{"id":3807,"date":"2023-09-01T15:09:00","date_gmt":"2023-09-01T13:09:00","guid":{"rendered":"https:\/\/creg-dev.i3a.es\/?p=3807"},"modified":"2025-12-10T18:05:31","modified_gmt":"2025-12-10T16:05:31","slug":"simona-renda","status":"publish","type":"post","link":"https:\/\/creg.i3a.es\/es\/simona-renda\/","title":{"rendered":"Simona Renda"},"content":{"rendered":"<div id=\"pl-gb3807-6a6676c51816f\"  class=\"panel-layout wp-block-siteorigin-panels-layout-block\" ><div id=\"pg-gb3807-6a6676c51816f-0\"  class=\"panel-grid panel-has-style\" ><div class=\"siteorigin-panels-stretch panel-row-style panel-row-style-for-gb3807-6a6676c51816f-0\" data-stretch-type=\"full-width-stretch\" ><div id=\"pgc-gb3807-6a6676c51816f-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb3807-6a6676c51816f-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-3807 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=\"..\/people\/\">Investigadores<\/a><\/h3>\n<h1 style=\"text-align: center\"><strong>Simona Renda<br \/>\n<\/strong><\/h1>\n\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-gb3807-6a6676c518a1d\"  class=\"panel-layout wp-block-siteorigin-panels-layout-block\" ><div id=\"pg-gb3807-6a6676c518a1d-0\"  class=\"panel-grid panel-no-style\" ><div id=\"pgc-gb3807-6a6676c518a1d-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb3807-6a6676c518a1d-0-0-0\" class=\"so-panel widget widget_sow-image panel-first-child panel-last-child\" data-index=\"0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-image so-widget-sow-image-default-8b5b6f678277-3807\"\n\t\t\t\n\t\t>\n<div class=\"sow-image-container\">\n\t\t<img \n\tsrc=\"https:\/\/creg.i3a.es\/wp-content\/uploads\/2023\/09\/Profile-photo-225x300.jpg\" width=\"225\" height=\"300\" srcset=\"https:\/\/creg.i3a.es\/wp-content\/uploads\/2023\/09\/Profile-photo-225x300.jpg 225w, https:\/\/creg.i3a.es\/wp-content\/uploads\/2023\/09\/Profile-photo-9x12.jpg 9w, https:\/\/creg.i3a.es\/wp-content\/uploads\/2023\/09\/Profile-photo.jpg 618w\" sizes=\"(max-width: 225px) 100vw, 225px\" title=\"Progetto senza titolo &#8211; 3\" alt=\"\" \t\tclass=\"so-widget-image\"\/>\n\t<\/div>\n\n<\/div><\/div><\/div><div id=\"pgc-gb3807-6a6676c518a1d-0-1\"  class=\"panel-grid-cell\" ><div id=\"panel-gb3807-6a6676c518a1d-0-1-0\" class=\"so-panel widget widget_sow-image-grid panel-first-child\" data-index=\"1\" ><div class=\"panel-widget-style panel-widget-style-for-gb3807-6a6676c518a1d-0-1-0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-image-grid so-widget-sow-image-grid-default-5ff4073610f5-3807\"\n\t\t\t\n\t\t>\t<div\n\t\tclass=\"sow-image-grid-wrapper\"\n\t\t\t\t\t>\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=\"https:\/\/www.linkedin.com\/in\/simonarenda\/\"\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:\/\/creg.i3a.es\/wp-content\/uploads\/2020\/10\/linkedin.png\" class=\"sow-image-grid-image_html\" alt=\"\" title=\"\" srcset=\"https:\/\/creg.i3a.es\/wp-content\/uploads\/2020\/10\/linkedin.png 37w, https:\/\/creg.i3a.es\/wp-content\/uploads\/2020\/10\/linkedin-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=\"https:\/\/scholar.google.com\/citations?user=SxXObLQAAAAJ&#038;hl=it\"\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:\/\/creg.i3a.es\/wp-content\/uploads\/2020\/10\/google-scholar.png\" class=\"sow-image-grid-image_html\" alt=\"\" title=\"\" srcset=\"https:\/\/creg.i3a.es\/wp-content\/uploads\/2020\/10\/google-scholar.png 37w, https:\/\/creg.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-gb3807-6a6676c518a1d-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> +34 876 555 429<\/p>\n<p><strong>Email:<\/strong> <a href=\"mailto:srenda@unizar.es\">srenda@unizar.es<\/a><\/p>\n<p><strong>Direcci\u00f3n:<\/strong> Despacho 3.1.11 c\/Mariano Esquillor SN Edificio I+D+i, I3A, 50018, Zaragoza (Spain)<\/p>\n<p><strong>Sideral:<\/strong> <a href=\"https:\/\/janovas.unizar.es\/sideral\/CV\/simona-renda\" target=\"_blank\" rel=\"noopener\">Ver el perfil (CV)<\/a><\/p>\n<\/blockquote>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>\n\n<div id=\"pl-gb3807-6a6676c51a072\"  class=\"panel-layout wp-block-siteorigin-panels-layout-block\" ><div id=\"pg-gb3807-6a6676c51a072-0\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb3807-6a6676c51a072-0\" ><div id=\"pgc-gb3807-6a6676c51a072-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb3807-6a6676c51a072-0-0-0\" 