{"id":4674,"date":"2023-05-25T09:11:18","date_gmt":"2023-05-25T07:11:18","guid":{"rendered":"https:\/\/gpt-dev.i3a.es\/?p=4674"},"modified":"2023-05-25T09:26:56","modified_gmt":"2023-05-25T07:26:56","slug":"lucia-garcia","status":"publish","type":"post","link":"https:\/\/gpt.i3a.es\/es\/lucia-garcia\/","title":{"rendered":"Luc\u00eda Garc\u00eda"},"content":{"rendered":"<div id=\"pl-gb4674-69df1f3e59382\"  class=\"panel-layout\" ><div id=\"pg-gb4674-69df1f3e59382-0\"  class=\"panel-grid panel-has-style\" ><div class=\"siteorigin-panels-stretch panel-row-style panel-row-style-for-gb4674-69df1f3e59382-0\" data-stretch-type=\"full-width-stretch\" ><div id=\"pgc-gb4674-69df1f3e59382-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4674-69df1f3e59382-0-0-0\" 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-4674 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>Luc\u00eda Garc\u00eda<\/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-gb4674-69df1f3e59e7d\"  class=\"panel-layout\" ><div id=\"pg-gb4674-69df1f3e59e7d-0\"  class=\"panel-grid panel-no-style\" ><div 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\/>\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\/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-gb4674-69df1f3e59e7d-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> luciag@unizar.es<\/p>\n<p><strong>Address:<\/strong><\/p>\n<\/blockquote>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>\n\n<div id=\"pl-gb4674-69df1f3e5bad3\"  class=\"panel-layout\" ><div id=\"pg-gb4674-69df1f3e5bad3-0\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4674-69df1f3e5bad3-0\" ><div id=\"pgc-gb4674-69df1f3e5bad3-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4674-69df1f3e5bad3-0-0-0\" class=\"so-panel widget widget_sow-headline panel-first-child\" data-index=\"0\" ><div class=\"panel-widget-style panel-widget-style-for-gb4674-69df1f3e5bad3-0-0-0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-headline so-widget-sow-headline-default-244eb6bef45a-4674\"\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 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Ut enim ad minim veniam, quis nostrud exercitation ullamco laboris nisi ut aliquip ex ea commodo consequat. Duis aute irure dolor in reprehenderit in voluptate velit esse cillum dolore eu fugiat nulla pariatur. Excepteur sint occaecat cupidatat non proident, sunt in culpa qui officia deserunt mollit anim id est laborum .Lorem ipsum dolor sit amet, consectetur.<\/p>\n<p>Lorem ipsum dolor sit amet, consectetur adipiscing elit, sed do eiusmod tempor incididunt ut labore et dolore magna aliqua. Ut enim ad minim veniam, quis nostrud exercitation ullamco laboris nisi ut aliquip ex ea commodo consequat. Duis aute irure dolor in reprehenderit in voluptate velit esse cillum dolore eu fugiat nulla pariatur. Excepteur sint occaecat cupidatat non proident, sunt in culpa qui officia deserunt mollit anim id est laborum .Lorem ipsum dolor sit amet, consectetur.<\/p>\n<p>Lorem ipsum dolor sit amet, consectetur adipiscing elit, sed do eiusmod tempor incididunt ut labore et dolore magna aliqua. Ut enim ad minim veniam, quis nostrud exercitation ullamco laboris nisi ut aliquip ex ea commodo consequat. Duis aute irure dolor in reprehenderit in voluptate velit esse cillum dolore eu fugiat nulla pariatur. Excepteur sint occaecat cupidatat non proident, sunt in culpa qui officia deserunt mollit anim id est laborum .Lorem ipsum dolor sit amet, consectetur.<\/p>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div><\/div><div id=\"pg-gb4674-69df1f3e5bad3-1\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4674-69df1f3e5bad3-1\" ><div id=\"pgc-gb4674-69df1f3e5bad3-1-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4674-69df1f3e5bad3-1-0-0\" class=\"so-panel widget widget_sow-headline panel-first-child\" data-index=\"2\" ><div class=\"panel-widget-style panel-widget-style-for-gb4674-69df1f3e5bad3-1-0-0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-headline so-widget-sow-headline-default-244eb6bef45a-4674\"\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\tPUBLICATIONS\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 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>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\">43 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 9 <a href=\"https:\/\/gpt.i3a.es\/es\/lucia-garcia\/?