814511/Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere"><img alt="Research paper thumbnail of Thermogravimetric analysis and kinetics modeling of isothermal carbonization of olive wood in inert atmosphere" class="work-thumbnail" src="https://attachments.academia-assets.com/93550647/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814511/Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere">Thermogravimetric analysis and kinetics modeling of isothermal carbonization of olive wood in inert atmosphere</a></div><div class="wp-workCard_item"><span>Thermochimica Acta</span><span>, 2006</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="4aec30bdac713027a66bbd4ceace0378" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550647,"asset_id":89814511,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550647/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814511"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814511"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814511; 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Measurements were carried out in a thermobalance for different fixed temperatures between 498 and 648 K. A two-stage semi-global kinetic model consisting of four sequential steps was proposed to derive kinetic parameters. The olive wood is classified in three pseudo-components. For the first two, similar thermal degradation mechanisms take place in a single reaction step. For the third, the thermal degradation takes place in two consecutive steps. The isothermal conditions allow the kinetic constants (activation energy and pre-exponential factors) to be estimated by means of the analytical solution of the mass conservation equations. An overall good agreement was obtained with activation energy values available in the literature.","publication_date":{"day":null,"month":null,"year":2006,"errors":{}},"publication_name":"Thermochimica Acta","grobid_abstract_attachment_id":93550647},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814511/Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere","translated_internal_url":"","created_at":"2022-11-02T12:34:16.214-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550647,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550647/thumbnails/1.jpg","file_name":"j.tca.2005.09.01820221102-1-14dh0zm.pdf","download_url":"https://www.academia.edu/attachments/93550647/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermogravimetric_analysis_and_kinetics.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550647/j.tca.2005.09.01820221102-1-14dh0zm-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3DThermogravimetric_analysis_and_kinetics.pdf\u0026Expires=1732517283\u0026Signature=G0eiJLwan5FYZGCoVuz6wReReMS4mAQcVIXBotpgAj~3TKwgqOnRG70gAFckpKNGks14ycnKLXzXbZGrjOfkTH-KcIDwRKiEFFOtqHVql59OxWy4AKPIejaZi2l8xf-VHVrYr-QrCaYEOLEBhkxw0GIrpDT-plkMzZFbl4pdEyFoX8fsMmL-LnwcurNuZP56ATPULzosdhGbrBsU4jM2W8FTvo~PttnZVSMFZTmO3rqIyxrj9epPapBaJTeeMyuq8qfbmq4jmj82AvXknmFVCVRCENqmG8fDyaOLbb7ZCzlK5aoZCR-CHS-ZpQX5HgXe-vvnav-~lF3O5r9OKCFkIg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere","translated_slug":"","page_count":8,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550647,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550647/thumbnails/1.jpg","file_name":"j.tca.2005.09.01820221102-1-14dh0zm.pdf","download_url":"https://www.academia.edu/attachments/93550647/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermogravimetric_analysis_and_kinetics.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550647/j.tca.2005.09.01820221102-1-14dh0zm-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3DThermogravimetric_analysis_and_kinetics.pdf\u0026Expires=1732517283\u0026Signature=G0eiJLwan5FYZGCoVuz6wReReMS4mAQcVIXBotpgAj~3TKwgqOnRG70gAFckpKNGks14ycnKLXzXbZGrjOfkTH-KcIDwRKiEFFOtqHVql59OxWy4AKPIejaZi2l8xf-VHVrYr-QrCaYEOLEBhkxw0GIrpDT-plkMzZFbl4pdEyFoX8fsMmL-LnwcurNuZP56ATPULzosdhGbrBsU4jM2W8FTvo~PttnZVSMFZTmO3rqIyxrj9epPapBaJTeeMyuq8qfbmq4jmj82AvXknmFVCVRCENqmG8fDyaOLbb7ZCzlK5aoZCR-CHS-ZpQX5HgXe-vvnav-~lF3O5r9OKCFkIg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":524,"name":"Analytical Chemistry","url":"https://www.academia.edu/Documents/in/Analytical_Chemistry"},{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics"},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling"},{"id":147640,"name":"Activation Energy","url":"https://www.academia.edu/Documents/in/Activation_Energy"},{"id":195204,"name":"TGA","url":"https://www.academia.edu/Documents/in/TGA"},{"id":345189,"name":"Carbonization","url":"https://www.academia.edu/Documents/in/Carbonization"},{"id":398652,"name":"Thermogravimetric Analysis","url":"https://www.academia.edu/Documents/in/Thermogravimetric_Analysis"},{"id":452650,"name":"Mass Conservation","url":"https://www.academia.edu/Documents/in/Mass_Conservation"},{"id":835697,"name":"Lumping Kinetic Model","url":"https://www.academia.edu/Documents/in/Lumping_Kinetic_Model"},{"id":1167882,"name":"Kinetic Parameter","url":"https://www.academia.edu/Documents/in/Kinetic_Parameter"},{"id":2263926,"name":"Inert Gas","url":"https://www.academia.edu/Documents/in/Inert_Gas"},{"id":2758069,"name":"Thermal Degradation","url":"https://www.academia.edu/Documents/in/Thermal_Degradation"},{"id":3849021,"name":"Kinetic model","url":"https://www.academia.edu/Documents/in/Kinetic_model"}],"urls":[{"id":25459348,"url":"https://api.elsevier.com/content/article/PII:S0040603105005009?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814510"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814510/2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier"><img alt="Research paper thumbnail of 2-D Modeling of thermo-kinetics coupled with heat and mass transfer in the reduction zone of a fixed bed downdraft biomass gasifier" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814510/2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier">2-D Modeling of thermo-kinetics coupled with heat and mass transfer in the reduction zone of a fixed bed downdraft biomass gasifier</a></div><div class="wp-workCard_item"><span>Renewable Energy</span><span>, 2014</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft b...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft biomass gasifier based on mass, energy and momentum conservation equations written for the solid and fluid phases and coupled with chemical kinetics. Kinetics parameters are derived from previous works and an effectiveness factor was used in the reaction rate correlation to quantify the mass transfer resistance in the bed. The obtained numerical results are compared with experimental and numerical data from literature and a reasonable agreement is observed. Fields of temperature, gaseous concentrations are investigated for the two-dimensional domain. Results show that the solid and fluid inlet temperatures to the reduction zone and the reactivity of the bio-char including the effectiveness factor are the main variables affecting the conversion of char to syngas in the gasification zone of the fixed bed reactor.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814510"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814510"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814510; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814510]").text(description); $(".js-view-count[data-work-id=89814510]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814510; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814510']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814510, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814510]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814510,"title":"2-D Modeling of thermo-kinetics coupled with heat and mass transfer in the reduction zone of a fixed bed downdraft biomass gasifier","translated_title":"","metadata":{"abstract":"ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft biomass gasifier based on mass, energy and momentum conservation equations written for the solid and fluid phases and coupled with chemical kinetics. Kinetics parameters are derived from previous works and an effectiveness factor was used in the reaction rate correlation to quantify the mass transfer resistance in the bed. The obtained numerical results are compared with experimental and numerical data from literature and a reasonable agreement is observed. Fields of temperature, gaseous concentrations are investigated for the two-dimensional domain. Results show that the solid and fluid inlet temperatures to the reduction zone and the reactivity of the bio-char including the effectiveness factor are the main variables affecting the conversion of char to syngas in the gasification zone of the fixed bed reactor.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2014,"errors":{}},"publication_name":"Renewable Energy"},"translated_abstract":"ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft biomass gasifier based on mass, energy and momentum conservation equations written for the solid and fluid phases and coupled with chemical kinetics. Kinetics parameters are derived from previous works and an effectiveness factor was used in the reaction rate correlation to quantify the mass transfer resistance in the bed. The obtained numerical results are compared with experimental and numerical data from literature and a reasonable agreement is observed. Fields of temperature, gaseous concentrations are investigated for the two-dimensional domain. Results show that the solid and fluid inlet temperatures to the reduction zone and the reactivity of the bio-char including the effectiveness factor are the main variables affecting the conversion of char to syngas in the gasification zone of the fixed bed reactor.","internal_url":"https://www.academia.edu/89814510/2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier","translated_internal_url":"","created_at":"2022-11-02T12:34:16.021-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":2738,"name":"Renewable Energy","url":"https://www.academia.edu/Documents/in/Renewable_Energy"},{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics"},{"id":5411,"name":"Biomass","url":"https://www.academia.edu/Documents/in/Biomass"},{"id":5413,"name":"Bioenergy","url":"https://www.academia.edu/Documents/in/Bioenergy"},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":33661,"name":"Heat and Mass Transfer","url":"https://www.academia.edu/Documents/in/Heat_and_Mass_Transfer"},{"id":39753,"name":"Activated Carbon","url":"https://www.academia.edu/Documents/in/Activated_Carbon"},{"id":54182,"name":"Biofuels","url":"https://www.academia.edu/Documents/in/Biofuels"},{"id":133177,"name":"Temperature","url":"https://www.academia.edu/Documents/in/Temperature"},{"id":161318,"name":"Mathematical Models","url":"https://www.academia.edu/Documents/in/Mathematical_Models"},{"id":213782,"name":"Renewable Resources","url":"https://www.academia.edu/Documents/in/Renewable_Resources"},{"id":319555,"name":"Momentum","url":"https://www.academia.edu/Documents/in/Momentum"},{"id":1237788,"name":"Electrical And Electronic Engineering","url":"https://www.academia.edu/Documents/in/Electrical_And_Electronic_Engineering"}],"urls":[{"id":25459347,"url":"https://api.elsevier.com/content/article/PII:S0960148113006939?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814509"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814509/Application_of_the_Finite_Volume_Method_to_Study_the_Effects_of_Baffles_on_Radiative_Heat_Transfer_in_Complex_Enclosures"><img alt="Research paper thumbnail of Application of the Finite-Volume Method to Study the Effects of Baffles on Radiative Heat Transfer in Complex Enclosures" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814509/Application_of_the_Finite_Volume_Method_to_Study_the_Effects_of_Baffles_on_Radiative_Heat_Transfer_in_Complex_Enclosures">Application of the Finite-Volume Method to Study the Effects of Baffles on Radiative Heat Transfer in Complex Enclosures</a></div><div class="wp-workCard_item"><span>Numerical Heat Transfer, Part A: Applications</span><span>, 2009</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">A finite-volume radiation model for participating gray media in 2-D and 3-D complex rectangular e...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">A finite-volume radiation model for participating gray media in 2-D and 3-D complex rectangular enclosures with obstacles is developed. The step and the bounded high-order resolution curved-line advection method (CLAM) schemes are examined. Using the ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814509"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814509"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814509; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814509]").text(description); $(".js-view-count[data-work-id=89814509]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814509; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814509']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814509, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814509]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814509,"title":"Application of the Finite-Volume Method to Study the Effects of Baffles on Radiative Heat Transfer in Complex Enclosures","translated_title":"","metadata":{"abstract":"A finite-volume radiation model for participating gray media in 2-D and 3-D complex rectangular enclosures with obstacles is developed. 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DCFC output is sensitive to electrolyte porosity and anode specific surface area.","publication_date":{"day":null,"month":null,"year":2014,"errors":{}},"publication_name":"Journal of Power Sources","grobid_abstract_attachment_id":93550636},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814508/2_D_numerical_modeling_and_experimental_investigation_of_electrochemical_mechanisms_coupled_with_heat_and_mass_transfer_in_a_planar_direct_carbon_fuel_cell","translated_internal_url":"","created_at":"2022-11-02T12:34:15.642-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550636,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550636/thumbnails/1.jpg","file_name":"j.jpowsour.2013.09.02420221102-1-v7k152.pdf","download_url":"https://www.academia.edu/attachments/93550636/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"2_D_numerical_modeling_and_experimental.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550636/j.jpowsour.2013.09.02420221102-1-v7k152-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3D2_D_numerical_modeling_and_experimental.pdf\u0026Expires=1732517283\u0026Signature=R3-31Js6knAQ8PBcJPFCLm~KBYChrzr5IRt-chArJJjvAJ32UKfJ4LG5O4YcNyOwX7VOsh5htlH-HuftIhevO9PYJTEs23BHwNI4499jiQ6s7lxN8kkIoMGvS6aj-eiEjJy5ZBSqTUEH1rL7aCoPbow0Jk4P0GBBXiCJhDRFk~tH0LG~cUJ3QcTfHr8S4Nm-hgtKhrl30DuwAGKrdn~g15ZeyGSyqzKJIYvqljt1AWiB9W4N3LiIQiLy4ic9XY1RAhbDzim6GIbMK~fg-xvhTjzT3P2aQTiEf2kk4ok4EqD3-b5RcG8MgPGWVe0PN26i5BhPg17U-P1gfUpwyQC~vg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"2_D_numerical_modeling_and_experimental_investigation_of_electrochemical_mechanisms_coupled_with_heat_and_mass_transfer_in_a_planar_direct_carbon_fuel_cell","translated_slug":"","page_count":14,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550636,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550636/thumbnails/1.jpg","file_name":"j.jpowsour.2013.09.02420221102-1-v7k152.pdf","download_url":"https://www.academia.edu/attachments/93550636/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"2_D_numerical_modeling_and_experimental.