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-3807\"\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-gb3807-6a6676c51a072-0-0-1\" 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 style=\"text-align: justify;\">Simona Renda es investigadora postdoctoral Juan de la Cierva y forma parte del Grupo Consolidado de Cat\u00e1lisis y Tecnolog\u00eda de Reactores (CREG) de la Universidad de Zaragoza desde 2023, as\u00ed como del Instituto de Investigaci\u00f3n en Ingenier\u00eda de Arag\u00f3n (I3A) desde 2025. Es licenciada y m\u00e1ster en Ingenier\u00eda Qu\u00edmica y obtuvo el doctorado en Ingenier\u00eda Industrial \u2013 programa de Ingenier\u00eda Qu\u00edmica por la Universidad de Salerno (Italia), con menci\u00f3n de excelencia.<\/p>\n<p style=\"text-align: justify;\" class=\"translation-block\">Su investigaci\u00f3n se centra en la cat\u00e1lisis y la ingenier\u00eda de reactores para aplicaciones medioambientales. Cuenta con una trayectoria consolidada en catalizadores estructurados y valorizaci\u00f3n de CO<sub>2<\/sub> y otros procesos industriales como el tratamiento de gases Claus, la desalaci\u00f3n de agua en procesos de destilaci\u00f3n con membranas y la deshidrogenaci\u00f3n de propano. Tiene experiencia tanto experimental como en modelizaci\u00f3n CFD, y sus proyectos combinan investigaci\u00f3n acad\u00e9mica con colaboraciones industriales. Ha participado en m\u00e1s de 10 proyectos de investigaci\u00f3n y transferencia tecnol\u00f3gica, incluyendo dos proyectos europeos en el marco H2020. \nEn el CREG desarrolla actualmente dos l\u00edneas principales:<\/p>\n<ul>\n<li style=\"list-style-type: none;\">\n<ul>\n<li class=\"translation-block\">Hidrogenaci\u00f3n de CO<sub>2<\/sub> para la obtenci\u00f3n de e-combustibles (dimetil \u00e9ter y metanol)<\/li>\n<li>Reactores de lecho fluidizado con flujo continuo de adsorbente para la intensificaci\u00f3n de procesos con captura in situ<\/li>\n<\/ul>\n<\/li>\n<\/ul>\n<p style=\"text-align: justify;\">Su actividad investigadora incluye colaboraciones con m\u00e1s de diez partners industriales y extranjeros, y ha participado con contribuciones cient\u00edficas en m\u00e1s de quince congresos internacionales. Es revisora activa de varias revistas cient\u00edficas y miembro del comit\u00e9 de j\u00f3venes editores de la revista Catalysts. Tambi\u00e9n est\u00e1 comprometida con la formaci\u00f3n: ha dirigido 6 trabajos de fin de grado y 9 de fin de m\u00e1ster, ha coordinado 5 estancias internacionales y dirige actualmente una tesis doctoral sobre valorizaci\u00f3n de CO\u2082. Ha participado en actividades docentes en asignaturas de cat\u00e1lisis e ingenier\u00eda de reactores en la Universidad de Salerno y en la Universidad de Zaragoza.<\/p>\n<p style=\"text-align: justify;\">Simona es autora de m\u00e1s de 30 art\u00edculos cient\u00edficos en revistas indexadas, con m\u00e1s de 800 citas y un \u00edndice h de 13 (seg\u00fan Scopus, diciembre de 2025).<\/p>\n<p>Orcid: <a href=\"https:\/\/orcid.org\/0000-0002-5926-5252\">https:\/\/orcid.org\/0000-0002-5926-5252<\/a><\/p>\n<p>Scopus: <a href=\"https:\/\/www.scopus.com\/authid\/detail.uri?authorId=57212381756\">https:\/\/www.scopus.com\/authid\/detail.uri?authorId=57212381756<\/a><\/p>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div><div id=\"pg-gb3807-6a6676c51a072-1\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb3807-6a6676c51a072-1\" ><div id=\"pgc-gb3807-6a6676c51a072-1-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb3807-6a6676c51a072-1-0-0\" 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-3807\"\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\tPUBLICACIONES\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-gb3807-6a6676c51a072-1-0-1\" class=\"so-panel widget widget_sow-editor panel-last-child\" data-index=\"3\" ><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<div class=\"teachpress_pub_list\"><form name=\"tppublistform\" method=\"get\" action=\"\"><a name=\"tppubs\" id=\"tppubs\"><\/a><div class=\"teachpress_filter\"><select class=\"default\" name=\"yr\" id=\"yr\" tabindex=\"2\" onchange=\"teachpress_jumpMenu('parent',this, 'https:\/\/creg.i3a.es\/es\/simona-renda\/?')