{"id":4680,"date":"2023-05-25T09:22:28","date_gmt":"2023-05-25T07:22:28","guid":{"rendered":"https:\/\/gpt-dev.i3a.es\/?p=4680"},"modified":"2023-05-25T09:22:28","modified_gmt":"2023-05-25T07:22:28","slug":"maria-abian","status":"publish","type":"post","link":"https:\/\/gpt.i3a.es\/es\/maria-abian\/","title":{"rendered":"Mar\u00eda Abi\u00e1n"},"content":{"rendered":"<div id=\"pl-gb4680-69df1d8c5967d\"  class=\"panel-layout\" ><div id=\"pg-gb4680-69df1d8c5967d-0\"  class=\"panel-grid panel-has-style\" ><div class=\"siteorigin-panels-stretch panel-row-style panel-row-style-for-gb4680-69df1d8c5967d-0\" data-stretch-type=\"full-width-stretch\" ><div id=\"pgc-gb4680-69df1d8c5967d-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4680-69df1d8c5967d-0-0-0\" class=\"so-panel widget widget_sow-hero panel-first-child panel-last-child\" data-index=\"0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-hero so-widget-sow-hero-default-93415d0e2dbf-4680 so-widget-fittext-wrapper\"\n\t\t\t data-fit-text-compressor=\"0.85\"\n\t\t>\t\t\t\t<div class=\"sow-slider-base\" style=\"display: none\" tabindex=\"0\">\n\t\t\t\t\t<ul\n\t\t\t\t\tclass=\"sow-slider-images\"\n\t\t\t\t\tdata-settings=\"{&quot;pagination&quot;:true,&quot;speed&quot;:800,&quot;timeout&quot;:8000,&quot;paused&quot;:false,&quot;pause_on_hover&quot;:false,&quot;swipe&quot;:true,&quot;nav_always_show_desktop&quot;:&quot;&quot;,&quot;nav_always_show_mobile&quot;:&quot;&quot;,&quot;breakpoint&quot;:&quot;780px&quot;,&quot;unmute&quot;:false,&quot;anchor&quot;:null}\"\n\t\t\t\t\t\t\t\t\t\tdata-anchor-id=\"\"\n\t\t\t\t>\t\t<li class=\"sow-slider-image\" style=\"visibility: visible;;background-color: #1e73be\" >\n\t\t\t\t\t<div class=\"sow-slider-image-container\">\n\t\t\t<div class=\"sow-slider-image-wrapper\">\n\t\t\t\t<h3 style=\"text-align: center\"><a href=\"..\/team\/\">Investigadores<\/a><\/h3>\n<h1 style=\"text-align: center\"><strong>Mar\u00eda Abi\u00e1n<\/strong><\/h1>\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t<\/li>\n\t\t<\/ul>\t\t\t\t<ol class=\"sow-slider-pagination\">\n\t\t\t\t\t\t\t\t\t\t\t<li><a href=\"#\" data-goto=\"0\" aria-label=\"mostrar diapositiva 1\"><\/a><\/li>\n\t\t\t\t\t\t\t\t\t<\/ol>\n\n\t\t\t\t<div class=\"sow-slide-nav sow-slide-nav-next\">\n\t\t\t\t\t<a href=\"#\" data-goto=\"next\" aria-label=\"diapositiva siguiente\" data-action=\"next\">\n\t\t\t\t\t\t<em class=\"sow-sld-icon-thin-right\"><\/em>\n\t\t\t\t\t<\/a>\n\t\t\t\t<\/div>\n\n\t\t\t\t<div class=\"sow-slide-nav sow-slide-nav-prev\">\n\t\t\t\t\t<a href=\"#\" data-goto=\"previous\" aria-label=\"diapositiva anterior\" data-action=\"prev\">\n\t\t\t\t\t\t<em class=\"sow-sld-icon-thin-left\"><\/em>\n\t\t\t\t\t<\/a>\n\t\t\t\t<\/div>\n\t\t\t\t<\/div><\/div><\/div><\/div><\/div><\/div><\/div>\n\n<div id=\"pl-gb4680-69df1d8c5a106\"  class=\"panel-layout\" ><div id=\"pg-gb4680-69df1d8c5a106-0\"  class=\"panel-grid panel-no-style\" ><div 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class=\"sow-image-grid-image\">\n\t\t\t\t\t\t\t\t\t\t\t\t\t<a href=\"#\"\n\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\ttarget=\"_blank\" \t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\trel=\"noopener noreferrer\" \t\t\t\t\t\t\t\t\t\t\t>\n\t\t\t\t\t\t\t\t<img loading=\"lazy\" decoding=\"async\" width=\"37\" height=\"37\" src=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2020\/10\/website.png\" class=\"sow-image-grid-image_html\" alt=\"\" title=\"\" srcset=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2020\/10\/website.png 37w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2020\/10\/website-12x12.png 12w\" sizes=\"auto, (max-width: 37px) 100vw, 37px\" \/>\t\t\t\t\t\t\t\t\t<\/a>\n\t\t\t\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t\t<div class=\"sow-image-grid-image\">\n\t\t\t\t\t\t\t\t\t\t\t\t\t<a href=\"#\"\n\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\ttarget=\"_blank\" \t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t\trel=\"noopener noreferrer\" \t\t\t\t\t\t\t\t\t\t\t>\n\t\t\t\t\t\t\t\t<img loading=\"lazy\" decoding=\"async\" width=\"37\" height=\"37\" src=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2020\/10\/google-scholar.png\" class=\"sow-image-grid-image_html\" alt=\"\" title=\"\" srcset=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2020\/10\/google-scholar.png 37w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2020\/10\/google-scholar-12x12.png 12w\" sizes=\"auto, (max-width: 37px) 100vw, 37px\" \/>\t\t\t\t\t\t\t\t\t<\/a>\n\t\t\t\t\t\t\t\t\t\t\t<\/div>\n\t\t\t<\/div>\n<\/div><\/div><\/div><div id=\"panel-gb4680-69df1d8c5a106-0-1-1\" class=\"so-panel widget widget_sow-editor