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550636/j.jpowsour.2013.09.02420221102-1-v7k152-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3D2_D_numerical_modeling_and_experimental.pdf\u0026Expires=1732517283\u0026Signature=R3-31Js6knAQ8PBcJPFCLm~KBYChrzr5IRt-chArJJjvAJ32UKfJ4LG5O4YcNyOwX7VOsh5htlH-HuftIhevO9PYJTEs23BHwNI4499jiQ6s7lxN8kkIoMGvS6aj-eiEjJy5ZBSqTUEH1rL7aCoPbow0Jk4P0GBBXiCJhDRFk~tH0LG~cUJ3QcTfHr8S4Nm-hgtKhrl30DuwAGKrdn~g15ZeyGSyqzKJIYvqljt1AWiB9W4N3LiIQiLy4ic9XY1RAhbDzim6GIbMK~fg-xvhTjzT3P2aQTiEf2kk4ok4EqD3-b5RcG8MgPGWVe0PN26i5BhPg17U-P1gfUpwyQC~vg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":1131650,"name":"Cathode","url":"https://www.academia.edu/Documents/in/Cathode"},{"id":1131651,"name":"Anode","url":"https://www.academia.edu/Documents/in/Anode"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"},{"id":1852738,"name":"Power Sources","url":"https://www.academia.edu/Documents/in/Power_Sources"}],"urls":[{"id":25459346,"url":"https://api.elsevier.com/content/article/PII:S0378775313015164?httpAccept=text/plain"}]}, dispatcherData: dispatcherData }); 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As an electrical power generator of power plants, it has a higher achievable efficiency (80%) than the Molten Carbonate (MCFC) and the Solid Oxide (SOFC) fuel cells, and has less emission than conventional coal-combustion power plants. In this paper, we propose a comparative study based on an analytical model for polarizations calculation in DCFC producing CO 2 and a mixture of (CO/CO 2) and using a carbonate melt (62 Li 2 CO 3 /38 K 2 CO 3 mol%) as electrolyte. The obtained results indicate that when the CO is taken into account in the anode side, the DCFC performance increases by 15% compared to only CO 2 producing DCFC system at the same operating conditions (moves from 1350 W m À2 to 1550 W m À2). Simulations lead to understand the effect of the operating conditions (temperature, cathodic gas composition and inlet cathodic pressure) on the performance of the DCFC in order to solve all constraints preventing the development of this type of fuel cell. The comparison of the obtained results with data from literature illustrates a relatively good agreement with an absolute average deviation of about 4%.","publication_date":{"day":null,"month":null,"year":2012,"errors":{}},"publication_name":"Journal of Electroanalytical Chemistry","grobid_abstract_attachment_id":93550642},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814507/Analytical_modeling_of_electrochemical_mechanisms_in_CO2_and_CO_CO2_producing_Direct_Carbon_Fuel_Cell","translated_internal_url":"","created_at":"2022-11-02T12:34:15.445-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550642,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550642/thumbnails/1.jpg","file_name":"j.jelechem.2012.01.01020221102-1-1l17vup.pdf","download_url":"https://www.academia.edu/attachments/93550642/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Analytical_modeling_of_electrochemical_m.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550642/j.jelechem.2012.01.01020221102-1-1l17vup-libre.pdf?1667418930=\u0026response-content-disposition=attachment%3B+filename%3DAnalytical_modeling_of_electrochemical_m.pdf\u0026Expires=1732517283\u0026Signature=d3997d87stNYDNwGTfUlERo0xIHvCHwskid1sVPyLs~mbzsVl0~vfqC2X1vNmSK0hyohEWLCGMsqCQTatT~e50XG-ZFkmbx5vFd8RKVGcaWx4cxb0DgJkq947qcSyxfnTFqmr71SimndeEslMlgvUAwhslPVHc8QhzlUIZzfPR-bTSsUh~P0B~pd-FoRaS4GUfb0IZlYUa0N-WkNGH91p~6O5M5Ae0hKzY~LyRqZEO9rIAZF8lhUZ2kgyOs-8pNmuFAAzRqEEFPtfElVw~fzCtV1u5yOXTcH997Mog5Nu0GvGiQz0ehJ1gla8Qn4UUf0CojjWg6bx1ERaA~d-3~S1w__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Analytical_modeling_of_electrochemical_mechanisms_in_CO2_and_CO_CO2_producing_Direct_Carbon_Fuel_Cell","translated_slug":"","page_count":8,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550642,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550642/thumbnails/1.jpg","file_name":"j.jelechem.2012.01.01020221102-1-1l17vup.pdf","download_url":"https://www.academia.edu/attachments/93550642/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Analytical_modeling_of_electrochemical_m.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550642/j.jelechem.2012.01.01020221102-1-1l17vup-libre.pdf?1667418930=\u0026response-content-disposition=attachment%3B+filename%3DAnalytical_modeling_of_electrochemical_m.pdf\u0026Expires=1732517283\u0026Signature=d3997d87stNYDNwGTfUlERo0xIHvCHwskid1sVPyLs~mbzsVl0~vfqC2X1vNmSK0hyohEWLCGMsqCQTatT~e50XG-ZFkmbx5vFd8RKVGcaWx4cxb0DgJkq947qcSyxfnTFqmr71SimndeEslMlgvUAwhslPVHc8QhzlUIZzfPR-bTSsUh~P0B~pd-FoRaS4GUfb0IZlYUa0N-WkNGH91p~6O5M5Ae0hKzY~LyRqZEO9rIAZF8lhUZ2kgyOs-8pNmuFAAzRqEEFPtfElVw~fzCtV1u5yOXTcH997Mog5Nu0GvGiQz0ehJ1gla8Qn4UUf0CojjWg6bx1ERaA~d-3~S1w__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":524,"name":"Analytical Chemistry","url":"https://www.academia.edu/Documents/in/Analytical_Chemistry"},{"id":4748,"name":"Electrochemistry","url":"https://www.academia.edu/Documents/in/Electrochemistry"},{"id":62806,"name":"Electroanalytical Chemistry","url":"https://www.academia.edu/Documents/in/Electroanalytical_Chemistry"},{"id":863497,"name":"Carbon Fibers","url":"https://www.academia.edu/Documents/in/Carbon_Fibers"}],"urls":[{"id":25459345,"url":"https://api.elsevier.com/content/article/PII:S1572665712000239?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814506"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814506/Mod%C3%A9lisation_des_transferts_radiatifs_dans_un_incin%C3%A9rateur_des_%C3%A9missions_polluantes_de_la_pyrolyse_du_bois"><img alt="Research paper thumbnail of Modélisation des transferts radiatifs dans un incinérateur des émissions polluantes de la pyrolyse du bois" class="work-thumbnail" src="https://attachments.academia-assets.com/93550643/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814506/Mod%C3%A9lisation_des_transferts_radiatifs_dans_un_incin%C3%A9rateur_des_%C3%A9missions_polluantes_de_la_pyrolyse_du_bois">Modélisation des transferts radiatifs dans un incinérateur des émissions polluantes de la pyrolyse du bois</a></div><div class="wp-workCard_item"><span>International Journal of Thermal Sciences</span><span>, 2004</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="f53c87f0358b8b925d6bee250c2033c9" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550643,"asset_id":89814506,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550643/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814506"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814506"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814506; 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Le calcul des propriétés radiatives d'un mélange de gaz et de suie est effectué à l'aide du modèle de somme pondérée de gaz gris (modèle SPGG). La symétrie axiale (thermique et radiative) du système ramène la résolution au cas d'une configuration bidimensionnelle. L'influence des principaux paramètres (émissivité, concentration de suie, rapport de pressions partielles) sur les distributions de flux net radiatif surfacique et de température au sein du milieu, est mise au point en considérant deux types de problèmes. Les résultats fournis par le code numérique élaboré sont en bon accord avec ceux obtenus par la méthode des rayons équivalents d'Hottel. Ce code assez souple peut tenir compte de différentes conditions aux limites et permet de modifier aisément l'ordre de discrétisation spatiale.","publication_date":{"day":null,"month":null,"year":2004,"errors":{}},"publication_name":"International Journal of Thermal Sciences","grobid_abstract_attachment_id":93550643},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814506/Mod%C3%A9lisation_des_transferts_radiatifs_dans_un_incin%C3%A9rateur_des_%C3%A9missions_polluantes_de_la_pyrolyse_du_bois","translated_internal_url":"","created_at":"2022-11-02T12:34:15.323-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550643,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550643/thumbnails/1.jpg","file_name":"j.ijthermalsci.2003.10.01320221102-1-157ld9v.pdf","download_url":"https://www.academia.edu/attachments/93550643/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Modelisation_des_transferts_radiatifs_da.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550643/j.ijthermalsci.2003.10.01320221102-1-157ld9v-libre.pdf?1667418928=\u0026response-content-disposition=attachment%3B+filename%3DModelisation_des_transferts_radiatifs_da.pdf\u0026Expires=1732517283\u0026Signature=VuP5W9tAwcE9m31IH2Uci62V8lUf8uLTg~5a55dhEodaIKM07Yvug~hB5PF0~QbdHFSTMwKRD4A9AyOEkHV3jFjObh7sBWk-2PUP6rrl0LHQHtQlWl43ZxbGfANo40SBwcoBvl~2v6zRSv~Upw4Osi6HKx8sm5xaxb5ZcdKZz7LW1QpKzMzUBzlAhsTvvTrcnPzh5SkZfO2lVsXysMCOlO1rSavSLsg51n2Tgni68Tju4wa9mZIPMsmJqRwwBJR2-TqN2rQM2mAjyVJSltuKbt78HQahLGZY5Uhe1syJClx-ehwejSuDsvWqRpY1CpvrMSwdANfNYyW5A~1sKXK~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Modélisation_des_transferts_radiatifs_dans_un_incinérateur_des_émissions_polluantes_de_la_pyrolyse_du_bois","translated_slug":"","page_count":12,"language":"fr","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550643,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550643/thumbnails/1.jpg","file_name":"j.ijthermalsci.2003.10.01320221102-1-157ld9v.pdf","download_url":"https://www.academia.edu/attachments/93550643/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Modelisation_des_transferts_radiatifs_da.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550643/j.ijthermalsci.2003.10.01320221102-1-157ld9v-libre.pdf?1667418928=\u0026response-content-disposition=attachment%3B+filename%3DModelisation_des_transferts_radiatifs_da.pdf\u0026Expires=1732517283\u0026Signature=VuP5W9tAwcE9m31IH2Uci62V8lUf8uLTg~5a55dhEodaIKM07Yvug~hB5PF0~QbdHFSTMwKRD4A9AyOEkHV3jFjObh7sBWk-2PUP6rrl0LHQHtQlWl43ZxbGfANo40SBwcoBvl~2v6zRSv~Upw4Osi6HKx8sm5xaxb5ZcdKZz7LW1QpKzMzUBzlAhsTvvTrcnPzh5SkZfO2lVsXysMCOlO1rSavSLsg51n2Tgni68Tju4wa9mZIPMsmJqRwwBJR2-TqN2rQM2mAjyVJSltuKbt78HQahLGZY5Uhe1syJClx-ehwejSuDsvWqRpY1CpvrMSwdANfNYyW5A~1sKXK~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":305,"name":"Applied Mathematics","url":"https://www.academia.edu/Documents/in/Applied_Mathematics"},{"id":498,"name":"Physics","url":"https://www.academia.edu/Documents/in/Physics"},{"id":951,"name":"Humanities","url":"https://www.academia.edu/Documents/in/Humanities"},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":60658,"name":"Numerical Simulation","url":"https://www.academia.edu/Documents/in/Numerical_Simulation"},{"id":67662,"name":"Incineration","url":"https://www.academia.edu/Documents/in/Incineration"},{"id":71578,"name":"Wood","url":"https://www.academia.edu/Documents/in/Wood"},{"id":187812,"name":"Thermal Sciences","url":"https://www.academia.edu/Documents/in/Thermal_Sciences"},{"id":355990,"name":"Gas combustion","url":"https://www.academia.edu/Documents/in/Gas_combustion"},{"id":442314,"name":"Radiative Transfer","url":"https://www.academia.edu/Documents/in/Radiative_Transfer"},{"id":554780,"name":"Interdisciplinary Engineering","url":"https://www.academia.edu/Documents/in/Interdisciplinary_Engineering"},{"id":742248,"name":"Incinerator","url":"https://www.academia.edu/Documents/in/Incinerator"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814505"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814505/Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination"><img alt="Research paper thumbnail of Experimental investigation of direct carbon fuel cell fueled by almond shell biochar: Part I. Physico-chemical characterization of the biochar fuel and cell performance examination" class="work-thumbnail" src="https://attachments.academia-assets.com/93550637/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814505/Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination">Experimental investigation of direct carbon fuel cell fueled by almond shell biochar: Part I. Physico-chemical characterization of the biochar fuel and cell performance examination</a></div><div class="wp-workCard_item"><span>International Journal of Hydrogen Energy</span><span>, 2013</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="90250c770ce314da84252ae8c2b5e3eb" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550637,"asset_id":89814505,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550637/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814505"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814505"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814505; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814505]").text(description); $(".js-view-count[data-work-id=89814505]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814505; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814505']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814505, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "90250c770ce314da84252ae8c2b5e3eb" } } $('.js-work-strip[data-work-id=89814505]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814505,"title":"Experimental investigation of direct carbon fuel cell fueled by almond shell biochar: Part I. Physico-chemical characterization of the biochar fuel and cell performance examination","translated_title":"","metadata":{"publisher":"Elsevier BV","grobid_abstract":"NiO-Samaria-Doped-Ceria (NiO-SDC) composite powders was synthesized by a traditional mechanical mixing process and tested as anode material for Direct Carbon Fuel Cell (DCFC), which uses almond shell biochar as fuel and molten carbonate-doped ceria composite as electrolyte. A three-layer pellet cell, viz. cathode (Lithiated NiO-SDC), composite electrolyte and anode (NiO-SDC) is fabricated by a die-pressing, screen printing and sintering method. In Part I, a bi-layer DCFC pellet powered by almond shell biochar was tested and demonstrated a good potential. In this paper, we report an improvement in the cell stability and performance by adding the (NiO-SDC) anode layer to the bi-layer pellet containing only cathode and electrolyte. The peak power density of the three-layer pellet cell at 700 C increases to reach 150 mW cm À2 instead of 127 mW cm À2 while, the stability period is ameliorated to be around 130 min. The results indicated that this porous anode material is promising as anode for DCFCs. The DCFC single cells experiments demonstrated that the anode polarization is dominating the total cell polarization. Therefore, improved power output could be achieved with an improved anode.","publication_date":{"day":null,"month":null,"year":2013,"errors":{}},"publication_name":"International Journal of Hydrogen Energy","grobid_abstract_attachment_id":93550637},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814505/Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination","translated_internal_url":"","created_at":"2022-11-02T12:34:14.889-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550637,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550637/thumbnails/1.jpg","file_name":"j.ijhydene.2013.07.06120221102-1-1vl6aeh.pdf","download_url":"https://www.academia.edu/attachments/93550637/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Experimental_investigation_of_direct_car.