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\/lucia-garcia\/?limit=9&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_2025\">2025<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Lete, Alejandro;  Lacleta, Francisco;  Garc\u00eda, Luc\u00eda;  Ruiz, Joaqu\u00edn;  Arauzo, Jes\u00fas<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('533','tp_links')\" style=\"cursor:pointer;\">Effect of calcination temperature and atmosphere on the properties and performance of CuAl catalysts for glycerol dehydration to acetol<\/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\">Biomass and Bioenergy, <\/span><span class=\"tp_pub_additional_volume\">vol. 195, <\/span><span class=\"tp_pub_additional_pages\">pp. 107725, <\/span><span class=\"tp_pub_additional_year\">2025<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 0961-9534<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_533\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('533','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_533\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('533','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_533\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('533','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_533\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{lete_effect_2025,<br \/>\r\ntitle = {Effect of calcination temperature and atmosphere on the properties and performance of CuAl catalysts for glycerol dehydration to acetol},<br \/>\r\nauthor = {Alejandro Lete and Francisco Lacleta and Luc\u00eda Garc\u00eda and Joaqu\u00edn Ruiz and Jes\u00fas Arauzo},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001369},<br \/>\r\ndoi = {10.1016\/j.biombioe.2025.107725},<br \/>\r\nissn = {0961-9534},<br \/>\r\nyear  = {2025},<br \/>\r\ndate = {2025-04-01},<br \/>\r\nurldate = {2025-04-01},<br \/>\r\njournal = {Biomass and Bioenergy},<br \/>\r\nvolume = {195},<br \/>\r\npages = {107725},<br \/>\r\nabstract = {A series of CuAl catalysts were prepared by the coprecipitation method. The objective of this study was to investigate the influence of different calcination temperatures (500, 600, and 675\u00a0\u00b0C) and calcination atmospheres (N2 or air) on the catalysts physicochemical properties and performance in the gas-phase glycerol dehydration to acetol. The catalytic tests were carried out in a fixed bed reactor at 250\u00a0\u00b0C, atmospheric pressure, and a catalyst weight to glycerol flow rate ratio (W\/m) of 30 gCatalyst min gGlycerol\u22121. The catalysts were characterized by ICP-OES, N2 adsorption-desorption, X-ray diffraction (XRD), H2 temperature programmed reduction (H2-TPR), temperature gravimetric analysis (TGA), and elemental analysis. The characterization results revealed that both calcination temperature and calcination atmosphere influenced the textural and metallic properties. Increasing the calcination temperature lowered the reduction temperature, and decreased the surface area. The calcination atmosphere influenced the surface area and pore diameter, and the N2 atmosphere generated a larger pore diameter. The best catalytic activity was achieved by the CuAl-675-N catalyst calcined at 675\u00a0\u00b0C in a N2 atmosphere, which produced a glycerol conversion of 99.0 % and an acetol yield of 67.3 %. The superior performance could be attributed to textural properties, the Cu phase, and minimized carbon deposition, establishing it as one efficient catalyst derived from inexpensive and widely available metals. This work proposes an economical and simple technique based on calcination to improve the catalytic activity of Cu-based 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('533','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_533\" style=\"display:none;\"><div class=\"tp_abstract_entry\">A series of CuAl catalysts were prepared by the coprecipitation method. The objective of this study was to investigate the influence of different calcination temperatures (500, 600, and 675\u00a0\u00b0C) and calcination atmospheres (N2 or air) on the catalysts physicochemical properties and performance in the gas-phase glycerol dehydration to acetol. The catalytic tests were carried out in a fixed bed reactor at 250\u00a0\u00b0C, atmospheric pressure, and a catalyst weight to glycerol flow rate ratio (W\/m) of 30 gCatalyst min gGlycerol\u22121. The catalysts were characterized by ICP-OES, N2 adsorption-desorption, X-ray diffraction (XRD), H2 temperature programmed reduction (H2-TPR), temperature gravimetric analysis (TGA), and elemental analysis. The characterization results revealed that both calcination temperature and calcination atmosphere influenced the textural and metallic properties. Increasing the calcination temperature lowered the reduction temperature, and decreased the surface area. The calcination atmosphere influenced the surface area and pore diameter, and the N2 atmosphere generated a larger pore diameter. The best catalytic activity was achieved by the CuAl-675-N catalyst calcined at 675\u00a0\u00b0C in a N2 atmosphere, which produced a glycerol conversion of 99.0 % and an acetol yield of 67.3 %. The superior performance could be attributed to textural properties, the Cu phase, and minimized carbon deposition, establishing it as one efficient catalyst derived from inexpensive and widely available metals. This work proposes an economical and simple technique based on calcination to improve the catalytic activity of Cu-based catalysts.