panel-last-child\" data-index=\"2\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-editor so-widget-sow-editor-base\"\n\t\t\t\n\t\t>\n<div class=\"siteorigin-widget-tinymce textwidget\">\n\t<blockquote>\n<p><strong>Tel\u00e9fono:<\/strong><\/p>\n<p><strong>Email:<\/strong> mabian@unizar.es<\/p>\n<p><strong>Address:<\/strong><\/p>\n<\/blockquote>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>\n\n<div id=\"pl-gb4680-69df1d8c5bc54\"  class=\"panel-layout\" ><div id=\"pg-gb4680-69df1d8c5bc54-0\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4680-69df1d8c5bc54-0\" ><div id=\"pgc-gb4680-69df1d8c5bc54-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4680-69df1d8c5bc54-0-0-0\" class=\"so-panel widget widget_sow-headline panel-first-child\" data-index=\"0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-headline so-widget-sow-headline-default-244eb6bef45a-4680\"\n\t\t\t\n\t\t><div class=\"sow-headline-container\">\n\t\t\t\t\t\t\t<h5 class=\"sow-headline\">\n\t\t\t\t\t\tSOBRE M\u00cd\t\t\t\t\t\t<\/h5>\n\t\t\t\t\t\t\t\t\t\t\t<div class=\"decoration\">\n\t\t\t\t\t\t<div class=\"decoration-inside\"><\/div>\n\t\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n<\/div><\/div><div id=\"panel-gb4680-69df1d8c5bc54-0-0-1\" class=\"so-panel widget widget_sow-editor panel-last-child\" data-index=\"1\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-editor so-widget-sow-editor-base\"\n\t\t\t\n\t\t>\n<div class=\"siteorigin-widget-tinymce textwidget\">\n\t<p>Associate professor at the Department of Chemical and Environmental Engineering of the University of Zaragoza (Spain), and researcher at the Thermochemical Process Group (GPT) of the Arag\u00f3n Institute of Engineering Research (I3A) of the University of Zaragoza (Spain).<\/p>\n<p>My research interests are in the fields of high temperature chemistry, chemical kinetic modeling, and formation and destruction of air pollutants (nitrogen oxides, sulfur compounds, \u2026) in energetic and industrial processes\/applications.<\/p>\n<p><strong>BIOGRAPHY<\/strong><\/p>\n<p>I graduated with a Master in Chemical Engineering from the University of Zaragoza (Spain) and in 2013 I got the degree of PhD in Chemical Engineering at the same university. As part of this investigation, in January-April 2011, I made a short term collaboration at the (Combustion Harmful Emission Control) CHEC group of the Technical University of Denmark. My research activities were related to hydrocarbon conversion in presence of different gaseous compounds that can be typically present in atmospheres with recycled flue gas (RFG), such as CO<sub>2<\/sub>, NO<sub>x\u00a0<\/sub>or SO<sub>2<\/sub>, to provide of the necessary experimental data both to get<br \/>\ninsight into the phenomena controlling the process and to improve and update a gas-phase combustion scheme in relation to different reaction environments.<\/p>\n<p>In 2015- 2017 I worked as a post-doctoral researcher at the Instituto de Carboqu\u00edmica (ICB) of the Spanish National Research Council (CSIC), with a research Grant funded by the Spanish Government.<br \/>\nDuring this time my research activities were focused on the development and optimization of oxygen carriers for the Chemical Looping Combustion process.\u00a0 In June-September 2016 I made a short term collaboration at the Department of Mechanical Engineering (DEM) of the Technical University of Lisbon (Portugal), to study the influence of the presence of metals on the combustion of biomass.<\/p>\n<p>Since 2017, I am a researcher at the Thermochemical Process Group (GPT) of the Arag\u00f3n Institute of Engineering Research (I3A) of the University of Zaragoza (Spain), performing fundamental studies related to the formation and destruction of main pollutants in thermo-chemical processes.<\/p>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div><div id=\"pg-gb4680-69df1d8c5bc54-1\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4680-69df1d8c5bc54-1\" ><div id=\"pgc-gb4680-69df1d8c5bc54-1-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4680-69df1d8c5bc54-1-0-0\" class=\"so-panel widget widget_sow-headline panel-first-child\" data-index=\"2\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-headline so-widget-sow-headline-default-244eb6bef45a-4680\"\n\t\t\t\n\t\t><div class=\"sow-headline-container\">\n\t\t\t\t\t\t\t<h5 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\"tgid=&amp;yr=&amp;auth=&amp;usr=&amp;type=article#tppubs\" >Art\u00edculos de revista<\/option><option value = \"tgid=&amp;yr=&amp;auth=&amp;usr=&amp;type=inproceedings#tppubs\" >Proceedings Articles<\/option><option value = \"tgid=&amp;yr=&amp;auth=&amp;usr=&amp;type=techreport#tppubs\" >Informes t\u00e9cnicos<\/option>\r\n                <\/select><\/div><input type=\"hidden\" name=\"trp-form-language\" value=\"es\"\/><\/form><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">30 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 6 <a href=\"https:\/\/gpt.i3a.es\/es\/maria-abian\/?limit=2&amp;tgid=&amp;yr=&amp;type=&amp;usr=&amp;auth=&amp;tsr=#tppubs\" title=\"p\u00e1gina siguiente\" class=\"page-numbers button\">&rsaquo;<\/a> <a href=\"https:\/\/gpt.i3a.es\/es\/maria-abian\/?limit=6&amp;tgid=&amp;yr=&amp;type=&amp;usr=&amp;auth=&amp;tsr=#tppubs\" title=\"\u00faltima p\u00e1gina\" class=\"page-numbers button\">&raquo;<\/a> <\/div><\/div><div class=\"teachpress_publication_list\"><h3 class=\"tp_h3\" id=\"tp_h3_2023\">2023<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Alzueta, Mar\u00eda U;  Abi\u00e1n, Mar\u00eda;  Elvira, I.;  Mercader, V\u00edctor D;  Sieso, L.<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('513','tp_links')\" style=\"cursor:pointer;\">Unraveling the NO reduction mechanisms occurring during the combustion of NH3\/CH4 mixtures<\/a> <span class=\"tp_pub_type tp_  article\">Art\u00edculo de revista<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_in\">En: <\/span><span class=\"tp_pub_additional_journal\">Combustion and Flame, <\/span><span class=\"tp_pub_additional_volume\">vol. 257, <\/span><span class=\"tp_pub_additional_pages\">pp. 112531, <\/span><span class=\"tp_pub_additional_year\">2023<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 0010-2180<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_513\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('513','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_513\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('513','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_513\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('513','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_513\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{alzueta_unraveling_2023,<br \/>\r\ntitle = {Unraveling the NO reduction mechanisms occurring during the combustion of NH3\/CH4 mixtures},<br \/>\r\nauthor = {Mar\u00eda U Alzueta and Mar\u00eda Abi\u00e1n and I. Elvira and V\u00edctor D Mercader and L. Sieso},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0010218022005405},<br \/>\r\ndoi = {10.1016\/j.combustflame.2022.112531},<br \/>\r\nissn = {0010-2180},<br \/>\r\nyear  = {2023},<br \/>\r\ndate = {2023-11-01},<br \/>\r\nurldate = {2023-11-01},<br \/>\r\njournal = {Combustion and Flame},<br \/>\r\nvolume = {257},<br \/>\r\npages = {112531},<br \/>\r\nseries = {James A. Miller Special Commemorative Issue},<br \/>\r\nabstract = {The interaction between NH3, CH4 and NO under different conditions of interest for combustion applications is analyzed, from both experimental and kinetic modeling points of view. Reduction of NO by reburn and by SNCR (selective non-catalytic reduction) strategies is evaluated, through an extense systematic study of the influence of the main variables of interest for NO reduction, by means of laboratory flow-reactor experiments at atmospheric pressure. Variables analyzed include: temperature in the 700 to 1500\u00a0K range, air stoichiometry from fuel-rich (\u03bb\u00a0=\u00a00.31) to fuel-lean conditions (\u03bb\u00a0=\u00a02.21), NH3\/CH4 ratio in the 0.4 to 10.78 range, NH3\/NO ratio in the 0.49 to 2.60 range the, and CH4\/NO ratio in the 0.37 to 1.98 range, dilution level, and bath gas by using nitrogen and argon, the latter to allow the precise determination of nitrogen balances. Results are interpreted using a literature reaction mechanism, together with reaction pathway analysis tools, and the main findings are discussed. Results indicate that ammonia promotes the conversion of methane, while methane inhibits the conversion of ammonia, due to the competition for radicals of both components in the mixture. The interaction of ammonia and methane implies that the reduction of NO by NH3\/CH4 mixtures is comparatively lower than the reduction obtained by NH3 and CH4 independently. Implications for practical applications of the reduction of NO by the studied mixtures are discussed.