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550637/j.ijhydene.2013.07.06120221102-1-1vl6aeh-libre.pdf?1667418931=\u0026response-content-disposition=attachment%3B+filename%3DExperimental_investigation_of_direct_car.pdf\u0026Expires=1732517283\u0026Signature=bMPYtnrNAujNmcsWzRYhdhwkKDRMuZ2Tj87cA3ziiEBCSF9PSftTIo4CTSQ61nDAACtmSDFzPyAUbIDKhfxG6kvZvFa2Lv-t9s6hrJzlx8x9YVJalpBRfsSOodOKGp1X4qEFOWHjWMVHrDSV9zHhjXdj~FuWjLFUiffrOY-tXYxPFSsozJn32Chmj1U8dhiY0GjM-bzRUylTIvtTElIMHmqzlo9gRFEqePRTtDxw8x8KvyD4kMwuR~5Qh-HKV5E9TtggR3tf0ODzzjH0suWfK0LZ5tvk9N81K0JOZVDrx22ip~4REgMGcRk2KVihoEofUsQ9GHWzq34SM3r6s7s~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination","translated_slug":"","page_count":10,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550637,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550637/thumbnails/1.jpg","file_name":"j.ijhydene.2013.07.06120221102-1-1vl6aeh.pdf","download_url":"https://www.academia.edu/attachments/93550637/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Experimental_investigation_of_direct_car.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550637/j.ijhydene.2013.07.06120221102-1-1vl6aeh-libre.pdf?1667418931=\u0026response-content-disposition=attachment%3B+filename%3DExperimental_investigation_of_direct_car.pdf\u0026Expires=1732517283\u0026Signature=bMPYtnrNAujNmcsWzRYhdhwkKDRMuZ2Tj87cA3ziiEBCSF9PSftTIo4CTSQ61nDAACtmSDFzPyAUbIDKhfxG6kvZvFa2Lv-t9s6hrJzlx8x9YVJalpBRfsSOodOKGp1X4qEFOWHjWMVHrDSV9zHhjXdj~FuWjLFUiffrOY-tXYxPFSsozJn32Chmj1U8dhiY0GjM-bzRUylTIvtTElIMHmqzlo9gRFEqePRTtDxw8x8KvyD4kMwuR~5Qh-HKV5E9TtggR3tf0ODzzjH0suWfK0LZ5tvk9N81K0JOZVDrx22ip~4REgMGcRk2KVihoEofUsQ9GHWzq34SM3r6s7s~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":7477,"name":"Fuel Cells","url":"https://www.academia.edu/Documents/in/Fuel_Cells"},{"id":10023,"name":"BIOCHAR","url":"https://www.academia.edu/Documents/in/BIOCHAR"},{"id":104345,"name":"Hydrogen Energy","url":"https://www.academia.edu/Documents/in/Hydrogen_Energy"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":863497,"name":"Carbon Fibers","url":"https://www.academia.edu/Documents/in/Carbon_Fibers"}],"urls":[{"id":25459344,"url":"https://api.elsevier.com/content/article/PII:S0360319913021009?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814503"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814503/Three_dimensional_modeling_of_water_transport_in_PEMFC"><img alt="Research paper thumbnail of Three-dimensional modeling of water transport in PEMFC" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814503/Three_dimensional_modeling_of_water_transport_in_PEMFC">Three-dimensional modeling of water transport in PEMFC</a></div><div class="wp-workCard_item"><span>International Journal of Hydrogen Energy</span><span>, 2013</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a P...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a PEMFC. In order to capture the effects of liquid water on the performance of the fuel cell, all regions are modeled from the anode to the cathode as having finite thickness. The geometry of the bipolar plate is modeled in detail to capture the effect of liquid water accumulation under the channel rib. This model takes into account the effect of temperature and inlet RH of both the anode and cathode. The three-dimensional model ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814503"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814503"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814503; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814503]").text(description); $(".js-view-count[data-work-id=89814503]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814503; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814503']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814503, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814503]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814503,"title":"Three-dimensional modeling of water transport in PEMFC","translated_title":"","metadata":{"abstract":"Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a PEMFC. In order to capture the effects of liquid water on the performance of the fuel cell, all regions are modeled from the anode to the cathode as having finite thickness. The geometry of the bipolar plate is modeled in detail to capture the effect of liquid water accumulation under the channel rib. This model takes into account the effect of temperature and inlet RH of both the anode and cathode. The three-dimensional model ...","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2013,"errors":{}},"publication_name":"International Journal of Hydrogen Energy"},"translated_abstract":"Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a PEMFC. In order to capture the effects of liquid water on the performance of the fuel cell, all regions are modeled from the anode to the cathode as having finite thickness. The geometry of the bipolar plate is modeled in detail to capture the effect of liquid water accumulation under the channel rib. This model takes into account the effect of temperature and inlet RH of both the anode and cathode. The three-dimensional model ...","internal_url":"https://www.academia.edu/89814503/Three_dimensional_modeling_of_water_transport_in_PEMFC","translated_internal_url":"","created_at":"2022-11-02T12:34:14.707-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Three_dimensional_modeling_of_water_transport_in_PEMFC","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":512,"name":"Mechanics","url":"https://www.academia.edu/Documents/in/Mechanics"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":104345,"name":"Hydrogen Energy","url":"https://www.academia.edu/Documents/in/Hydrogen_Energy"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":568612,"name":"Finite Volume Method","url":"https://www.academia.edu/Documents/in/Finite_Volume_Method"},{"id":891610,"name":"Proton Exchange Membrane Fuel Cell","url":"https://www.academia.edu/Documents/in/Proton_Exchange_Membrane_Fuel_Cell"},{"id":1131650,"name":"Cathode","url":"https://www.academia.edu/Documents/in/Cathode"},{"id":1131651,"name":"Anode","url":"https://www.academia.edu/Documents/in/Anode"}],"urls":[{"id":25459343,"url":"https://api.elsevier.com/content/article/PII:S0360319912024627?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814501"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814501/Two_dimensional_modeling_of_electrochemical_and_transport_phenomena_in_the_porous_structures_of_a_PEMFC"><img alt="Research paper thumbnail of Two-dimensional modeling of electrochemical and transport phenomena in the porous structures of a PEMFC" class="work-thumbnail" src="https://attachments.academia-assets.com/93550638/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814501/Two_dimensional_modeling_of_electrochemical_and_transport_phenomena_in_the_porous_structures_of_a_PEMFC">Two-dimensional modeling of electrochemical and transport phenomena in the porous structures of a PEMFC</a></div><div class="wp-workCard_item"><span>International Journal of Hydrogen Energy</span><span>, 2009</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="ef0ebc201020d5fe7b442475e772f055" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550638,"asset_id":89814501,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550638/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814501"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814501"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814501; 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The catalyst layers and membrane are each considered as distinct regions with finite thickness and calculated properties such as permeability, local protonic conductivity, and local dissolved water diffusion. This finite thickness model enables to model accurately the protonic current in these regions with higher accuracy than using an infinitesimal interface. In addition, this model takes into account the effect of osmotic drag in the membrane and catalyst layers. General boundary conditions are implemented in a way taking into consideration any given species concentration at the fuel cell inlet, such as water vapor which is a very important parameter in determining the efficiency of fuel cells. Other operating parameters such as temperature, pressure and porosity of the porous structure are also investigated to characterize their effect on the fuel cell efficiency.","publication_date":{"day":null,"month":null,"year":2009,"errors":{}},"publication_name":"International Journal of Hydrogen Energy","grobid_abstract_attachment_id":93550638},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814501/Two_dimensional_modeling_of_electrochemical_and_transport_phenomena_in_the_porous_structures_of_a_PEMFC","translated_internal_url":"","created_at":"2022-11-02T12:34:14.420-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550638,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550638/thumbnails/1.jpg","file_name":"j.ijhydene.2008.11.01220221102-1-1erpyvy.pdf","download_url":"https://www.academia.edu/attachments/93550638/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Two_dimensional_modeling_of_electrochemi.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550638/j.ijhydene.2008.11.01220221102-1-1erpyvy-libre.pdf?1667418932=\u0026response-content-disposition=attachment%3B+filename%3DTwo_dimensional_modeling_of_electrochemi.pdf\u0026Expires=1732517283\u0026Signature=HB6gA5NRGzCE2gXQ08YUjQZTHXUOm6twn2oF5rsnTU17daaGtjqYl~DL9ROP5RzMDb3zCr4ATHWbbxdot~8tpijojyjg124DFsl6atU0~43X8ZZGtGfFCDZLNlxorUmYAGgiymCdeBPblbH25Z4gJuR8VoaSyVMM4wwRVd1Xy00FjC-CxqxCWoRT1dNHEub7EWv5XHjv122EaC7zIuP1nAwmuZYv8AEv2HG329GX7LGSUgj1qOEtVmFFFKUP0I8fKYgpfrD~IDUxZktb2CQk-109gUW0BKd5h3WaKiCpBkS6wSfMRQHxsCG8ojWFjCGsqL~uMG5J~06ZK6jeQx3DfA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Two_dimensional_modeling_of_electrochemical_and_transport_phenomena_in_the_porous_structures_of_a_PEMFC","translated_slug":"","page_count":13,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550638,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550638/thumbnails/1.jpg","file_name":"j.ijhydene.2008.11.01220221102-1-1erpyvy.pdf","download_url":"https://www.academia.edu/attachments/93550638/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Two_dimensional_modeling_of_electrochemi.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550638/j.ijhydene.2008.11.01220221102-1-1erpyvy-libre.pdf?1667418932=\u0026response-content-disposition=attachment%3B+filename%3DTwo_dimensional_modeling_of_electrochemi.pdf\u0026Expires=1732517283\u0026Signature=HB6gA5NRGzCE2gXQ08YUjQZTHXUOm6twn2oF5rsnTU17daaGtjqYl~DL9ROP5RzMDb3zCr4ATHWbbxdot~8tpijojyjg124DFsl6atU0~43X8ZZGtGfFCDZLNlxorUmYAGgiymCdeBPblbH25Z4gJuR8VoaSyVMM4wwRVd1Xy00FjC-CxqxCWoRT1dNHEub7EWv5XHjv122EaC7zIuP1nAwmuZYv8AEv2HG329GX7LGSUgj1qOEtVmFFFKUP0I8fKYgpfrD~IDUxZktb2CQk-109gUW0BKd5h3WaKiCpBkS6wSfMRQHxsCG8ojWFjCGsqL~uMG5J~06ZK6jeQx3DfA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":3771,"name":"Hydrogen","url":"https://www.academia.edu/Documents/in/Hydrogen"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":24546,"name":"Transport phenomena","url":"https://www.academia.edu/Documents/in/Transport_phenomena"},{"id":27303,"name":"Fuel Cell","url":"https://www.academia.edu/Documents/in/Fuel_Cell"},{"id":104345,"name":"Hydrogen Energy","url":"https://www.academia.edu/Documents/in/Hydrogen_Energy"},{"id":199105,"name":"PEM fuel cell","url":"https://www.academia.edu/Documents/in/PEM_fuel_cell"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":332277,"name":"Finite Volume","url":"https://www.academia.edu/Documents/in/Finite_Volume"},{"id":497452,"name":"Numerical Model","url":"https://www.academia.edu/Documents/in/Numerical_Model"},{"id":800918,"name":"Charge transfer","url":"https://www.academia.edu/Documents/in/Charge_transfer"},{"id":867022,"name":"Boundary Condition","url":"https://www.academia.edu/Documents/in/Boundary_Condition"},{"id":1191377,"name":"Water Vapor","url":"https://www.academia.edu/Documents/in/Water_Vapor"}],"urls":[{"id":25459342,"url":"https://api.elsevier.com/content/article/PII:S0360319908014791?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814500"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814500/Effect_of_optical_properties_on_oscillatory_hydromagnetic_double_diffusive_convection_within_semitransparent_fluid"><img alt="Research paper thumbnail of Effect of optical properties on oscillatory hydromagnetic double-diffusive convection within semitransparent fluid" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814500/Effect_of_optical_properties_on_oscillatory_hydromagnetic_double_diffusive_convection_within_semitransparent_fluid">Effect of optical properties on oscillatory hydromagnetic double-diffusive convection within semitransparent fluid</a></div><div class="wp-workCard_item"><span>International Journal of Heat and Mass Transfer</span><span>, 2006</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dim...