\">\r\n                   <option value=\"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=#tppubs\">Todos los a\u00f1os<\/option>\r\n                   <option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2026#tppubs\" >2026<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2025#tppubs\" >2025<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2024#tppubs\" >2024<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2023#tppubs\" >2023<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2022#tppubs\" >2022<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2021#tppubs\" >2021<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2020#tppubs\" >2020<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=2019#tppubs\" >2019<\/option><option value = 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\"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1996#tppubs\" >1996<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1995#tppubs\" >1995<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1994#tppubs\" >1994<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1993#tppubs\" >1993<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1992#tppubs\" >1992<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1991#tppubs\" >1991<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1988#tppubs\" >1988<\/option><option value = \"tgid=&amp;type=&amp;auth=&amp;usr=&amp;yr=1986#tppubs\" >1986<\/option>\r\n                <\/select><select class=\"default\" name=\"type\" id=\"type\" tabindex=\"3\" onchange=\"teachpress_jumpMenu('parent',this, 'https:\/\/creg.i3a.es\/es\/simona-renda\/?')\">\r\n                   <option value=\"tgid=&amp;yr=&amp;auth=&amp;usr=&amp;type=#tppubs\">Todas las tipolog\u00edas<\/option>\r\n                   <option value = \"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=book#tppubs\" >Libros<\/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=proceedings#tppubs\" >Actas de congresos<\/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\">39 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 8 <a href=\"https:\/\/creg.i3a.es\/es\/simona-renda\/?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:\/\/creg.i3a.es\/es\/simona-renda\/?limit=8&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_2026\">2026<\/h3><div class=\"tp_publication tp_publication_proceedings\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Gonz\u00e1lez Pizarro, Rodrigo;  Renda, Simona;  Lasobras Laguna, Javier;  Soler Herrero, Jaime;  Men\u00e9ndez Sastre, Miguel;  Herguido Huerta, Javier<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('3074','tp_links')\" style=\"cursor:pointer;\">Intensified Catalytic CO\u2082 Conversion into e-Fuels: A Study of Different Process Intensification Strategies<\/a> <span class=\"tp_pub_type tp_  proceedings\">Actas de congresos<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_volume\">vol. 14, <\/span><span class=\"tp_pub_additional_year\">2026<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_resource_link\"><a id=\"tp_links_sh_3074\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3074','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_3074\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3074','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_3074\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@proceedings{Gonz\u00e1lezPizarro_Renda_LasobrasLaguna_SolerHerrero_Men\u00e9ndezSastre_HerguidoHuerta_2026,<br \/>\r\ntitle = {Intensified Catalytic CO\u2082 Conversion into e-Fuels: A Study of Different Process Intensification Strategies},<br \/>\r\nauthor = {Gonz\u00e1lez Pizarro, Rodrigo and Renda, Simona and Lasobras Laguna, Javier and Soler Herrero, Jaime and Men\u00e9ndez Sastre, Miguel and Herguido Huerta, Javier},<br \/>\r\nurl = {https:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13351},<br \/>\r\ndoi = {10.26754\/jji-i3a.202613351},<br \/>\r\nyear  = {2026},<br \/>\r\ndate = {2026-07-01},<br \/>\r\nurldate = {2026-07-01},<br \/>\r\njournal = {Jornada de J\u00f3venes Investigadores del I3A},<br \/>\r\nvolume = {14},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {proceedings}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3074','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_3074\" 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:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13351\" title=\"https:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13351\" target=\"_blank\">https:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13351<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.26754\/jji-i3a.202613351\" title=\"DOI