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('533','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_533\" 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\/S0961953425001369\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001369\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001369<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/j.biombioe.2025.107725\" title=\"DOI de seguimiento:10.1016\/j.biombioe.2025.107725\" target=\"_blank\">doi:10.1016\/j.biombioe.2025.107725<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('533','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><h3 class=\"tp_h3\" id=\"tp_h3_2024\">2024<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Lete, Alejandro;  Raso, Raquel;  Garc\u00eda, Luc\u00eda;  Ruiz, Joaqu\u00edn;  Arauzo, Jes\u00fas<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('521','tp_links')\" style=\"cursor:pointer;\">Synthesis of ketones from glycerol and 1,2-propanediol using copper and nickel catalysts: Unraveling the impact of reaction phase and active metal<\/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. 371, <\/span><span class=\"tp_pub_additional_pages\">pp. 132001, <\/span><span class=\"tp_pub_additional_year\">2024<\/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_521\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('521','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_521\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('521','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_521\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('521','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_521\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{lete_synthesis_2024,<br \/>\r\ntitle = {Synthesis of ketones from glycerol and 1,2-propanediol using copper and nickel catalysts: Unraveling the impact of reaction phase and active metal},<br \/>\r\nauthor = {Alejandro Lete and Raquel Raso and Luc\u00eda Garc\u00eda and Joaqu\u00edn Ruiz and Jes\u00fas Arauzo},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236124011499},<br \/>\r\ndoi = {10.1016\/j.fuel.2024.132001},<br \/>\r\nissn = {0016-2361},<br \/>\r\nyear  = {2024},<br \/>\r\ndate = {2024-09-01},<br \/>\r\nurldate = {2024-09-01},<br \/>\r\njournal = {Fuel},<br \/>\r\nvolume = {371},<br \/>\r\npages = {132001},<br \/>\r\nabstract = {Catalysts based on nickel-aluminum and copper\u2013aluminum were synthesized through the coprecipitation method with a Ni or Cu content of 28\u00a0mol%, expressed as Ni\/(Ni\u00a0+\u00a0Al) or Cu\/(Cu\u00a0+\u00a0Al). The catalysts were calcined at 675\u00a0\u00b0C and thoroughly analyzed using various characterization techniques (ICP-OES, N2 adsorption\u2013desorption, NH3-TPD, CO2-TPD, XRD, H2-TPR and elemental analysis). The samples were tested in two different reaction systems, gas phase at atmospheric pressure and liquid phase at 34 absolute bar, to investigate the production of ketones from glycerol and 1,2-propanediol under reaction conditions of 227\u00a0\u00b0C and a mass of catalyst\/reagent mass flow rate ratio (W\/m) of 10 gCatalyst\u00b7min\/gReagent. The characterization results revealed catalysts with high specific surface area and nickel and copper metallic particles, exhibiting good catalytic activity towards liquid products. Gas phase reactions favored the generation of acetol and carbon deposits, which were minimal in liquid phase reactions. The active metal played a crucial role, and it was demonstrated that copper, with a higher number of acidic sites, exhibited greater selectivity towards ketones than the nickel catalyst. The best performance was achieved by the CuAl catalyst in the gas phase reaction of glycerol, with a conversion of 67.0\u00a0\u00b1\u00a04.0\u00a0%, a carbon selectivity to acetol in the liquid products of 61.4\u00a0% and a yield to acetol of 119.8 mgAcetol\/gGlycerol.