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dimensional rectangular enclosure is studied numerically for fixed Prandtl, Rayleigh, and Lewis numbers, Pr=13.6, Ra=105, Le=2. Uniform temperatures and concentrations are imposed along the vertical walls while the horizontal walls are assumed to be adiabatic and impermeable to mass transfer. The influences of the optical thickness and scattering</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814500"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814500"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814500; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814500]").text(description); $(".js-view-count[data-work-id=89814500]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814500; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814500']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814500, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814500]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814500,"title":"Effect of optical properties on oscillatory hydromagnetic double-diffusive convection within semitransparent fluid","translated_title":"","metadata":{"abstract":"The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dimensional rectangular enclosure is studied numerically for fixed Prandtl, Rayleigh, and Lewis numbers, Pr=13.6, Ra=105, Le=2. Uniform temperatures and concentrations are imposed along the vertical walls while the horizontal walls are assumed to be adiabatic and impermeable to mass transfer. The influences of the optical thickness and scattering","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2006,"errors":{}},"publication_name":"International Journal of Heat and Mass Transfer"},"translated_abstract":"The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dimensional rectangular enclosure is studied numerically for fixed Prandtl, Rayleigh, and Lewis numbers, Pr=13.6, Ra=105, Le=2. Uniform temperatures and concentrations are imposed along the vertical walls while the horizontal walls are assumed to be adiabatic and impermeable to mass transfer. The influences of the optical thickness and scattering","internal_url":"https://www.academia.edu/89814500/Effect_of_optical_properties_on_oscillatory_hydromagnetic_double_diffusive_convection_within_semitransparent_fluid","translated_internal_url":"","created_at":"2022-11-02T12:34:14.278-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_optical_properties_on_oscillatory_hydromagnetic_double_diffusive_convection_within_semitransparent_fluid","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":512,"name":"Mechanics","url":"https://www.academia.edu/Documents/in/Mechanics"},{"id":1327,"name":"Convection","url":"https://www.academia.edu/Documents/in/Convection"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":33661,"name":"Heat and Mass Transfer","url":"https://www.academia.edu/Documents/in/Heat_and_Mass_Transfer"},{"id":80414,"name":"Mathematical Sciences","url":"https://www.academia.edu/Documents/in/Mathematical_Sciences"},{"id":118582,"name":"Physical sciences","url":"https://www.academia.edu/Documents/in/Physical_sciences"},{"id":185380,"name":"Optical Properties","url":"https://www.academia.edu/Documents/in/Optical_Properties"},{"id":251375,"name":"Radiative Heat Transfer","url":"https://www.academia.edu/Documents/in/Radiative_Heat_Transfer"},{"id":387544,"name":"Double Diffusive Convection","url":"https://www.academia.edu/Documents/in/Double_Diffusive_Convection"},{"id":1119718,"name":"Initial Condition","url":"https://www.academia.edu/Documents/in/Initial_Condition"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814499"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814499/Effect_of_radiative_heat_transfer_on_the_three_dimensional_Boyancy_flow_in_cubic_enclosure_heated_from_the_side"><img alt="Research paper thumbnail of Effect of radiative heat transfer on the three-dimensional Boyancy flow in cubic enclosure heated from the side" class="work-thumbnail" src="https://attachments.academia-assets.com/93550672/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814499/Effect_of_radiative_heat_transfer_on_the_three_dimensional_Boyancy_flow_in_cubic_enclosure_heated_from_the_side">Effect of radiative heat transfer on the three-dimensional Boyancy flow in cubic enclosure heated from the side</a></div><div class="wp-workCard_item"><span>International Journal of Heat and Fluid Flow</span><span>, 2008</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="e987ddf539684155087f761bae710ba0" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550672,"asset_id":89814499,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550672/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814499"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814499"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814499; 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The natural convection equations, using the Boussinesq approximation for the treatment of buoyancy term in the momentum equation, are expressed using the vorticity-stream function formulation. These equations and the radiative transfer equation are discretized, respectively, with the control volume finite difference method and the FTn finite volume method. The successive relaxation-iterating scheme is used to solve the resultant algebraic system equations. Results show that the structure of the main flow is considerably altered by of the conduction-radiation parameter. The inner spiraling flows are found very sensible in location and direction to the radiative heat transfer. However, the peripheral spiraling motion is qualitatively insensitive to these parameters. 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thumbnail of A parametric study of radiative heat transfer in pulverised coal furnaces" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/96244654/A_parametric_study_of_radiative_heat_transfer_in_pulverised_coal_furnaces">A parametric study of radiative heat transfer in pulverised coal furnaces</a></div><div class="wp-workCard_item"><span>International Journal of Heat and Mass Transfer</span><span>, 2000</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. ...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. The absorption and scattering efficiencies and the phase function of coal, char and fly-ash particles are obtained from Lorenz-Mie theory and wavelength dependent optical ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="96244654"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="96244654"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 96244654; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=96244654]").text(description); $(".js-view-count[data-work-id=96244654]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 96244654; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='96244654']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 96244654, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=96244654]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":96244654,"title":"A parametric study of radiative heat transfer in pulverised coal furnaces","translated_title":"","metadata":{"abstract":"The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. The absorption and scattering efficiencies and the phase function of coal, char and fly-ash particles are obtained from Lorenz-Mie theory and wavelength dependent optical ...","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2000,"errors":{}},"publication_name":"International Journal of Heat and Mass Transfer"},"translated_abstract":"The P-1 approximation and the Monte Carlo method are applied in cylindrical coal-fired furnaces. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="96244575"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/96244575/Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface"><img alt="Research paper thumbnail of Investigation of the chemical and electrochemical behaviour of mass transfer at an archaeological bronze/soil interface" class="work-thumbnail" src="https://attachments.academia-assets.com/98197237/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/96244575/Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface">Investigation of the chemical and electrochemical behaviour of mass transfer at an archaeological bronze/soil interface</a></div><div class="wp-workCard_item"><span>Anti-Corrosion Methods and Materials</span><span>, 2003</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">This paper describes a study on the corrosion behaviour of archaeological bronze in simulated gro...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">This paper describes a study on the corrosion behaviour of archaeological bronze in simulated groundwater by means of a simulated occluded cell. The study revealed migration, enrichment and deposition patterns of ions in the environment and the cations produced by anodic dissolution during localised corrosion of bronze. The cycle voltametry technique was utilised for the first time on the study of electrochemical behaviour of the bronze/simulated occluded solution interface. The potential and current peaks of oxidation‐reduction at the cathode and anode in the occluded solutions at various time intervals facilitated a study of the corrosion products formation processes and their formation speeds.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="ab1245bc5bf39554f82d3688527483ca" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":98197237,"asset_id":96244575,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/98197237/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="96244575"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="96244575"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 96244575; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=96244575]").text(description); $(".js-view-count[data-work-id=96244575]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 96244575; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='96244575']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 96244575, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "ab1245bc5bf39554f82d3688527483ca" } } $('.js-work-strip[data-work-id=96244575]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":96244575,"title":"Investigation of the chemical and electrochemical behaviour of mass transfer at an archaeological bronze/soil interface","translated_title":"","metadata":{"abstract":"This paper describes a study on the corrosion behaviour of archaeological bronze in simulated groundwater by means of a simulated occluded cell. The study revealed migration, enrichment and deposition patterns of ions in the environment and the cations produced by anodic dissolution during localised corrosion of bronze. The cycle voltametry technique was utilised for the first time on the study of electrochemical behaviour of the bronze/simulated occluded solution interface. The potential and current peaks of oxidation‐reduction at the cathode and anode in the occluded solutions at various time intervals facilitated a study of the corrosion products formation processes and their formation speeds.","publisher":"Emerald","publication_date":{"day":null,"month":null,"year":2003,"errors":{}},"publication_name":"Anti-Corrosion Methods and Materials"},"translated_abstract":"This paper describes a study on the corrosion behaviour of archaeological bronze in simulated groundwater by means of a simulated occluded cell. The study revealed migration, enrichment and deposition patterns of ions in the environment and the cations produced by anodic dissolution during localised corrosion of bronze. The cycle voltametry technique was utilised for the first time on the study of electrochemical behaviour of the bronze/simulated occluded solution interface. The potential and current peaks of oxidation‐reduction at the cathode and anode in the occluded solutions at various time intervals facilitated a study of the corrosion products formation processes and their formation speeds.","internal_url":"https://www.academia.edu/96244575/Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface","translated_internal_url":"","created_at":"2023-02-03T10:04:49.155-08:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":98197237,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/98197237/thumbnails/1.jpg","file_name":"j.jpowsour.2015.01.17120230203-1-1ew4lzc.pdf","download_url":"https://www.academia.edu/attachments/98197237/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Investigation_of_the_chemical_and_electr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/98197237/j.jpowsour.2015.01.17120230203-1-1ew4lzc-libre.pdf?1675450622=\u0026response-content-disposition=attachment%3B+filename%3DInvestigation_of_the_chemical_and_electr.pdf\u0026Expires=1732517282\u0026Signature=UWM-j~UfYRgJsvMZftmW5FOi~-FXtYB4XYYzpfuQcEluAJ1v8-DELhq4nSv8WJmqQPdX1nSA~pam0w~FTnc96Mh8j3AFSVzrTiq7pqTwFiIfITej-sqSSEzDceOd9KyytUiDYVyczgQdHxQMcXpxA8bYaPezy4~UJhsGoSiDW6X-178kMQZl22zixjrvG4eghIlhtfTJ8sU28GDYrf4QO-yBGseYjyLj3OvqZ1u-a82bPrRn1gc~zQqsIKXwbgcTbgq3vuJ6czxfU0t3SI3OC50ATlakkTV8elR04SZCB3LkekOlCUYTKbVhZ~s2F9nvRZJwZhFP04OK5TlbnhRRVg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Investigation_of_the_chemical_and_electrochemical_behaviour_of_mass_transfer_at_an_archaeological_bronze_soil_interface","translated_slug":"","page_count":12,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":98197237,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/98197237/thumbnails/1.jpg","file_name":"j.jpowsour.2015.01.17120230203-1-1ew4lzc.pdf","download_url":"https://www.academia.edu/attachments/98197237/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Investigation_of_the_chemical_and_electr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/98197237/j.jpowsour.2015.01.17120230203-1-1ew4lzc-libre.pdf?1675450622=\u0026response-content-disposition=attachment%3B+filename%3DInvestigation_of_the_chemical_and_electr.pdf\u0026Expires=1732517282\u0026Signature=UWM-j~UfYRgJsvMZftmW5FOi~-FXtYB4XYYzpfuQcEluAJ1v8-DELhq4nSv8WJmqQPdX1nSA~pam0w~FTnc96Mh8j3AFSVzrTiq7pqTwFiIfITej-sqSSEzDceOd9KyytUiDYVyczgQdHxQMcXpxA8bYaPezy4~UJhsGoSiDW6X-178kMQZl22zixjrvG4eghIlhtfTJ8sU28GDYrf4QO-yBGseYjyLj3OvqZ1u-a82bPrRn1gc~zQqsIKXwbgcTbgq3vuJ6czxfU0t3SI3OC50ATlakkTV8elR04SZCB3LkekOlCUYTKbVhZ~s2F9nvRZJwZhFP04OK5TlbnhRRVg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":6309,"name":"Metallurgy","url":"https://www.academia.edu/Documents/in/Metallurgy"},{"id":92948,"name":"Bronze","url":"https://www.academia.edu/Documents/in/Bronze"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"}],"urls":[{"id":28658480,"url":"http://www.emeraldinsight.com/doi/full-xml/10.1108/00035590310492234"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814518"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814518/Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier"><img alt="Research paper thumbnail of Comprehensive experimental investigation and numerical modeling of the combined partial oxidation-gasification zone in a pilot downdraft air-blown gasifier" class="work-thumbnail" src="https://attachments.academia-assets.com/93550641/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814518/Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier">Comprehensive experimental investigation and numerical modeling of the combined partial oxidation-gasification zone in a pilot downdraft air-blown gasifier</a></div><div class="wp-workCard_item"><span>Energy Conversion and Management</span><span>, 2017</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="4b98b63406b69de8c9e51b8cbfa2f12d" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550641,"asset_id":89814518,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550641/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814518"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814518"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814518; 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Experimental temperature profiles along the different zones of the gasifier are measured and overlapping regions between the different gasifier stratified zones is proved: we identified two main zones (dryingpyrolysis zone and partial oxidation-reduction zone) instead of four stratified zones as proposed in the literature. In light of this experimental finding, a two dimensional mathematical model is developed for the combined partial oxidation-reduction zone based on conservation equations coupled to the heterogeneous and homogeneous chemistry. Partial oxidation and thermal cracking mechanisms of tar are proposed based on the available kinetic data. The model is developed for the quasi-steady state period of the experiment and used to simulate the heat and mass transport fields within the computational domain, analyze the interaction between the heterogeneous and homogeneous reactions and evaluate the performance of the gasifier in terms of tar conversion and syngas composition. Validation against the mean experimental temperature data and the producer gas composition at the outlet of the reactor are presented and a satisfactory agreement is observed. The influence of pyrolysis gas composition, air flow rate and bed porosity on the process and its outputs is also investigated.","publication_date":{"day":null,"month":null,"year":2017,"errors":{}},"publication_name":"Energy Conversion and Management","grobid_abstract_attachment_id":93550641},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814518/Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier","translated_internal_url":"","created_at":"2022-11-02T12:34:17.316-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550641,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550641/thumbnails/1.jpg","file_name":"j.enconman.2017.04.04020221102-1-16hms5e.pdf","download_url":"https://www.academia.edu/attachments/93550641/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Comprehensive_experimental_investigation.