de seguimiento:10.26754\/jji-i3a.202613351\" target=\"_blank\">doi:10.26754\/jji-i3a.202613351<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3074','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><div class=\"tp_publication tp_publication_proceedings\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Flores Calvo, Diego;  Gonz\u00e1lez Pizarro, Rodrigo;  Soler Herrero, Jaime;  Men\u00e9ndez Sastre, Miguel;  Renda, Simona;  Lasobras Laguna, Javier;  Herguido Huerta, Javier<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('3076','tp_links')\" style=\"cursor:pointer;\">Optimizaci\u00f3n de las condiciones de operaci\u00f3n para la s\u00edntesis de metanol v\u00eda hidrogenaci\u00f3n catal\u00edtica de CO2 en reactor de lecho fijo<\/a> <span class=\"tp_pub_type tp_  proceedings\">Actas de congresos<\/span> <\/p><p class=\"tp_pub_additional\"><span class=\"tp_pub_additional_volume\">vol. 14, <\/span><span class=\"tp_pub_additional_year\">2026<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_resource_link\"><a id=\"tp_links_sh_3076\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3076','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_3076\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3076','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_3076\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@proceedings{FloresCalvo_Gonz\u00e1lezPizarro_SolerHerrero_Men\u00e9ndezSastre_Renda_LasobrasLaguna_HerguidoHuerta_2026,<br \/>\r\ntitle = {Optimizaci\u00f3n de las condiciones de operaci\u00f3n para la s\u00edntesis de metanol v\u00eda hidrogenaci\u00f3n catal\u00edtica de CO2 en reactor de lecho fijo},<br \/>\r\nauthor = {Flores Calvo, Diego and Gonz\u00e1lez Pizarro, Rodrigo and Soler Herrero, Jaime and Men\u00e9ndez Sastre, Miguel and Renda, Simona and Lasobras Laguna, Javier and Herguido Huerta, Javier},<br \/>\r\nurl = {https:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13387},<br \/>\r\ndoi = {10.26754\/jji-i3a.202613387},<br \/>\r\nyear  = {2026},<br \/>\r\ndate = {2026-07-01},<br \/>\r\nurldate = {2026-07-01},<br \/>\r\njournal = {Jornada de J\u00f3venes Investigadores del I3A},<br \/>\r\nvolume = {14},<br \/>\r\nkeywords = {},<br \/>\r\npubstate = {published},<br \/>\r\ntppubtype = {proceedings}<br \/>\r\n}<br \/>\r\n<\/pre><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3076','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_3076\" 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:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13387\" title=\"https:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13387\" target=\"_blank\">https:\/\/papiro.unizar.es\/ojs\/index.php\/jji3a\/article\/view\/13387<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.26754\/jji-i3a.202613387\" title=\"DOI de seguimiento:10.26754\/jji-i3a.202613387\" target=\"_blank\">doi:10.26754\/jji-i3a.202613387<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3076','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\"> Gonz\u00e1lez-Pizarro, R.;  Calero-Berrocal, R.;  Lasobras, J.;  Renda, S.;  Rodr\u00edguez-Pardo, M. R.;  Soler, J.;  Men\u00e9ndez, M.;  Herguido, J.<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('3064','tp_links')\" style=\"cursor:pointer;\">Tuning e-fuel selectivity in sorption-enhanced CO2 hydrogenation over In2O3\/ZrO2: The effect of LTA and FAU zeolites<\/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. 406, <\/span><span class=\"tp_pub_additional_pages\">pp. 136974, <\/span><span class=\"tp_pub_additional_year\">2026<\/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_3064\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3064','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_3064\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3064','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_3064\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3064','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_3064\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{GONZALEZPIZARRO2026136974,<br \/>\r\ntitle = {Tuning e-fuel selectivity in sorption-enhanced CO2 hydrogenation over In2O3\/ZrO2: The effect of LTA and FAU zeolites},<br \/>\r\nauthor = {R. Gonz\u00e1lez-Pizarro and R. Calero-Berrocal and J. Lasobras and S. Renda and M. R. Rodr\u00edguez-Pardo and J. Soler and M. Men\u00e9ndez and J. Herguido},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236125026997},<br \/>\r\ndoi = {https:\/\/doi.org\/10.1016\/j.fuel.2025.136974},<br \/>\r\nissn = {0016-2361},<br \/>\r\nyear  = {2026},<br \/>\r\ndate = {2026-01-01},<br \/>\r\njournal = {Fuel},<br \/>\r\nvolume = {406},<br \/>\r\npages = {136974},<br \/>\r\nabstract = {The e-fuels synthesis via CO2 hydrogenation and the Sorption Enhanced Reaction technology are captivating strategies for CO2 utilization and the integration of renewable energy sources. This study focuses on enhancing the conversion of CO2 over an In2O3\/ZrO2 catalyst by incorporating LTA zeolites (3A and 4A) and a FAU zeolite (13X). Key operational parameters, such as temperature (T), Gas Hour Space Velocity (GHSV), type of zeolite, and Zeolite: Catalyst mass ratio (Z\/C), were systematically varied. LTA zeolites (3A and 4A) provided the highest CO2 conversions. The introduction of a water-adsorbing solid into the reactor significantly altered the products yield and selectivity. While the selectivity towards CH4, CH3OH, and C2H6O appeared to lay on the type of zeolite, the selectivity towards CO remained unaffected. Zeolite 3A demonstrated the greatest enhancement in selectivity towards CH4 and CH3OH, whereas the synthesis of C2H6O was favored by zeolites 4A and 13X. The Zeolite:Catalyst mass ratio also played a crucial role in process performance, influencing both CO2 conversion and product selectivity. Increasing this ratio improved CO2 conversion and reduced CO selectivity under all operating conditions, while CH4 selectivity increased. However, the selectivity toward CH3OH and C2H6O exhibited an anomalous and complementary behavior. While a maximum was observed for DME, a minimum was registered in methanol production, suggesting a dependency of the dehydration reaction kinetics on the amount of water produced during the reaction.},<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('3064','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_3064\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The e-fuels synthesis via CO2 hydrogenation and the Sorption Enhanced Reaction technology are captivating strategies for CO2 utilization and the integration of renewable energy sources. This study focuses on enhancing the conversion of CO2 over an In2O3\/ZrO2 catalyst by incorporating LTA zeolites (3A and 4A) and a FAU zeolite (13X). Key operational parameters, such as temperature (T), Gas Hour Space Velocity (GHSV), type of zeolite, and Zeolite: Catalyst mass ratio (Z\/C), were systematically varied. LTA zeolites (3A and 4A) provided the highest CO2 conversions. The introduction of a water-adsorbing solid into the reactor significantly altered the products yield and selectivity. While the selectivity towards CH4, CH3OH, and C2H6O appeared to lay on the type of zeolite, the selectivity towards CO remained unaffected. Zeolite 3A demonstrated the greatest enhancement in selectivity towards CH4 and CH3OH, whereas the synthesis of C2H6O was favored by zeolites 4A and 13X. The Zeolite:Catalyst mass ratio also played a crucial role in process performance, influencing both CO2 conversion and product selectivity. Increasing this ratio improved CO2 conversion and reduced CO selectivity under all operating conditions, while CH4 selectivity increased. However, the selectivity toward CH3OH and C2H6O exhibited an anomalous and complementary behavior. While a maximum was observed for DME, a minimum was registered in methanol production, suggesting a dependency of the dehydration reaction kinetics on the amount of water produced during the reaction.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3064','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_3064\" 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\/S0016236125026997\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236125026997\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236125026997<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/https:\/\/doi.org\/10.1016\/j.fuel.2025.136974\" title=\"DOI de seguimiento:https:\/\/doi.org\/10.1016\/j.fuel.2025.136974\" target=\"_blank\">doi:https:\/\/doi.org\/10.1016\/j.fuel.2025.136974<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3064','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\"> Gonz\u00e1lez-Pizarro, R.;  Renda, S.;  Lasobras, J.;  Soler, J.;  Men\u00e9ndez, M.;  Herguido, J.