},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {article}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('513','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_513\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The interaction between NH3, CH4 and NO under different conditions of interest for combustion applications is analyzed, from both experimental and kinetic modeling points of view. Reduction of NO by reburn and by SNCR (selective non-catalytic reduction) strategies is evaluated, through an extense systematic study of the influence of the main variables of interest for NO reduction, by means of laboratory flow-reactor experiments at atmospheric pressure. Variables analyzed include: temperature in the 700 to 1500\u00a0K range, air stoichiometry from fuel-rich (\u03bb\u00a0=\u00a00.31) to fuel-lean conditions (\u03bb\u00a0=\u00a02.21), NH3\/CH4 ratio in the 0.4 to 10.78 range, NH3\/NO ratio in the 0.49 to 2.60 range the, and CH4\/NO ratio in the 0.37 to 1.98 range, dilution level, and bath gas by using nitrogen and argon, the latter to allow the precise determination of nitrogen balances. Results are interpreted using a literature reaction mechanism, together with reaction pathway analysis tools, and the main findings are discussed. Results indicate that ammonia promotes the conversion of methane, while methane inhibits the conversion of ammonia, due to the competition for radicals of both components in the mixture. The interaction of ammonia and methane implies that the reduction of NO by NH3\/CH4 mixtures is comparatively lower than the reduction obtained by NH3 and CH4 independently. Implications for practical applications of the reduction of NO by the studied mixtures are discussed.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('513','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_513\" style=\"display:none;\"><div class=\"tp_links_entry\"><ul class=\"tp_pub_list\"><li><i class=\"fas fa-globe\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0010218022005405\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0010218022005405\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0010218022005405<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/j.combustflame.2022.112531\" title=\"DOI de seguimiento:10.1016\/j.combustflame.2022.112531\" target=\"_blank\">doi:10.1016\/j.combustflame.2022.112531<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('513','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><h3 class=\"tp_h3\" id=\"tp_h3_2021\">2021<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Abi\u00e1n, Mar\u00eda;  Ben\u00e9s, Mario;  Go\u00f1i, A;  Mu\u00f1oz, B;  Alzueta, Mar\u00eda U<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('164','tp_links')\" style=\"cursor:pointer;\">Study of the oxidation of ammonia in a flow reactor. Experiments and kinetic modeling simulation<\/a> <span class=\"tp_pub_type tp_  article\">Art\u00edculo de revista<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_in\">En: <\/span><span class=\"tp_pub_additional_journal\">Fuel, <\/span><span class=\"tp_pub_additional_volume\">vol. 300, <\/span><span class=\"tp_pub_additional_pages\">pp. 120979, <\/span><span class=\"tp_pub_additional_year\">2021<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 0016-2361<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_164\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('164','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_164\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('164','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_164\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('164','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_164\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Abian2021,<br \/>\r\ntitle = {Study of the oxidation of ammonia in a flow reactor. Experiments and kinetic modeling simulation},<br \/>\r\nauthor = {Mar\u00eda Abi\u00e1n and Mario Ben\u00e9s and A Go\u00f1i and B Mu\u00f1oz and Mar\u00eda U Alzueta},<br \/>\r\ndoi = {10.1016\/J.FUEL.2021.120979},<br \/>\r\nissn = {0016-2361},<br \/>\r\nyear  = {2021},<br \/>\r\ndate = {2021-09-01},<br \/>\r\njournal = {Fuel},<br \/>\r\nvolume = {300},<br \/>\r\npages = {120979},<br \/>\r\npublisher = {Elsevier},<br \/>\r\nabstract = {The present work is focused on the analysis of the ammonia oxidation process and the formation of main nitrogen oxides (NO, NO2 and N2O) over a wide range of temperatures and O2 reaction environments. Experiments are performed at atmospheric pressure in a laboratory quartz tubular flow reactor, covering the temperature range of 875 to 1450 K and for different air excess ratios (from pyrolysis to very oxidizing conditions). The experimental results are simulated and interpreted in terms of a detailed chemical-kinetic mechanism. Reaction path and sensitivity analyses are used to delineate the NH3 oxidation scheme.