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550641/j.enconman.2017.04.04020221102-1-16hms5e-libre.pdf?1667418941=\u0026response-content-disposition=attachment%3B+filename%3DComprehensive_experimental_investigation.pdf\u0026Expires=1732517283\u0026Signature=LzmAnY6ixQbKWErjkynrLt3H72YBqO-KnT2pogsffPhFnhs1YaWoJOanJdn663Nuhhaii~RYZgvg7hbCDgmm0bVhrlDeAuUZ54~h4VE2SAyn6Fhrpa7RLtAhlzB7-6wsaVmjBmtezzS8AEvgASvILNq6-m0KsHw1eSzQIWVI2Vo8xUmSf02t78-zTfjuB7A931NLCowT0~vg1xNY4nOcrYi2HCR-XxeDmQGVEplmPPg~jZ5a8NkU4JMrfKWHzwKDN46AAe~uOXhiSMu1LvxlMwEefIu7eC30Hl0Xl4QxUHqUDQimFeR-Z7F~4UF7dDLGMv2a~6qJywjq-DgzNRWuPg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Comprehensive_experimental_investigation_and_numerical_modeling_of_the_combined_partial_oxidation_gasification_zone_in_a_pilot_downdraft_air_blown_gasifier","translated_slug":"","page_count":19,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550641,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550641/thumbnails/1.jpg","file_name":"j.enconman.2017.04.04020221102-1-16hms5e.pdf","download_url":"https://www.academia.edu/attachments/93550641/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Comprehensive_experimental_investigation.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550641/j.enconman.2017.04.04020221102-1-16hms5e-libre.pdf?1667418941=\u0026response-content-disposition=attachment%3B+filename%3DComprehensive_experimental_investigation.pdf\u0026Expires=1732517283\u0026Signature=LzmAnY6ixQbKWErjkynrLt3H72YBqO-KnT2pogsffPhFnhs1YaWoJOanJdn663Nuhhaii~RYZgvg7hbCDgmm0bVhrlDeAuUZ54~h4VE2SAyn6Fhrpa7RLtAhlzB7-6wsaVmjBmtezzS8AEvgASvILNq6-m0KsHw1eSzQIWVI2Vo8xUmSf02t78-zTfjuB7A931NLCowT0~vg1xNY4nOcrYi2HCR-XxeDmQGVEplmPPg~jZ5a8NkU4JMrfKWHzwKDN46AAe~uOXhiSMu1LvxlMwEefIu7eC30Hl0Xl4QxUHqUDQimFeR-Z7F~4UF7dDLGMv2a~6qJywjq-DgzNRWuPg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":872370,"name":"Syngas","url":"https://www.academia.edu/Documents/in/Syngas"},{"id":1237788,"name":"Electrical And Electronic Engineering","url":"https://www.academia.edu/Documents/in/Electrical_And_Electronic_Engineering"}],"urls":[{"id":25459350,"url":"https://api.elsevier.com/content/article/PII:S0196890417303497?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); 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Cell performance was determined (350 mW/cm² at 750 °C) in operating conditions propitious to carbon deposition. Cell performance with methanol was slightly higher than with hydrogen. Different reactants distribution adjacent to the double conducting electrolyte may explain the improved cell output. Better performance with methanol could be also consequence of the improved electronic conductivity in the presence of carbon deposits. Results indicated that catalytic decomposition of methanol in the anodic three phase boundaries is dependent of temperature and governed by a complex anodic electrochemical dynamics. Anode gases were analyzed and a process scheme including H 2 /CO/CH 3 OH has been proposed. An experimental protocol using a switch between hydrogen and methanol feed was elucidated and a series of chemical reactions was proposed inducing the coking removing from anode. For a pre-feasibility assessment of the experimental cell, performance comparison with Delphi Gen 3 cell fed by diesel used as element in an auxiliary power unit was proposed. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814514"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814514/Environmentally_Friendly_Refrigerants_HFC_refrigerants_condensation_inside_smooth_horizontal_tubes"><img alt="Research paper thumbnail of Environmentally Friendly Refrigerants HFC refrigerants condensation inside smooth horizontal tubes" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814514/Environmentally_Friendly_Refrigerants_HFC_refrigerants_condensation_inside_smooth_horizontal_tubes">Environmentally Friendly Refrigerants HFC refrigerants condensation inside smooth horizontal tubes</a></div><div class="wp-workCard_item"><span>International Journal of Energy, Environment and Economics</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">A theoretical analysis of heat transfer and pressures drop during the condensation of pure HFC re...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">A theoretical analysis of heat transfer and pressures drop during the condensation of pure HFC refrigerants (and HCFC22) inside a horizontal smooth tube is developed. The tube wall is subject to a constant heat flux density. Heat and mass transfer through the liquid are described by classical equations of continuity, momentum and energy. An overall good agreement was obtained with the experimental data of local heat transfer coefficient and pressure drop in the literature.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814514"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814514"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814514; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814514]").text(description); $(".js-view-count[data-work-id=89814514]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814514; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814514']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814514, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814514]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814514,"title":"Environmentally Friendly Refrigerants HFC refrigerants condensation inside smooth horizontal tubes","translated_title":"","metadata":{"abstract":"A theoretical analysis of heat transfer and pressures drop during the condensation of pure HFC refrigerants (and HCFC22) inside a horizontal smooth tube is developed. 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Indeed, 70% of the initial mass of anhydrous wood are found in the vapor as aerosols, ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814513"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814513"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814513; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814513]").text(description); $(".js-view-count[data-work-id=89814513]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814513; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814513']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814513, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814513]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814513,"title":"Depollution of atmospheric emissions of wood pyrolysis furnaces","translated_title":"","metadata":{"abstract":"The wood carbonization in Tunisia consists essentially of traditional activity using charcoaling stacks and pits characterized by high atmospheric pollution and poor energy conversion. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814512"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814512/Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_%C3%89tude_thermom%C3%A9canique_de_la_condensation_des_fluides_frigorig%C3%A8nes_purs_et_m%C3%A9langes_az%C3%A9otropes_et_quasi_az%C3%A9otropes_%C3%A0_lint%C3%A9rieur_dune_conduite_horizontale"><img alt="Research paper thumbnail of Thermomechanical study of the condensation of pure and mixed azeotropic and non-azeotropic refrigerating fluids in a horizontal tube | Étude thermomécanique de la condensation des fluides frigorigènes purs et mélanges azéotropes et quasi-azéotropes à l'intérieur d'une conduite horizontale" class="work-thumbnail" src="https://attachments.academia-assets.com/93550640/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814512/Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_%C3%89tude_thermom%C3%A9canique_de_la_condensation_des_fluides_frigorig%C3%A8nes_purs_et_m%C3%A9langes_az%C3%A9otropes_et_quasi_az%C3%A9otropes_%C3%A0_lint%C3%A9rieur_dune_conduite_horizontale">Thermomechanical study of the condensation of pure and mixed azeotropic and non-azeotropic refrigerating fluids in a horizontal tube | Étude thermomécanique de la condensation des fluides frigorigènes purs et mélanges azéotropes et quasi-azéotropes à l'intérieur d'une conduite horizontale</a></div><div class="wp-workCard_item"><span>Mecanique et Industries</span><span>, 2003</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="1143dadf3360db9da935b60f602f3a96" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550640,"asset_id":89814512,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550640/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814512"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814512"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814512; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814512]").text(description); $(".js-view-count[data-work-id=89814512]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814512; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814512']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814512, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "1143dadf3360db9da935b60f602f3a96" } } $('.js-work-strip[data-work-id=89814512]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814512,"title":"Thermomechanical study of the condensation of pure and mixed azeotropic and non-azeotropic refrigerating fluids in a horizontal tube | Étude thermomécanique de la condensation des fluides frigorigènes purs et mélanges azéotropes et quasi-azéotropes à l'intérieur d'une conduite horizontale","translated_title":"","metadata":{"grobid_abstract":"Un modèle physique est proposé pour l'étude de l'écoulement diphasique et du transfert thermique lors de la condensation en film et en régime stratifié à l'intérieur d'un tube lisse horizontal des réfrigérants purs R22, R134a, R32, R125 et des mélanges ; azéotrope (R32/R125) (60/40 %) et quasi-azéotrope R410a (R32/R125) (50/50 %). À partir de ce modèle, est élaborée la formulation mathématique en se basant sur les équations de conservation et des bilans à l'interface liquide-vapeur. Les résultats numériques, relatifs au transfert thermique, montrent un accord satisfaisant avec les données expérimentales disponibles dans la littérature. 2003 Éditions scientifiques et médicales Elsevier SAS. Tous droits réservés.","publication_date":{"day":null,"month":null,"year":2003,"errors":{}},"publication_name":"Mecanique et Industries","grobid_abstract_attachment_id":93550640},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814512/Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_%C3%89tude_thermom%C3%A9canique_de_la_condensation_des_fluides_frigorig%C3%A8nes_purs_et_m%C3%A9langes_az%C3%A9otropes_et_quasi_az%C3%A9otropes_%C3%A0_lint%C3%A9rieur_dune_conduite_horizontale","translated_internal_url":"","created_at":"2022-11-02T12:34:16.452-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550640,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550640/thumbnails/1.jpg","file_name":"s1296-2139_2803_2900036-820221102-1-2m7bx4.pdf","download_url":"https://www.academia.edu/attachments/93550640/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermomechanical_study_of_the_condensati.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550640/s1296-2139_2803_2900036-820221102-1-2m7bx4-libre.pdf?1667418924=\u0026response-content-disposition=attachment%3B+filename%3DThermomechanical_study_of_the_condensati.pdf\u0026Expires=1732517283\u0026Signature=YuPufRCO8tir--c5IhzkmAUuctyHW4J9L-UzivgjtRokL-d3Nce6VogpPELE5fw~fblYHKqSkbvNjd9u6LE7yIo~dvQivn~g7pB75DQOF-68LLpr~ycMz42rG-26r1wTcgVt1Ig8CGPOiB~wDhs7BQoOGaswesUehZDsmYUC2L2VtuzZweMASZHFYbtHbf9jGnOjlP9di-NSlr9Lks-dGqX2O8rbNVuiVtadSC8qc~exWkSSClN~fbheZbArzV1aySqvnJ03TokXlE10sA6~Bh31ITPc0mPUSOMfWF29pDptrtnn~1~GhSqgHIrqBx~Mx1zfAN6HglOTHDn9hUI-IA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Thermomechanical_study_of_the_condensation_of_pure_and_mixed_azeotropic_and_non_azeotropic_refrigerating_fluids_in_a_horizontal_tube_Étude_thermomécanique_de_la_condensation_des_fluides_frigorigènes_purs_et_mélanges_azéotropes_et_quasi_azéotropes_à_lintérieur_dune_conduite_horizontale","translated_slug":"","page_count":9,"language":"fr","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550640,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550640/thumbnails/1.jpg","file_name":"s1296-2139_2803_2900036-820221102-1-2m7bx4.pdf","download_url":"https://www.academia.edu/attachments/93550640/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermomechanical_study_of_the_condensati.