},<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('521','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_521\" style=\"display:none;\"><div class=\"tp_abstract_entry\">Catalysts based on nickel-aluminum and copper\u2013aluminum were synthesized through the coprecipitation method with a Ni or Cu content of 28\u00a0mol%, expressed as Ni\/(Ni\u00a0+\u00a0Al) or Cu\/(Cu\u00a0+\u00a0Al). The catalysts were calcined at 675\u00a0\u00b0C and thoroughly analyzed using various characterization techniques (ICP-OES, N2 adsorption\u2013desorption, NH3-TPD, CO2-TPD, XRD, H2-TPR and elemental analysis). The samples were tested in two different reaction systems, gas phase at atmospheric pressure and liquid phase at 34 absolute bar, to investigate the production of ketones from glycerol and 1,2-propanediol under reaction conditions of 227\u00a0\u00b0C and a mass of catalyst\/reagent mass flow rate ratio (W\/m) of 10 gCatalyst\u00b7min\/gReagent. The characterization results revealed catalysts with high specific surface area and nickel and copper metallic particles, exhibiting good catalytic activity towards liquid products. Gas phase reactions favored the generation of acetol and carbon deposits, which were minimal in liquid phase reactions. The active metal played a crucial role, and it was demonstrated that copper, with a higher number of acidic sites, exhibited greater selectivity towards ketones than the nickel catalyst. The best performance was achieved by the CuAl catalyst in the gas phase reaction of glycerol, with a conversion of 67.0\u00a0\u00b1\u00a04.0\u00a0%, a carbon selectivity to acetol in the liquid products of 61.4\u00a0% and a yield to acetol of 119.8 mgAcetol\/gGlycerol.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('521','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_521\" 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\/S0016236124011499\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236124011499\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236124011499<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/j.fuel.2024.132001\" title=\"DOI de seguimiento:10.1016\/j.fuel.2024.132001\" target=\"_blank\">doi:10.1016\/j.fuel.2024.132001<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('521','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\"> Lete, Alejandro;  Garc\u00eda, Luc\u00eda;  Ruiz, Joaqu\u00edn;  Arauzo, Jes\u00fas<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('520','tp_links')\" style=\"cursor:pointer;\">Catalytic Conversion of 1,2-propanediol to 2-propanone: An Exploratory Study<\/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\">Chemical Engineering Transactions, <\/span><span class=\"tp_pub_additional_volume\">vol. 109, <\/span><span class=\"tp_pub_additional_pages\">pp. 133\u2013138, <\/span><span class=\"tp_pub_additional_year\">2024<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 2283-9216<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_resource_link\"><a id=\"tp_links_sh_520\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('520','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_520\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('520','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_520\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{lete_catalytic_2024,<br \/>\r\ntitle = {Catalytic Conversion of 1,2-propanediol to 2-propanone: An Exploratory Study},<br \/>\r\nauthor = {Alejandro Lete and Luc\u00eda Garc\u00eda and Joaqu\u00edn Ruiz and Jes\u00fas Arauzo},<br \/>\r\ndoi = {10.3303\/CET24109023},<br \/>\r\nissn = {2283-9216},<br \/>\r\nyear  = {2024},<br \/>\r\ndate = {2024-01-01},<br \/>\r\nurldate = {2024-01-01},<br \/>\r\njournal = {Chemical Engineering Transactions},<br \/>\r\nvolume = {109},<br \/>\r\npages = {133\u2013138},<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('520','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_520\" 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\/10.3303\/CET24109023\" title=\"DOI de seguimiento:10.3303\/CET24109023\" target=\"_blank\">doi:10.3303\/CET24109023<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('520','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><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\"> Raso, Raquel;  Lete, Alejandro;  Garc\u00eda, Luc\u00eda;  Ruiz, Joaqu\u00edn;  Oliva, Miriam;  Arauzo, Jes\u00fas<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('507','tp_links')\" style=\"cursor:pointer;\">Aqueous phase hydrogenolysis of glycerol with in situ generated hydrogen over Ni\/Al3Fe1 catalyst: effect of the calcination temperature<\/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\">RSC Advances, <\/span><span class=\"tp_pub_additional_volume\">vol. 13, <\/span><span class=\"tp_pub_additional_number\">no 