<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('3066','tp_links')\" style=\"cursor:pointer;\">Low loading copper-based catalysts for effective CO2 hydrogenation to methanol<\/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. 408, <\/span><span class=\"tp_pub_additional_pages\">pp. 137642, <\/span><span class=\"tp_pub_additional_year\">2026<\/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_3066\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3066','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_3066\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3066','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_3066\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3066','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_3066\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{GONZALEZPIZARRO2026137642,<br \/>\r\ntitle = {Low loading copper-based catalysts for effective CO2 hydrogenation to methanol},<br \/>\r\nauthor = {R. Gonz\u00e1lez-Pizarro and S. Renda and J. Lasobras and J. Soler and M. Men\u00e9ndez and J. Herguido},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S001623612503368X},<br \/>\r\ndoi = {https:\/\/doi.org\/10.1016\/j.fuel.2025.137642},<br \/>\r\nissn = {0016-2361},<br \/>\r\nyear  = {2026},<br \/>\r\ndate = {2026-01-01},<br \/>\r\njournal = {Fuel},<br \/>\r\nvolume = {408},<br \/>\r\npages = {137642},<br \/>\r\nabstract = {Methanol synthesis via CO2 hydrogenation is an emerging Power-to-Liquid (PtL) technology aimed to accelerate the energy transition and the defossilization of key sectors, particularly maritime transport. This study focuses on the study of low loading formulations, to minimize the catalyst cost. Key operational variables including temperature (T), Weight Hourly Space Velocity (WHSV), copper and zinc loadings, and aging state were systematically varied. An overall active phase loading of 10\u00a0%wt emerged as optimal. Within this total loading, a 5\u00a0%wtCu-5\u00a0%wtZn\/ZrO2 catalysts delivered higher methanol productivity than 10\u00a0%wtCu\/ZrO2; however, the bimetallic catalysts showed pronounced deactivation under water-rich atmospheres, establishing 10\u00a0%wtCu\/ZrO2 as the most promising catalysts. Operating temperature and WHSV exerted a strong, synergistic influence on CH3OH formation; in particular, increasing WHSV shifted the reaction away from thermodynamic control and boosted methanol synthesis. Finally, the catalytic performance of these low-loading catalysts was benchmarked against high-copper-loading methanol catalysts reported in the literature by critically compare their activities as a function of the residence time (\u03c4) calculated at reaction conditions. This assessment revealed that the proposed formulation is highly competitive when compared to most conventional formulation, with a maximum methanol space time yield (STYCH3OH) of 3.9 gCH3OH gCu-1\u00a0h-1. This comparison confirms that the catalysts proposed in this study could offer a remarkably more efficient use of the active phase than the conventional high-copper-loading catalysts.},<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('3066','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_3066\" style=\"display:none;\"><div class=\"tp_abstract_entry\">Methanol synthesis via CO2 hydrogenation is an emerging Power-to-Liquid (PtL) technology aimed to accelerate the energy transition and the defossilization of key sectors, particularly maritime transport. This study focuses on the study of low loading formulations, to minimize the catalyst cost. Key operational variables including temperature (T), Weight Hourly Space Velocity (WHSV), copper and zinc loadings, and aging state were systematically varied. An overall active phase loading of 10\u00a0%wt emerged as optimal. Within this total loading, a 5\u00a0%wtCu-5\u00a0%wtZn\/ZrO2 catalysts delivered higher methanol productivity than 10\u00a0%wtCu\/ZrO2; however, the bimetallic catalysts showed pronounced deactivation under water-rich atmospheres, establishing 10\u00a0%wtCu\/ZrO2 as the most promising catalysts. Operating temperature and WHSV exerted a strong, synergistic influence on CH3OH formation; in particular, increasing WHSV shifted the reaction away from thermodynamic control and boosted methanol synthesis. Finally, the catalytic performance of these low-loading catalysts was benchmarked against high-copper-loading methanol catalysts reported in the literature by critically compare their activities as a function of the residence time (\u03c4) calculated at reaction conditions. This assessment revealed that the proposed formulation is highly competitive when compared to most conventional formulation, with a maximum methanol space time yield (STYCH3OH) of 3.9 gCH3OH gCu-1\u00a0h-1. This comparison confirms that the catalysts proposed in this study could offer a remarkably more efficient use of the active phase than the conventional high-copper-loading catalysts.