},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {article}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('164','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_164\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The present work is focused on the analysis of the ammonia oxidation process and the formation of main nitrogen oxides (NO, NO2 and N2O) over a wide range of temperatures and O2 reaction environments. Experiments are performed at atmospheric pressure in a laboratory quartz tubular flow reactor, covering the temperature range of 875 to 1450 K and for different air excess ratios (from pyrolysis to very oxidizing conditions). The experimental results are simulated and interpreted in terms of a detailed chemical-kinetic mechanism. Reaction path and sensitivity analyses are used to delineate the NH3 oxidation scheme.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('164','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_164\" style=\"display:none;\"><div class=\"tp_links_entry\"><ul class=\"tp_pub_list\"><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/J.FUEL.2021.120979\" title=\"DOI de seguimiento:10.1016\/J.FUEL.2021.120979\" target=\"_blank\">doi:10.1016\/J.FUEL.2021.120979<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('164','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Ben\u00e9s, Mario;  Pozo, Guillermo;  Abi\u00e1n, Mar\u00eda;  Millera, \u00c1ngela;  Bilbao, Rafael;  Alzueta, Mar\u00eda U<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('179','tp_links')\" style=\"cursor:pointer;\">Experimental Study of the Pyrolysis of NH3under Flow Reactor Conditions<\/a> <span class=\"tp_pub_type tp_  article\">Art\u00edculo de revista<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_in\">En: <\/span><span class=\"tp_pub_additional_journal\">Energy and Fuels, <\/span><span class=\"tp_pub_additional_year\">2021<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 15205029<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_179\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('179','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_179\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('179','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_179\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('179','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_179\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Benes2021,<br \/>\r\ntitle = {Experimental Study of the Pyrolysis of NH3under Flow Reactor Conditions},<br \/>\r\nauthor = {Mario Ben\u00e9s and Guillermo Pozo and Mar\u00eda Abi\u00e1n and \u00c1ngela Millera and Rafael Bilbao and Mar\u00eda U Alzueta},<br \/>\r\nurl = {https:\/\/dx.doi.org\/10.1021\/acs.energyfuels.0c03387},<br \/>\r\ndoi = {10.1021\/acs.energyfuels.0c03387},<br \/>\r\nissn = {15205029},<br \/>\r\nyear  = {2021},<br \/>\r\ndate = {2021-01-01},<br \/>\r\njournal = {Energy and Fuels},<br \/>\r\npublisher = {American Chemical Society},<br \/>\r\nabstract = {The possibility of using ammonia (NH3), as a fuel and as an energy carrier with low pollutant emissions, can contribute to the transition to a low-carbon economy. To use ammonia as fuel, knowledge about the NH3 conversion is desired. In particular, the conversion of ammonia under pyrolysis conditions could be determinant in the description of its combustion mechanism. In this work, pyrolysis experiments of ammonia have been performed in both a quartz tubular flow reactor (900-1500 K) and a non-porous alumina tubular flow reactor (900-1800 K) using Ar or N2 as bath gas. An experimental study of the influence of the reactor material (quartz or alumina), the bulk gas (N2 or Ar), the ammonia inlet concentration (1000 and 10a 000 ppm), and the gas residence time [2060\/T (K)-8239\/T (K) s] on the pyrolysis process has been performed. After the reaction, the resulting compounds (NH3, H2, and N2) are analyzed in a gas chromatograph\/thermal conductivity detector chromatograph and an infrared continuous analyzer. Results show that H2 and N2 are the main products of the thermal decomposition of ammonia. Under the conditions of the present work, differences between working in a quartz or non-porous alumina reactor are not significant under pyrolysis conditions for temperatures lower than 1400 K. Neither the bath gas nor the ammonia inlet concentration influence the ammonia conversion values. For a given temperature and under all conditions studied, conversion of ammonia increases with an increasing gas residence time, which results into a narrower temperature window for NH3 conversion.