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550640/s1296-2139_2803_2900036-820221102-1-2m7bx4-libre.pdf?1667418924=\u0026response-content-disposition=attachment%3B+filename%3DThermomechanical_study_of_the_condensati.pdf\u0026Expires=1732517283\u0026Signature=YuPufRCO8tir--c5IhzkmAUuctyHW4J9L-UzivgjtRokL-d3Nce6VogpPELE5fw~fblYHKqSkbvNjd9u6LE7yIo~dvQivn~g7pB75DQOF-68LLpr~ycMz42rG-26r1wTcgVt1Ig8CGPOiB~wDhs7BQoOGaswesUehZDsmYUC2L2VtuzZweMASZHFYbtHbf9jGnOjlP9di-NSlr9Lks-dGqX2O8rbNVuiVtadSC8qc~exWkSSClN~fbheZbArzV1aySqvnJ03TokXlE10sA6~Bh31ITPc0mPUSOMfWF29pDptrtnn~1~GhSqgHIrqBx~Mx1zfAN6HglOTHDn9hUI-IA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":522,"name":"Thermodynamics","url":"https://www.academia.edu/Documents/in/Thermodynamics"},{"id":8066,"name":"Two Phase Flow","url":"https://www.academia.edu/Documents/in/Two_Phase_Flow"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":184965,"name":"Theoretical Analysis","url":"https://www.academia.edu/Documents/in/Theoretical_Analysis"},{"id":634545,"name":"Condensation","url":"https://www.academia.edu/Documents/in/Condensation"},{"id":1120502,"name":"Experimental Data","url":"https://www.academia.edu/Documents/in/Experimental_Data"},{"id":1444222,"name":"Refrigerant","url":"https://www.academia.edu/Documents/in/Refrigerant"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814511"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814511/Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere"><img alt="Research paper thumbnail of Thermogravimetric analysis and kinetics modeling of isothermal carbonization of olive wood in inert atmosphere" class="work-thumbnail" src="https://attachments.academia-assets.com/93550647/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814511/Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere">Thermogravimetric analysis and kinetics modeling of isothermal carbonization of olive wood in inert atmosphere</a></div><div class="wp-workCard_item"><span>Thermochimica Acta</span><span>, 2006</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="4aec30bdac713027a66bbd4ceace0378" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550647,"asset_id":89814511,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550647/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814511"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814511"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814511; 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Measurements were carried out in a thermobalance for different fixed temperatures between 498 and 648 K. A two-stage semi-global kinetic model consisting of four sequential steps was proposed to derive kinetic parameters. The olive wood is classified in three pseudo-components. For the first two, similar thermal degradation mechanisms take place in a single reaction step. For the third, the thermal degradation takes place in two consecutive steps. The isothermal conditions allow the kinetic constants (activation energy and pre-exponential factors) to be estimated by means of the analytical solution of the mass conservation equations. An overall good agreement was obtained with activation energy values available in the literature.","publication_date":{"day":null,"month":null,"year":2006,"errors":{}},"publication_name":"Thermochimica Acta","grobid_abstract_attachment_id":93550647},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814511/Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere","translated_internal_url":"","created_at":"2022-11-02T12:34:16.214-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550647,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550647/thumbnails/1.jpg","file_name":"j.tca.2005.09.01820221102-1-14dh0zm.pdf","download_url":"https://www.academia.edu/attachments/93550647/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermogravimetric_analysis_and_kinetics.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550647/j.tca.2005.09.01820221102-1-14dh0zm-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3DThermogravimetric_analysis_and_kinetics.pdf\u0026Expires=1732517283\u0026Signature=G0eiJLwan5FYZGCoVuz6wReReMS4mAQcVIXBotpgAj~3TKwgqOnRG70gAFckpKNGks14ycnKLXzXbZGrjOfkTH-KcIDwRKiEFFOtqHVql59OxWy4AKPIejaZi2l8xf-VHVrYr-QrCaYEOLEBhkxw0GIrpDT-plkMzZFbl4pdEyFoX8fsMmL-LnwcurNuZP56ATPULzosdhGbrBsU4jM2W8FTvo~PttnZVSMFZTmO3rqIyxrj9epPapBaJTeeMyuq8qfbmq4jmj82AvXknmFVCVRCENqmG8fDyaOLbb7ZCzlK5aoZCR-CHS-ZpQX5HgXe-vvnav-~lF3O5r9OKCFkIg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Thermogravimetric_analysis_and_kinetics_modeling_of_isothermal_carbonization_of_olive_wood_in_inert_atmosphere","translated_slug":"","page_count":8,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550647,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550647/thumbnails/1.jpg","file_name":"j.tca.2005.09.01820221102-1-14dh0zm.pdf","download_url":"https://www.academia.edu/attachments/93550647/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Thermogravimetric_analysis_and_kinetics.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550647/j.tca.2005.09.01820221102-1-14dh0zm-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3DThermogravimetric_analysis_and_kinetics.pdf\u0026Expires=1732517283\u0026Signature=G0eiJLwan5FYZGCoVuz6wReReMS4mAQcVIXBotpgAj~3TKwgqOnRG70gAFckpKNGks14ycnKLXzXbZGrjOfkTH-KcIDwRKiEFFOtqHVql59OxWy4AKPIejaZi2l8xf-VHVrYr-QrCaYEOLEBhkxw0GIrpDT-plkMzZFbl4pdEyFoX8fsMmL-LnwcurNuZP56ATPULzosdhGbrBsU4jM2W8FTvo~PttnZVSMFZTmO3rqIyxrj9epPapBaJTeeMyuq8qfbmq4jmj82AvXknmFVCVRCENqmG8fDyaOLbb7ZCzlK5aoZCR-CHS-ZpQX5HgXe-vvnav-~lF3O5r9OKCFkIg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":524,"name":"Analytical Chemistry","url":"https://www.academia.edu/Documents/in/Analytical_Chemistry"},{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics"},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling"},{"id":147640,"name":"Activation Energy","url":"https://www.academia.edu/Documents/in/Activation_Energy"},{"id":195204,"name":"TGA","url":"https://www.academia.edu/Documents/in/TGA"},{"id":345189,"name":"Carbonization","url":"https://www.academia.edu/Documents/in/Carbonization"},{"id":398652,"name":"Thermogravimetric Analysis","url":"https://www.academia.edu/Documents/in/Thermogravimetric_Analysis"},{"id":452650,"name":"Mass Conservation","url":"https://www.academia.edu/Documents/in/Mass_Conservation"},{"id":835697,"name":"Lumping Kinetic Model","url":"https://www.academia.edu/Documents/in/Lumping_Kinetic_Model"},{"id":1167882,"name":"Kinetic Parameter","url":"https://www.academia.edu/Documents/in/Kinetic_Parameter"},{"id":2263926,"name":"Inert Gas","url":"https://www.academia.edu/Documents/in/Inert_Gas"},{"id":2758069,"name":"Thermal Degradation","url":"https://www.academia.edu/Documents/in/Thermal_Degradation"},{"id":3849021,"name":"Kinetic model","url":"https://www.academia.edu/Documents/in/Kinetic_model"}],"urls":[{"id":25459348,"url":"https://api.elsevier.com/content/article/PII:S0040603105005009?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814510"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814510/2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier"><img alt="Research paper thumbnail of 2-D Modeling of thermo-kinetics coupled with heat and mass transfer in the reduction zone of a fixed bed downdraft biomass gasifier" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814510/2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier">2-D Modeling of thermo-kinetics coupled with heat and mass transfer in the reduction zone of a fixed bed downdraft biomass gasifier</a></div><div class="wp-workCard_item"><span>Renewable Energy</span><span>, 2014</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft b...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft biomass gasifier based on mass, energy and momentum conservation equations written for the solid and fluid phases and coupled with chemical kinetics. Kinetics parameters are derived from previous works and an effectiveness factor was used in the reaction rate correlation to quantify the mass transfer resistance in the bed. The obtained numerical results are compared with experimental and numerical data from literature and a reasonable agreement is observed. Fields of temperature, gaseous concentrations are investigated for the two-dimensional domain. Results show that the solid and fluid inlet temperatures to the reduction zone and the reactivity of the bio-char including the effectiveness factor are the main variables affecting the conversion of char to syngas in the gasification zone of the fixed bed reactor.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814510"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814510"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814510; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814510]").text(description); $(".js-view-count[data-work-id=89814510]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814510; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814510']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814510, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814510]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814510,"title":"2-D Modeling of thermo-kinetics coupled with heat and mass transfer in the reduction zone of a fixed bed downdraft biomass gasifier","translated_title":"","metadata":{"abstract":"ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft biomass gasifier based on mass, energy and momentum conservation equations written for the solid and fluid phases and coupled with chemical kinetics. Kinetics parameters are derived from previous works and an effectiveness factor was used in the reaction rate correlation to quantify the mass transfer resistance in the bed. The obtained numerical results are compared with experimental and numerical data from literature and a reasonable agreement is observed. Fields of temperature, gaseous concentrations are investigated for the two-dimensional domain. Results show that the solid and fluid inlet temperatures to the reduction zone and the reactivity of the bio-char including the effectiveness factor are the main variables affecting the conversion of char to syngas in the gasification zone of the fixed bed reactor.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2014,"errors":{}},"publication_name":"Renewable Energy"},"translated_abstract":"ABSTRACT A two dimensional modeling is developed in the reduction zone of a fixed bed downdraft biomass gasifier based on mass, energy and momentum conservation equations written for the solid and fluid phases and coupled with chemical kinetics. Kinetics parameters are derived from previous works and an effectiveness factor was used in the reaction rate correlation to quantify the mass transfer resistance in the bed. The obtained numerical results are compared with experimental and numerical data from literature and a reasonable agreement is observed. Fields of temperature, gaseous concentrations are investigated for the two-dimensional domain. Results show that the solid and fluid inlet temperatures to the reduction zone and the reactivity of the bio-char including the effectiveness factor are the main variables affecting the conversion of char to syngas in the gasification zone of the fixed bed reactor.","internal_url":"https://www.academia.edu/89814510/2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier","translated_internal_url":"","created_at":"2022-11-02T12:34:16.021-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"2_D_Modeling_of_thermo_kinetics_coupled_with_heat_and_mass_transfer_in_the_reduction_zone_of_a_fixed_bed_downdraft_biomass_gasifier","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":2738,"name":"Renewable Energy","url":"https://www.academia.edu/Documents/in/Renewable_Energy"},{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics"},{"id":5411,"name":"Biomass","url":"https://www.academia.edu/Documents/in/Biomass"},{"id":5413,"name":"Bioenergy","url":"https://www.academia.edu/Documents/in/Bioenergy"},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":33661,"name":"Heat and Mass Transfer","url":"https://www.academia.edu/Documents/in/Heat_and_Mass_Transfer"},{"id":39753,"name":"Activated Carbon","url":"https://www.academia.edu/Documents/in/Activated_Carbon"},{"id":54182,"name":"Biofuels","url":"https://www.academia.edu/Documents/in/Biofuels"},{"id":133177,"name":"Temperature","url":"https://www.academia.edu/Documents/in/Temperature"},{"id":161318,"name":"Mathematical Models","url":"https://www.academia.edu/Documents/in/Mathematical_Models"},{"id":213782,"name":"Renewable Resources","url":"https://www.academia.edu/Documents/in/Renewable_Resources"},{"id":319555,"name":"Momentum","url":"https://www.academia.edu/Documents/in/Momentum"},{"id":1237788,"name":"Electrical And Electronic Engineering","url":"https://www.academia.edu/Documents/in/Electrical_And_Electronic_Engineering"}],"urls":[{"id":25459347,"url":"https://api.elsevier.com/content/article/PII:S0960148113006939?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814509"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814509/Application_of_the_Finite_Volume_Method_to_Study_the_Effects_of_Baffles_on_Radiative_Heat_Transfer_in_Complex_Enclosures"><img alt="Research paper thumbnail of Application of the Finite-Volume Method to Study the Effects of Baffles on Radiative Heat Transfer in Complex Enclosures" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814509/Application_of_the_Finite_Volume_Method_to_Study_the_Effects_of_Baffles_on_Radiative_Heat_Transfer_in_Complex_Enclosures">Application of the Finite-Volume Method to Study the Effects of Baffles on Radiative Heat Transfer in Complex Enclosures</a></div><div class="wp-workCard_item"><span>Numerical Heat Transfer, Part A: Applications</span><span>, 2009</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">A finite-volume radiation model for participating gray media in 2-D and 3-D complex rectangular e...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">A finite-volume radiation model for participating gray media in 2-D and 3-D complex rectangular enclosures with obstacles is developed. The step and the bounded high-order resolution curved-line advection method (CLAM) schemes are examined. Using the ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814509"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814509"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814509; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814509]").text(description); $(".js-view-count[data-work-id=89814509]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814509; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814509']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814509, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814509]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814509,"title":"Application of the Finite-Volume Method to Study the Effects of Baffles on Radiative Heat Transfer in Complex Enclosures","translated_title":"","metadata":{"abstract":"A finite-volume radiation model for participating gray media in 2-D and 3-D complex rectangular enclosures with obstacles is developed. 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DCFC output is sensitive to electrolyte porosity and anode specific surface area.","publication_date":{"day":null,"month":null,"year":2014,"errors":{}},"publication_name":"Journal of Power Sources","grobid_abstract_attachment_id":93550636},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814508/2_D_numerical_modeling_and_experimental_investigation_of_electrochemical_mechanisms_coupled_with_heat_and_mass_transfer_in_a_planar_direct_carbon_fuel_cell","translated_internal_url":"","created_at":"2022-11-02T12:34:15.642-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550636,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550636/thumbnails/1.jpg","file_name":"j.jpowsour.2013.09.02420221102-1-v7k152.pdf","download_url":"https://www.academia.edu/attachments/93550636/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"2_D_numerical_modeling_and_experimental.