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3066','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_3066\" 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\/S001623612503368X\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S001623612503368X\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S001623612503368X<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/https:\/\/doi.org\/10.1016\/j.fuel.2025.137642\" title=\"DOI de seguimiento:https:\/\/doi.org\/10.1016\/j.fuel.2025.137642\" target=\"_blank\">doi:https:\/\/doi.org\/10.1016\/j.fuel.2025.137642<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3066','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\"> Gonz\u00e1lez-Pizarro, R.;  Lasobras, J.;  Renda, S.;  Soler, J.;  Men\u00e9ndez, M.;  Herguido, J.<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('3067','tp_links')\" style=\"cursor:pointer;\">Overcoming thermodynamic limitations of the low-temperature reverse water-gas shift in a sorption-enhanced fluidized bed reactor with continuous sorbent feeding and separation (SEFBR\u00a0+\u00a0CSF)<\/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\">Separation and Purification Technology, <\/span><span class=\"tp_pub_additional_volume\">vol. 404, <\/span><span class=\"tp_pub_additional_pages\">pp. 138902, <\/span><span class=\"tp_pub_additional_year\">2026<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 1383-5866<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_3067\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3067','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_3067\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3067','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_3067\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('3067','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_3067\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{GONZALEZPIZARRO2026138902,<br \/>\r\ntitle = {Overcoming thermodynamic limitations of the low-temperature reverse water-gas shift in a sorption-enhanced fluidized bed reactor with continuous sorbent feeding and separation (SEFBR\u00a0+\u00a0CSF)},<br \/>\r\nauthor = {R. Gonz\u00e1lez-Pizarro and J. Lasobras and S. Renda and J. Soler and M. Men\u00e9ndez and J. Herguido},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S1383586626021684},<br \/>\r\ndoi = {https:\/\/doi.org\/10.1016\/j.seppur.2026.138902},<br \/>\r\nissn = {1383-5866},<br \/>\r\nyear  = {2026},<br \/>\r\ndate = {2026-01-01},<br \/>\r\njournal = {Separation and Purification Technology},<br \/>\r\nvolume = {404},<br \/>\r\npages = {138902},<br \/>\r\nabstract = {Abstract <br \/>\r\nThis work presents a novel approach for intensifying the reverse water gas shift (rWGS) reaction by integrating an advanced fluidized-bed reactor design with a continuous solid sorbent feeding\/separation strategy. The proposed Sorption Enhanced Fluidized Bed Reactor combined with Continuous Sorbent Feeding and Separation (SEFBR\u00a0+\u00a0CSF) enables continuous operation while maintaining the intensification effect traditionally associated with temporal-limited sorption-enhanced processes. This configuration externalizes the regeneration of the water-adsorbing zeolite, which is continuously and selectively withdrawn from the reactor in a partially or fully saturated state and replaced with regenerated material, thereby sustaining the sorption capacity throughout operation. Process intensification was experimentally demonstrated in the SEFBR\u00a0+\u00a0CSF configuration, which achieved CO yields significantly higher than those obtained in the conventional fluidized-bed reactor (cFBR). During the interval in which continuous sorbent feeding was applied, CO production surpassed the thermodynamic equilibrium limit at operating temperatures between 260 and 300\u00a0\u00b0C. When compared with literature data under similar conditions, the proposed system exhibited superior CO yields, particularly in the low-temperature regime where conventional LT-rWGS performance is typically limited. Overall, the SEFBR\u00a0+\u00a0CSF system represents a promising pathway for continuous sorption-enhanced operation, providing improved efficiency and enabling the process to exceed the equilibrium constraints of the LT-rWGS reaction.