},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {article}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('179','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_179\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The possibility of using ammonia (NH3), as a fuel and as an energy carrier with low pollutant emissions, can contribute to the transition to a low-carbon economy. To use ammonia as fuel, knowledge about the NH3 conversion is desired. In particular, the conversion of ammonia under pyrolysis conditions could be determinant in the description of its combustion mechanism. In this work, pyrolysis experiments of ammonia have been performed in both a quartz tubular flow reactor (900-1500 K) and a non-porous alumina tubular flow reactor (900-1800 K) using Ar or N2 as bath gas. An experimental study of the influence of the reactor material (quartz or alumina), the bulk gas (N2 or Ar), the ammonia inlet concentration (1000 and 10a 000 ppm), and the gas residence time [2060\/T (K)-8239\/T (K) s] on the pyrolysis process has been performed. After the reaction, the resulting compounds (NH3, H2, and N2) are analyzed in a gas chromatograph\/thermal conductivity detector chromatograph and an infrared continuous analyzer. Results show that H2 and N2 are the main products of the thermal decomposition of ammonia. Under the conditions of the present work, differences between working in a quartz or non-porous alumina reactor are not significant under pyrolysis conditions for temperatures lower than 1400 K. Neither the bath gas nor the ammonia inlet concentration influence the ammonia conversion values. For a given temperature and under all conditions studied, conversion of ammonia increases with an increasing gas residence time, which results into a narrower temperature window for NH3 conversion.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('179','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_179\" style=\"display:none;\"><div class=\"tp_links_entry\"><ul class=\"tp_pub_list\"><li><i class=\"fas fa-globe\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1021\/acs.energyfuels.0c03387\" title=\"https:\/\/dx.doi.org\/10.1021\/acs.energyfuels.0c03387\" target=\"_blank\">https:\/\/dx.doi.org\/10.1021\/acs.energyfuels.0c03387<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('179','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><h3 class=\"tp_h3\" id=\"tp_h3_2020\">2020<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Colom-D\u00edaz, Juan Manuel;  Leci\u00f1ena, M;  Pel\u00e1ez, A;  Abi\u00e1n, Mar\u00eda;  Millera, \u00c1ngela;  Bilbao, Rafael;  Alzueta, Mar\u00eda U<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('203','tp_links')\" style=\"cursor:pointer;\">Study of the conversion of CH4\/H2S mixtures at different pressures<\/a> <span class=\"tp_pub_type tp_  article\">Art\u00edculo de revista<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_in\">En: <\/span><span class=\"tp_pub_additional_journal\">Fuel, <\/span><span class=\"tp_pub_additional_volume\">vol. 262, <\/span><span class=\"tp_pub_additional_pages\">pp. 116484, <\/span><span class=\"tp_pub_additional_year\">2020<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 00162361<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_203\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('203','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_203\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('203','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_203\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('203','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_203\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Colom-Diaz2020,<br \/>\r\ntitle = {Study of the conversion of CH4\/H2S mixtures at different pressures},<br \/>\r\nauthor = {Juan Manuel Colom-D\u00edaz and M Leci\u00f1ena and A Pel\u00e1ez and Mar\u00eda Abi\u00e1n and \u00c1ngela Millera and Rafael Bilbao and Mar\u00eda U Alzueta},<br \/>\r\ndoi = {10.1016\/j.fuel.2019.116484},<br \/>\r\nissn = {00162361},<br \/>\r\nyear  = {2020},<br \/>\r\ndate = {2020-02-01},<br \/>\r\njournal = {Fuel},<br \/>\r\nvolume = {262},<br \/>\r\npages = {116484},<br \/>\r\npublisher = {Elsevier Ltd},<br \/>\r\nabstract = {Due to the different scenarios where sour gas is present, its composition can be different and, therefore, it can be exploited through different processes, being combustion one of them. In this context, this work deals with the oxidation of CH4 and H2S at different pressures and under a wide variety of conditions. The oxidation has been evaluated experimentally in two different flow reactor set-ups, one working at atmospheric pressure and another one operating from atmospheric to high pressures (40 bar). Different CH4\/H2S mixtures have been tested, together with different oxygen concentrations and in the temperature range of 500\u20131400 K. The experimental results obtained show that the oxidation of the CH4\/H2S mixtures is shifted to lower temperatures as pressure increases, obtaining the same trends at atmospheric pressure in both experimental set-ups. H2S oxidation occurs prior to CH4 