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550636/j.jpowsour.2013.09.02420221102-1-v7k152-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3D2_D_numerical_modeling_and_experimental.pdf\u0026Expires=1732517283\u0026Signature=R3-31Js6knAQ8PBcJPFCLm~KBYChrzr5IRt-chArJJjvAJ32UKfJ4LG5O4YcNyOwX7VOsh5htlH-HuftIhevO9PYJTEs23BHwNI4499jiQ6s7lxN8kkIoMGvS6aj-eiEjJy5ZBSqTUEH1rL7aCoPbow0Jk4P0GBBXiCJhDRFk~tH0LG~cUJ3QcTfHr8S4Nm-hgtKhrl30DuwAGKrdn~g15ZeyGSyqzKJIYvqljt1AWiB9W4N3LiIQiLy4ic9XY1RAhbDzim6GIbMK~fg-xvhTjzT3P2aQTiEf2kk4ok4EqD3-b5RcG8MgPGWVe0PN26i5BhPg17U-P1gfUpwyQC~vg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"2_D_numerical_modeling_and_experimental_investigation_of_electrochemical_mechanisms_coupled_with_heat_and_mass_transfer_in_a_planar_direct_carbon_fuel_cell","translated_slug":"","page_count":14,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550636,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550636/thumbnails/1.jpg","file_name":"j.jpowsour.2013.09.02420221102-1-v7k152.pdf","download_url":"https://www.academia.edu/attachments/93550636/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"2_D_numerical_modeling_and_experimental.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550636/j.jpowsour.2013.09.02420221102-1-v7k152-libre.pdf?1667418926=\u0026response-content-disposition=attachment%3B+filename%3D2_D_numerical_modeling_and_experimental.pdf\u0026Expires=1732517283\u0026Signature=R3-31Js6knAQ8PBcJPFCLm~KBYChrzr5IRt-chArJJjvAJ32UKfJ4LG5O4YcNyOwX7VOsh5htlH-HuftIhevO9PYJTEs23BHwNI4499jiQ6s7lxN8kkIoMGvS6aj-eiEjJy5ZBSqTUEH1rL7aCoPbow0Jk4P0GBBXiCJhDRFk~tH0LG~cUJ3QcTfHr8S4Nm-hgtKhrl30DuwAGKrdn~g15ZeyGSyqzKJIYvqljt1AWiB9W4N3LiIQiLy4ic9XY1RAhbDzim6GIbMK~fg-xvhTjzT3P2aQTiEf2kk4ok4EqD3-b5RcG8MgPGWVe0PN26i5BhPg17U-P1gfUpwyQC~vg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":1131650,"name":"Cathode","url":"https://www.academia.edu/Documents/in/Cathode"},{"id":1131651,"name":"Anode","url":"https://www.academia.edu/Documents/in/Anode"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"},{"id":1852738,"name":"Power Sources","url":"https://www.academia.edu/Documents/in/Power_Sources"}],"urls":[{"id":25459346,"url":"https://api.elsevier.com/content/article/PII:S0378775313015164?httpAccept=text/plain"}]}, dispatcherData: dispatcherData }); 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As an electrical power generator of power plants, it has a higher achievable efficiency (80%) than the Molten Carbonate (MCFC) and the Solid Oxide (SOFC) fuel cells, and has less emission than conventional coal-combustion power plants. In this paper, we propose a comparative study based on an analytical model for polarizations calculation in DCFC producing CO 2 and a mixture of (CO/CO 2) and using a carbonate melt (62 Li 2 CO 3 /38 K 2 CO 3 mol%) as electrolyte. The obtained results indicate that when the CO is taken into account in the anode side, the DCFC performance increases by 15% compared to only CO 2 producing DCFC system at the same operating conditions (moves from 1350 W m À2 to 1550 W m À2). Simulations lead to understand the effect of the operating conditions (temperature, cathodic gas composition and inlet cathodic pressure) on the performance of the DCFC in order to solve all constraints preventing the development of this type of fuel cell. The comparison of the obtained results with data from literature illustrates a relatively good agreement with an absolute average deviation of about 4%.","publication_date":{"day":null,"month":null,"year":2012,"errors":{}},"publication_name":"Journal of Electroanalytical Chemistry","grobid_abstract_attachment_id":93550642},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814507/Analytical_modeling_of_electrochemical_mechanisms_in_CO2_and_CO_CO2_producing_Direct_Carbon_Fuel_Cell","translated_internal_url":"","created_at":"2022-11-02T12:34:15.445-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550642,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550642/thumbnails/1.jpg","file_name":"j.jelechem.2012.01.01020221102-1-1l17vup.pdf","download_url":"https://www.academia.edu/attachments/93550642/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Analytical_modeling_of_electrochemical_m.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550642/j.jelechem.2012.01.01020221102-1-1l17vup-libre.pdf?1667418930=\u0026response-content-disposition=attachment%3B+filename%3DAnalytical_modeling_of_electrochemical_m.pdf\u0026Expires=1732517283\u0026Signature=d3997d87stNYDNwGTfUlERo0xIHvCHwskid1sVPyLs~mbzsVl0~vfqC2X1vNmSK0hyohEWLCGMsqCQTatT~e50XG-ZFkmbx5vFd8RKVGcaWx4cxb0DgJkq947qcSyxfnTFqmr71SimndeEslMlgvUAwhslPVHc8QhzlUIZzfPR-bTSsUh~P0B~pd-FoRaS4GUfb0IZlYUa0N-WkNGH91p~6O5M5Ae0hKzY~LyRqZEO9rIAZF8lhUZ2kgyOs-8pNmuFAAzRqEEFPtfElVw~fzCtV1u5yOXTcH997Mog5Nu0GvGiQz0ehJ1gla8Qn4UUf0CojjWg6bx1ERaA~d-3~S1w__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Analytical_modeling_of_electrochemical_mechanisms_in_CO2_and_CO_CO2_producing_Direct_Carbon_Fuel_Cell","translated_slug":"","page_count":8,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550642,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550642/thumbnails/1.jpg","file_name":"j.jelechem.2012.01.01020221102-1-1l17vup.pdf","download_url":"https://www.academia.edu/attachments/93550642/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Analytical_modeling_of_electrochemical_m.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550642/j.jelechem.2012.01.01020221102-1-1l17vup-libre.pdf?1667418930=\u0026response-content-disposition=attachment%3B+filename%3DAnalytical_modeling_of_electrochemical_m.pdf\u0026Expires=1732517283\u0026Signature=d3997d87stNYDNwGTfUlERo0xIHvCHwskid1sVPyLs~mbzsVl0~vfqC2X1vNmSK0hyohEWLCGMsqCQTatT~e50XG-ZFkmbx5vFd8RKVGcaWx4cxb0DgJkq947qcSyxfnTFqmr71SimndeEslMlgvUAwhslPVHc8QhzlUIZzfPR-bTSsUh~P0B~pd-FoRaS4GUfb0IZlYUa0N-WkNGH91p~6O5M5Ae0hKzY~LyRqZEO9rIAZF8lhUZ2kgyOs-8pNmuFAAzRqEEFPtfElVw~fzCtV1u5yOXTcH997Mog5Nu0GvGiQz0ehJ1gla8Qn4UUf0CojjWg6bx1ERaA~d-3~S1w__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":524,"name":"Analytical Chemistry","url":"https://www.academia.edu/Documents/in/Analytical_Chemistry"},{"id":4748,"name":"Electrochemistry","url":"https://www.academia.edu/Documents/in/Electrochemistry"},{"id":62806,"name":"Electroanalytical Chemistry","url":"https://www.academia.edu/Documents/in/Electroanalytical_Chemistry"},{"id":863497,"name":"Carbon Fibers","url":"https://www.academia.edu/Documents/in/Carbon_Fibers"}],"urls":[{"id":25459345,"url":"https://api.elsevier.com/content/article/PII:S1572665712000239?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814506"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814506/Mod%C3%A9lisation_des_transferts_radiatifs_dans_un_incin%C3%A9rateur_des_%C3%A9missions_polluantes_de_la_pyrolyse_du_bois"><img alt="Research paper thumbnail of Modélisation des transferts radiatifs dans un incinérateur des émissions polluantes de la pyrolyse du bois" class="work-thumbnail" src="https://attachments.academia-assets.com/93550643/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814506/Mod%C3%A9lisation_des_transferts_radiatifs_dans_un_incin%C3%A9rateur_des_%C3%A9missions_polluantes_de_la_pyrolyse_du_bois">Modélisation des transferts radiatifs dans un incinérateur des émissions polluantes de la pyrolyse du bois</a></div><div class="wp-workCard_item"><span>International Journal of Thermal Sciences</span><span>, 2004</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="f53c87f0358b8b925d6bee250c2033c9" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550643,"asset_id":89814506,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550643/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814506"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814506"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814506; 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Le calcul des propriétés radiatives d'un mélange de gaz et de suie est effectué à l'aide du modèle de somme pondérée de gaz gris (modèle SPGG). La symétrie axiale (thermique et radiative) du système ramène la résolution au cas d'une configuration bidimensionnelle. L'influence des principaux paramètres (émissivité, concentration de suie, rapport de pressions partielles) sur les distributions de flux net radiatif surfacique et de température au sein du milieu, est mise au point en considérant deux types de problèmes. Les résultats fournis par le code numérique élaboré sont en bon accord avec ceux obtenus par la méthode des rayons équivalents d'Hottel. Ce code assez souple peut tenir compte de différentes conditions aux limites et permet de modifier aisément l'ordre de discrétisation spatiale.","publication_date":{"day":null,"month":null,"year":2004,"errors":{}},"publication_name":"International Journal of Thermal Sciences","grobid_abstract_attachment_id":93550643},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814506/Mod%C3%A9lisation_des_transferts_radiatifs_dans_un_incin%C3%A9rateur_des_%C3%A9missions_polluantes_de_la_pyrolyse_du_bois","translated_internal_url":"","created_at":"2022-11-02T12:34:15.323-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550643,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550643/thumbnails/1.jpg","file_name":"j.ijthermalsci.2003.10.01320221102-1-157ld9v.pdf","download_url":"https://www.academia.edu/attachments/93550643/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Modelisation_des_transferts_radiatifs_da.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550643/j.ijthermalsci.2003.10.01320221102-1-157ld9v-libre.pdf?1667418928=\u0026response-content-disposition=attachment%3B+filename%3DModelisation_des_transferts_radiatifs_da.pdf\u0026Expires=1732517283\u0026Signature=VuP5W9tAwcE9m31IH2Uci62V8lUf8uLTg~5a55dhEodaIKM07Yvug~hB5PF0~QbdHFSTMwKRD4A9AyOEkHV3jFjObh7sBWk-2PUP6rrl0LHQHtQlWl43ZxbGfANo40SBwcoBvl~2v6zRSv~Upw4Osi6HKx8sm5xaxb5ZcdKZz7LW1QpKzMzUBzlAhsTvvTrcnPzh5SkZfO2lVsXysMCOlO1rSavSLsg51n2Tgni68Tju4wa9mZIPMsmJqRwwBJR2-TqN2rQM2mAjyVJSltuKbt78HQahLGZY5Uhe1syJClx-ehwejSuDsvWqRpY1CpvrMSwdANfNYyW5A~1sKXK~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Modélisation_des_transferts_radiatifs_dans_un_incinérateur_des_émissions_polluantes_de_la_pyrolyse_du_bois","translated_slug":"","page_count":12,"language":"fr","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550643,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550643/thumbnails/1.jpg","file_name":"j.ijthermalsci.2003.10.01320221102-1-157ld9v.pdf","download_url":"https://www.academia.edu/attachments/93550643/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Modelisation_des_transferts_radiatifs_da.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550643/j.ijthermalsci.2003.10.01320221102-1-157ld9v-libre.pdf?1667418928=\u0026response-content-disposition=attachment%3B+filename%3DModelisation_des_transferts_radiatifs_da.pdf\u0026Expires=1732517283\u0026Signature=VuP5W9tAwcE9m31IH2Uci62V8lUf8uLTg~5a55dhEodaIKM07Yvug~hB5PF0~QbdHFSTMwKRD4A9AyOEkHV3jFjObh7sBWk-2PUP6rrl0LHQHtQlWl43ZxbGfANo40SBwcoBvl~2v6zRSv~Upw4Osi6HKx8sm5xaxb5ZcdKZz7LW1QpKzMzUBzlAhsTvvTrcnPzh5SkZfO2lVsXysMCOlO1rSavSLsg51n2Tgni68Tju4wa9mZIPMsmJqRwwBJR2-TqN2rQM2mAjyVJSltuKbt78HQahLGZY5Uhe1syJClx-ehwejSuDsvWqRpY1CpvrMSwdANfNYyW5A~1sKXK~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":305,"name":"Applied Mathematics","url":"https://www.academia.edu/Documents/in/Applied_Mathematics"},{"id":498,"name":"Physics","url":"https://www.academia.edu/Documents/in/Physics"},{"id":951,"name":"Humanities","url":"https://www.academia.edu/Documents/in/Humanities"},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling"},{"id":8067,"name":"Heat Transfer","url":"https://www.academia.edu/Documents/in/Heat_Transfer"},{"id":60658,"name":"Numerical Simulation","url":"https://www.academia.edu/Documents/in/Numerical_Simulation"},{"id":67662,"name":"Incineration","url":"https://www.academia.edu/Documents/in/Incineration"},{"id":71578,"name":"Wood","url":"https://www.academia.edu/Documents/in/Wood"},{"id":187812,"name":"Thermal Sciences","url":"https://www.academia.edu/Documents/in/Thermal_Sciences"},{"id":355990,"name":"Gas combustion","url":"https://www.academia.edu/Documents/in/Gas_combustion"},{"id":442314,"name":"Radiative Transfer","url":"https://www.academia.edu/Documents/in/Radiative_Transfer"},{"id":554780,"name":"Interdisciplinary Engineering","url":"https://www.academia.edu/Documents/in/Interdisciplinary_Engineering"},{"id":742248,"name":"Incinerator","url":"https://www.academia.edu/Documents/in/Incinerator"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814505"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814505/Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination"><img alt="Research paper thumbnail of Experimental investigation of direct carbon fuel cell fueled by almond shell biochar: Part I. Physico-chemical characterization of the biochar fuel and cell performance examination" class="work-thumbnail" src="https://attachments.academia-assets.com/93550637/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814505/Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination">Experimental investigation of direct carbon fuel cell fueled by almond shell biochar: Part I. Physico-chemical characterization of the biochar fuel and cell performance examination</a></div><div class="wp-workCard_item"><span>International Journal of Hydrogen Energy</span><span>, 2013</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="90250c770ce314da84252ae8c2b5e3eb" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550637,"asset_id":89814505,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550637/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814505"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814505"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814505; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814505]").text(description); $(".js-view-count[data-work-id=89814505]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814505; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814505']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814505, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "90250c770ce314da84252ae8c2b5e3eb" } } $('.js-work-strip[data-work-id=89814505]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814505,"title":"Experimental investigation of direct carbon fuel cell fueled by almond shell biochar: Part I. Physico-chemical characterization of the biochar fuel and cell performance examination","translated_title":"","metadata":{"publisher":"Elsevier BV","grobid_abstract":"NiO-Samaria-Doped-Ceria (NiO-SDC) composite powders was synthesized by a traditional mechanical mixing process and tested as anode material for Direct Carbon Fuel Cell (DCFC), which uses almond shell biochar as fuel and molten carbonate-doped ceria composite as electrolyte. A three-layer pellet cell, viz. cathode (Lithiated NiO-SDC), composite electrolyte and anode (NiO-SDC) is fabricated by a die-pressing, screen printing and sintering method. In Part I, a bi-layer DCFC pellet powered by almond shell biochar was tested and demonstrated a good potential. In this paper, we report an improvement in the cell stability and performance by adding the (NiO-SDC) anode layer to the bi-layer pellet containing only cathode and electrolyte. The peak power density of the three-layer pellet cell at 700 C increases to reach 150 mW cm À2 instead of 127 mW cm À2 while, the stability period is ameliorated to be around 130 min. The results indicated that this porous anode material is promising as anode for DCFCs. The DCFC single cells experiments demonstrated that the anode polarization is dominating the total cell polarization. Therefore, improved power output could be achieved with an improved anode.","publication_date":{"day":null,"month":null,"year":2013,"errors":{}},"publication_name":"International Journal of Hydrogen Energy","grobid_abstract_attachment_id":93550637},"translated_abstract":null,"internal_url":"https://www.academia.edu/89814505/Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination","translated_internal_url":"","created_at":"2022-11-02T12:34:14.889-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":93550637,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550637/thumbnails/1.jpg","file_name":"j.ijhydene.2013.07.06120221102-1-1vl6aeh.pdf","download_url":"https://www.academia.edu/attachments/93550637/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Experimental_investigation_of_direct_car.