},<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('3067','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_3067\" style=\"display:none;\"><div class=\"tp_abstract_entry\">Abstract <br \/>\r\nThis work presents a novel approach for intensifying the reverse water gas shift (rWGS) reaction by integrating an advanced fluidized-bed reactor design with a continuous solid sorbent feeding\/separation strategy. The proposed Sorption Enhanced Fluidized Bed Reactor combined with Continuous Sorbent Feeding and Separation (SEFBR\u00a0+\u00a0CSF) enables continuous operation while maintaining the intensification effect traditionally associated with temporal-limited sorption-enhanced processes. This configuration externalizes the regeneration of the water-adsorbing zeolite, which is continuously and selectively withdrawn from the reactor in a partially or fully saturated state and replaced with regenerated material, thereby sustaining the sorption capacity throughout operation. Process intensification was experimentally demonstrated in the SEFBR\u00a0+\u00a0CSF configuration, which achieved CO yields significantly higher than those obtained in the conventional fluidized-bed reactor (cFBR). During the interval in which continuous sorbent feeding was applied, CO production surpassed the thermodynamic equilibrium limit at operating temperatures between 260 and 300\u00a0\u00b0C. When compared with literature data under similar conditions, the proposed system exhibited superior CO yields, particularly in the low-temperature regime where conventional LT-rWGS performance is typically limited. Overall, the SEFBR\u00a0+\u00a0CSF system represents a promising pathway for continuous sorption-enhanced operation, providing improved efficiency and enabling the process to exceed the equilibrium constraints of the LT-rWGS reaction.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3067','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_3067\" 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\/S1383586626021684\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S1383586626021684\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S1383586626021684<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/https:\/\/doi.org\/10.1016\/j.seppur.2026.138902\" title=\"DOI de seguimiento:https:\/\/doi.org\/10.1016\/j.seppur.2026.138902\" target=\"_blank\">doi:https:\/\/doi.org\/10.1016\/j.seppur.2026.138902<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('3067','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><\/div><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">39 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 8 <a href=\"https:\/\/creg.i3a.es\/es\/simona-renda\/?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:\/\/creg.i3a.es\/es\/simona-renda\/?limit=8&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":3,"featured_media":5618,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"footnotes":""},"categories":[240,239],"tags":[],"class_list":["post-3807","post","type-post","status-publish","format-standard","has-post-thumbnail","hentry","category-post-doctoral-researchers","category-team"],"_links":{"self":[{"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/posts\/3807","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/users\/3"}],"replies":[{"embeddable":true,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/comments?post=3807"}],"version-history":[{"count":21,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/posts\/3807\/revisions"}],"predecessor-version":[{"id":5622,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/posts\/3807\/revisions\/5622"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/media\/5618"}],"wp:attachment":[{"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/media?parent=3807"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/categories?post=3807"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/creg.i3a.es\/es\/wp-json\/wp\/v2\/tags?post=3807"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}