oxidation at all conditions, providing radicals to the system that promote CH4 oxidation to lower temperatures (compared to neat CH4 oxidation). This effect is more relevant as pressure increases. H2S oxidation is inhibited by CH4 at atmospheric pressure, being more noticeable when the CH4\/H2S ratio is higher. At higher pressures, the H2S conversion occurs similarly in the absence or presence of CH4. The experimental results have been modeled with an updated kinetic model from previous works from the literature, which, in general, matches well the experimental trends, while some discrepancies between experimental and modeling results at atmospheric pressure and 40 bar are found in the conversion of H2S and CH4.},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {article}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('203','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_203\" style=\"display:none;\"><div class=\"tp_abstract_entry\">Due to the different scenarios where sour gas is present, its composition can be different and, therefore, it can be exploited through different processes, being combustion one of them. In this context, this work deals with the oxidation of CH4 and H2S at different pressures and under a wide variety of conditions. The oxidation has been evaluated experimentally in two different flow reactor set-ups, one working at atmospheric pressure and another one operating from atmospheric to high pressures (40 bar). Different CH4\/H2S mixtures have been tested, together with different oxygen concentrations and in the temperature range of 500\u20131400 K. The experimental results obtained show that the oxidation of the CH4\/H2S mixtures is shifted to lower temperatures as pressure increases, obtaining the same trends at atmospheric pressure in both experimental set-ups. H2S oxidation occurs prior to CH4 oxidation at all conditions, providing radicals to the system that promote CH4 oxidation to lower temperatures (compared to neat CH4 oxidation). This effect is more relevant as pressure increases. H2S oxidation is inhibited by CH4 at atmospheric pressure, being more noticeable when the CH4\/H2S ratio is higher. At higher pressures, the H2S conversion occurs similarly in the absence or presence of CH4. The experimental results have been modeled with an updated kinetic model from previous works from the literature, which, in general, matches well the experimental trends, while some discrepancies between experimental and modeling results at atmospheric pressure and 40 bar are found in the conversion of H2S and CH4.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('203','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_203\" style=\"display:none;\"><div class=\"tp_links_entry\"><ul class=\"tp_pub_list\"><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/j.fuel.2019.116484\" title=\"DOI de seguimiento:10.1016\/j.fuel.2019.116484\" target=\"_blank\">doi:10.1016\/j.fuel.2019.116484<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('203','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><h3 class=\"tp_h3\" id=\"tp_h3_2019\">2019<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Colom-D\u00edaz, Juan Manuel;  Abi\u00e1n, Mar\u00eda;  Millera, \u00c1ngela;  Bilbao, Rafael;  Alzueta, Mar\u00eda U<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('208','tp_links')\" style=\"cursor:pointer;\">Influence of pressure on H2S oxidation. Experiments and kinetic modeling<\/a> <span class=\"tp_pub_type tp_  article\">Art\u00edculo de revista<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_in\">En: <\/span><span class=\"tp_pub_additional_journal\">Fuel, <\/span><span class=\"tp_pub_additional_volume\">vol. 258, <\/span><span class=\"tp_pub_additional_pages\">pp. 116145, <\/span><span class=\"tp_pub_additional_year\">2019<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 00162361<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_208\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('208','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_208\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('208','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_208\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('208','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_208\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Colom-Diaz2019b,<br \/>\r\ntitle = {Influence of pressure on H2S oxidation. Experiments and kinetic modeling},<br \/>\r\nauthor = {Juan Manuel Colom-D\u00edaz and Mar\u00eda Abi\u00e1n and \u00c1ngela Millera and Rafael Bilbao and Mar\u00eda U Alzueta},<br \/>\r\ndoi = {10.1016\/j.fuel.2019.116145},<br \/>\r\nissn = {00162361},<br \/>\r\nyear  = {2019},<br \/>\r\ndate = {2019-12-01},<br \/>\r\njournal = {Fuel},<br \/>\r\nvolume = {258},<br \/>\r\npages = {116145},<br \/>\r\npublisher = {Elsevier Ltd},<br \/>\r\nabstract = {The oxidation of H2S at different manometric pressures (0.6\u201340 bar), in the temperature range of 500\u20131000 K and under slightly oxidizing conditions ($\u0142ambda$ = 2), has been studied. Experiments have been performed in a quartz tubular flow reactor. The results have shown that H2S conversion shifts to lower temperatures as the pressure increases. The kinetic model used in this work is based on a previous one proposed by the authors to describe H2S oxidation at atmospheric pressure, which has been updated with a H2\/O2 reaction subset for high pressures. Model results match fairly well the experimental ones both from the present work and from the literature. The reaction pathways of H2S oxidation analyzed are similar to the ones at atmospheric pressure. The differences are found in the radicals that are involved in the oxidation process at the different pressures. For a given temperature it is shown that, under the operating conditions of this work, pressure will have a major role than the gas residence time in the oxidation rate.},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {article}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('208','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_208\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The oxidation of H2S at different manometric pressures (0.6\u201340 bar), in the temperature range of 500\u20131000 K and under slightly oxidizing conditions ($\u0142ambda$ = 2), has been studied. Experiments have been performed in a quartz tubular flow reactor. The results have shown that H2S conversion shifts to lower temperatures as the pressure increases. The kinetic model used in this work is based on a previous one proposed by the authors to describe H2S oxidation at atmospheric pressure, which has been updated with a H2\/O2 reaction subset for high pressures. Model results match fairly well the experimental ones both from the present work and from the literature. The reaction pathways of H2S oxidation analyzed are similar to the ones at atmospheric pressure. The differences are found in the radicals that are involved in the oxidation process at the different pressures. For a given temperature it is shown that, under the operating conditions of this work, pressure will have a major role than the gas residence time in the oxidation rate.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('208','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_208\" style=\"display:none;\"><div class=\"tp_links_entry\"><ul class=\"tp_pub_list\"><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/j.fuel.2019.116145\" title=\"DOI de seguimiento:10.1016\/j.fuel.2019.116145\" target=\"_blank\">doi:10.1016\/j.fuel.2019.116145<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('208','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><\/div><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">30 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 6 <a href=\"https:\/\/gpt.i3a.es\/es\/maria-abian\/?limit=2&amp;tgid=&amp;yr=&amp;type=&amp;usr=&amp;auth=&amp;tsr=#tppubs\" title=\"p\u00e1gina siguiente\" class=\"page-numbers button\">&rsaquo;<\/a> <a href=\"https:\/\/gpt.i3a.es\/es\/maria-abian\/?limit=6&amp;tgid=&amp;yr=&amp;type=&amp;usr=&amp;auth=&amp;tsr=#tppubs\" title=\"\u00faltima p\u00e1gina\" class=\"page-numbers button\">&raquo;<\/a> <\/div><\/div><\/div>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div><\/div>\n\n\n<p><\/p>","protected":false},"excerpt":{"rendered":"","protected":false},"author":1,"featured_media":4681,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"footnotes":""},"categories":[238,239],"tags":[],"class_list":["post-4680","post","type-post","status-publish","format-standard","has-post-thumbnail","hentry","category-permanent-members","category-team"],"_links":{"self":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4680","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/comments?post=4680"}],"version-history":[{"count":1,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4680\/revisions"}],"predecessor-version":[{"id":4682,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4680\/revisions\/4682"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media\/4681"}],"wp:attachment":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media?parent=4680"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/categories?post=4680"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/tags?post=4680"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}