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550637/j.ijhydene.2013.07.06120221102-1-1vl6aeh-libre.pdf?1667418931=\u0026response-content-disposition=attachment%3B+filename%3DExperimental_investigation_of_direct_car.pdf\u0026Expires=1732517283\u0026Signature=bMPYtnrNAujNmcsWzRYhdhwkKDRMuZ2Tj87cA3ziiEBCSF9PSftTIo4CTSQ61nDAACtmSDFzPyAUbIDKhfxG6kvZvFa2Lv-t9s6hrJzlx8x9YVJalpBRfsSOodOKGp1X4qEFOWHjWMVHrDSV9zHhjXdj~FuWjLFUiffrOY-tXYxPFSsozJn32Chmj1U8dhiY0GjM-bzRUylTIvtTElIMHmqzlo9gRFEqePRTtDxw8x8KvyD4kMwuR~5Qh-HKV5E9TtggR3tf0ODzzjH0suWfK0LZ5tvk9N81K0JOZVDrx22ip~4REgMGcRk2KVihoEofUsQ9GHWzq34SM3r6s7s~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Experimental_investigation_of_direct_carbon_fuel_cell_fueled_by_almond_shell_biochar_Part_I_Physico_chemical_characterization_of_the_biochar_fuel_and_cell_performance_examination","translated_slug":"","page_count":10,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[{"id":93550637,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/93550637/thumbnails/1.jpg","file_name":"j.ijhydene.2013.07.06120221102-1-1vl6aeh.pdf","download_url":"https://www.academia.edu/attachments/93550637/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Experimental_investigation_of_direct_car.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/93550637/j.ijhydene.2013.07.06120221102-1-1vl6aeh-libre.pdf?1667418931=\u0026response-content-disposition=attachment%3B+filename%3DExperimental_investigation_of_direct_car.pdf\u0026Expires=1732517283\u0026Signature=bMPYtnrNAujNmcsWzRYhdhwkKDRMuZ2Tj87cA3ziiEBCSF9PSftTIo4CTSQ61nDAACtmSDFzPyAUbIDKhfxG6kvZvFa2Lv-t9s6hrJzlx8x9YVJalpBRfsSOodOKGp1X4qEFOWHjWMVHrDSV9zHhjXdj~FuWjLFUiffrOY-tXYxPFSsozJn32Chmj1U8dhiY0GjM-bzRUylTIvtTElIMHmqzlo9gRFEqePRTtDxw8x8KvyD4kMwuR~5Qh-HKV5E9TtggR3tf0ODzzjH0suWfK0LZ5tvk9N81K0JOZVDrx22ip~4REgMGcRk2KVihoEofUsQ9GHWzq34SM3r6s7s~3g__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":7477,"name":"Fuel Cells","url":"https://www.academia.edu/Documents/in/Fuel_Cells"},{"id":10023,"name":"BIOCHAR","url":"https://www.academia.edu/Documents/in/BIOCHAR"},{"id":104345,"name":"Hydrogen Energy","url":"https://www.academia.edu/Documents/in/Hydrogen_Energy"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":863497,"name":"Carbon Fibers","url":"https://www.academia.edu/Documents/in/Carbon_Fibers"}],"urls":[{"id":25459344,"url":"https://api.elsevier.com/content/article/PII:S0360319913021009?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814503"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814503/Three_dimensional_modeling_of_water_transport_in_PEMFC"><img alt="Research paper thumbnail of Three-dimensional modeling of water transport in PEMFC" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814503/Three_dimensional_modeling_of_water_transport_in_PEMFC">Three-dimensional modeling of water transport in PEMFC</a></div><div class="wp-workCard_item"><span>International Journal of Hydrogen Energy</span><span>, 2013</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a P...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a PEMFC. In order to capture the effects of liquid water on the performance of the fuel cell, all regions are modeled from the anode to the cathode as having finite thickness. The geometry of the bipolar plate is modeled in detail to capture the effect of liquid water accumulation under the channel rib. This model takes into account the effect of temperature and inlet RH of both the anode and cathode. The three-dimensional model ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814503"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814503"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814503; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814503]").text(description); $(".js-view-count[data-work-id=89814503]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814503; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814503']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814503, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814503]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814503,"title":"Three-dimensional modeling of water transport in PEMFC","translated_title":"","metadata":{"abstract":"Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a PEMFC. In order to capture the effects of liquid water on the performance of the fuel cell, all regions are modeled from the anode to the cathode as having finite thickness. The geometry of the bipolar plate is modeled in detail to capture the effect of liquid water accumulation under the channel rib. This model takes into account the effect of temperature and inlet RH of both the anode and cathode. The three-dimensional model ...","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2013,"errors":{}},"publication_name":"International Journal of Hydrogen Energy"},"translated_abstract":"Abstract A three dimensional two phase flow model is proposed to study transport phenomena in a PEMFC. In order to capture the effects of liquid water on the performance of the fuel cell, all regions are modeled from the anode to the cathode as having finite thickness. The geometry of the bipolar plate is modeled in detail to capture the effect of liquid water accumulation under the channel rib. This model takes into account the effect of temperature and inlet RH of both the anode and cathode. The three-dimensional model ...","internal_url":"https://www.academia.edu/89814503/Three_dimensional_modeling_of_water_transport_in_PEMFC","translated_internal_url":"","created_at":"2022-11-02T12:34:14.707-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":44382641,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Three_dimensional_modeling_of_water_transport_in_PEMFC","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":44382641,"first_name":"Halouani","middle_initials":null,"last_name":"Kamel","page_name":"HalouaniKamel","domain_name":"uus","created_at":"2016-03-03T06:25:03.869-08:00","display_name":"Halouani Kamel","url":"https://uus.academia.edu/HalouaniKamel"},"attachments":[],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":512,"name":"Mechanics","url":"https://www.academia.edu/Documents/in/Mechanics"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":2024,"name":"Mass Transfer","url":"https://www.academia.edu/Documents/in/Mass_Transfer"},{"id":104345,"name":"Hydrogen Energy","url":"https://www.academia.edu/Documents/in/Hydrogen_Energy"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":568612,"name":"Finite Volume Method","url":"https://www.academia.edu/Documents/in/Finite_Volume_Method"},{"id":891610,"name":"Proton Exchange Membrane Fuel Cell","url":"https://www.academia.edu/Documents/in/Proton_Exchange_Membrane_Fuel_Cell"},{"id":1131650,"name":"Cathode","url":"https://www.academia.edu/Documents/in/Cathode"},{"id":1131651,"name":"Anode","url":"https://www.academia.edu/Documents/in/Anode"}],"urls":[{"id":25459343,"url":"https://api.elsevier.com/content/article/PII:S0360319912024627?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814501"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814501/Two_dimensional_modeling_of_electrochemical_and_transport_phenomena_in_the_porous_structures_of_a_PEMFC"><img alt="Research paper thumbnail of Two-dimensional modeling of electrochemical and transport phenomena in the porous structures of a PEMFC" class="work-thumbnail" src="https://attachments.academia-assets.com/93550638/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814501/Two_dimensional_modeling_of_electrochemical_and_transport_phenomena_in_the_porous_structures_of_a_PEMFC">Two-dimensional modeling of electrochemical and transport phenomena in the porous structures of a PEMFC</a></div><div class="wp-workCard_item"><span>International Journal of Hydrogen Energy</span><span>, 2009</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="ef0ebc201020d5fe7b442475e772f055" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550638,"asset_id":89814501,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550638/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814501"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814501"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814501; 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The catalyst layers and membrane are each considered as distinct regions with finite thickness and calculated properties such as permeability, local protonic conductivity, and local dissolved water diffusion. This finite thickness model enables to model accurately the protonic current in these regions with higher accuracy than using an infinitesimal interface. In addition, this model takes into account the effect of osmotic drag in the membrane and catalyst layers. General boundary conditions are implemented in a way taking into consideration any given species concentration at the fuel cell inlet, such as water vapor which is a very important parameter in determining the efficiency of fuel cells. 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href="https://www.academia.edu/89814500/Effect_of_optical_properties_on_oscillatory_hydromagnetic_double_diffusive_convection_within_semitransparent_fluid"><img alt="Research paper thumbnail of Effect of optical properties on oscillatory hydromagnetic double-diffusive convection within semitransparent fluid" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814500/Effect_of_optical_properties_on_oscillatory_hydromagnetic_double_diffusive_convection_within_semitransparent_fluid">Effect of optical properties on oscillatory hydromagnetic double-diffusive convection within semitransparent fluid</a></div><div class="wp-workCard_item"><span>International Journal of Heat and Mass Transfer</span><span>, 2006</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dim...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dimensional rectangular enclosure is studied numerically for fixed Prandtl, Rayleigh, and Lewis numbers, Pr=13.6, Ra=105, Le=2. Uniform temperatures and concentrations are imposed along the vertical walls while the horizontal walls are assumed to be adiabatic and impermeable to mass transfer. The influences of the optical thickness and scattering</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814500"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814500"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814500; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=89814500]").text(description); $(".js-view-count[data-work-id=89814500]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 89814500; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='89814500']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 89814500, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=89814500]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":89814500,"title":"Effect of optical properties on oscillatory hydromagnetic double-diffusive convection within semitransparent fluid","translated_title":"","metadata":{"abstract":"The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dimensional rectangular enclosure is studied numerically for fixed Prandtl, Rayleigh, and Lewis numbers, Pr=13.6, Ra=105, Le=2. Uniform temperatures and concentrations are imposed along the vertical walls while the horizontal walls are assumed to be adiabatic and impermeable to mass transfer. The influences of the optical thickness and scattering","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2006,"errors":{}},"publication_name":"International Journal of Heat and Mass Transfer"},"translated_abstract":"The effect of radiative heat transfer on the hydromagnetic double-diffusive convection in two-dimensional rectangular enclosure is studied numerically for fixed Prandtl, Rayleigh, and Lewis numbers, Pr=13.6, Ra=105, Le=2. Uniform temperatures and concentrations are imposed along the vertical walls while the horizontal walls are assumed to be adiabatic and impermeable to mass transfer. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="89814499"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/89814499/Effect_of_radiative_heat_transfer_on_the_three_dimensional_Boyancy_flow_in_cubic_enclosure_heated_from_the_side"><img alt="Research paper thumbnail of Effect of radiative heat transfer on the three-dimensional Boyancy flow in cubic enclosure heated from the side" class="work-thumbnail" src="https://attachments.academia-assets.com/93550672/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/89814499/Effect_of_radiative_heat_transfer_on_the_three_dimensional_Boyancy_flow_in_cubic_enclosure_heated_from_the_side">Effect of radiative heat transfer on the three-dimensional Boyancy flow in cubic enclosure heated from the side</a></div><div class="wp-workCard_item"><span>International Journal of Heat and Fluid Flow</span><span>, 2008</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="e987ddf539684155087f761bae710ba0" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":93550672,"asset_id":89814499,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/93550672/download_file?st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&st=MTczMjUxMzY4Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="89814499"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="89814499"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 89814499; 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The natural convection equations, using the Boussinesq approximation for the treatment of buoyancy term in the momentum equation, are expressed using the vorticity-stream function formulation. These equations and the radiative transfer equation are discretized, respectively, with the control volume finite difference method and the FTn finite volume method. The successive relaxation-iterating scheme is used to solve the resultant algebraic system equations. Results show that the structure of the main flow is considerably altered by of the conduction-radiation parameter. The inner spiraling flows are found very sensible in location and direction to the radiative heat transfer. However, the peripheral spiraling motion is qualitatively insensitive to these parameters. 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