8, <\/span><span class=\"tp_pub_additional_pages\">pp. 5483\u20135495, <\/span><span class=\"tp_pub_additional_year\">2023<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 2046-2069<\/span><span class=\"tp_pub_additional_note\">, (Publisher: The Royal Society of Chemistry)<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_507\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('507','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_507\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('507','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_507\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('507','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_507\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{raso_aqueous_2023,<br \/>\r\ntitle = {Aqueous phase hydrogenolysis of glycerol with in situ generated hydrogen over Ni\/Al3Fe1 catalyst: effect of the calcination temperature},<br \/>\r\nauthor = {Raquel Raso and Alejandro Lete and Luc\u00eda Garc\u00eda and Joaqu\u00edn Ruiz and Miriam Oliva and Jes\u00fas Arauzo},<br \/>\r\nurl = {https:\/\/pubs.rsc.org\/en\/content\/articlelanding\/2023\/ra\/d2ra07929a},<br \/>\r\ndoi = {10.1039\/D2RA07929A},<br \/>\r\nissn = {2046-2069},<br \/>\r\nyear  = {2023},<br \/>\r\ndate = {2023-02-01},<br \/>\r\nurldate = {2023-02-01},<br \/>\r\njournal = {RSC Advances},<br \/>\r\nvolume = {13},<br \/>\r\nnumber = {8},<br \/>\r\npages = {5483\u20135495},<br \/>\r\nabstract = {The present work studied the influence of the calcination temperature on the aqueous phase hydrogenolysis of glycerol with in situ generated hydrogen over a Ni\/Al3Fe1 catalyst. The Ni\/Al3Fe1 catalyst was synthesized by the co-precipitation method at 28 mol% of Ni (Ni\/(Ni + Al + Fe)) and a molar ratio of Al\/Fe of 3\/1. The prepared catalyst was calcined at different temperatures (500\u2013750 \u00b0C). The obtained samples were tested for the aqueous phase hydrogenolysis (APH) of glycerol and characterized by several analytical techniques (ICP-OES, H2-TPR, XRD, N2-physisorption, NH3-TPD, STEM, FESEM, and TGA). The catalyst calcined at 625 \u00b0C was selected as the best sample due to its high acidity, metal dispersion, and catalytic activity; 1,2-propanediol was the highest carbon selectivity product. In addition, it experienced lower metal leaching than the catalyst calcined at 500 \u00b0C.},<br \/>\r\nnote = {Publisher: The Royal Society of Chemistry},<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('507','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_507\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The present work studied the influence of the calcination temperature on the aqueous phase hydrogenolysis of glycerol with in situ generated hydrogen over a Ni\/Al3Fe1 catalyst. The Ni\/Al3Fe1 catalyst was synthesized by the co-precipitation method at 28 mol% of Ni (Ni\/(Ni + Al + Fe)) and a molar ratio of Al\/Fe of 3\/1. The prepared catalyst was calcined at different temperatures (500\u2013750 \u00b0C). The obtained samples were tested for the aqueous phase hydrogenolysis (APH) of glycerol and characterized by several analytical techniques (ICP-OES, H2-TPR, XRD, N2-physisorption, NH3-TPD, STEM, FESEM, and TGA). The catalyst calcined at 625 \u00b0C was selected as the best sample due to its high acidity, metal dispersion, and catalytic activity; 1,2-propanediol was the highest carbon selectivity product. In addition, it experienced lower metal leaching than the catalyst calcined at 500 \u00b0C.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('507','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_507\" 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:\/\/pubs.rsc.org\/en\/content\/articlelanding\/2023\/ra\/d2ra07929a\" title=\"https:\/\/pubs.rsc.org\/en\/content\/articlelanding\/2023\/ra\/d2ra07929a\" target=\"_blank\">https:\/\/pubs.rsc.org\/en\/content\/articlelanding\/2023\/ra\/d2ra07929a<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1039\/D2RA07929A\" title=\"DOI de seguimiento:10.1039\/D2RA07929A\" target=\"_blank\">doi:10.1039\/D2RA07929A<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('507','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\"> Fortea, Jorge;  Garc\u00eda, Luc\u00eda;  Ruiz, Joaqu\u00edn;  Oliva, Miriam;  Arauzo, Jes\u00fas<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('167','tp_links')\" style=\"cursor:pointer;\">An Insight into the Separation of 1,2-Propanediol, Ethylene Glycol, Acetol and Glycerol from an Aqueous Solution by Adsorption on Activated Carbon<\/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\">Processes 2021, Vol. 9, Page 1438, <\/span><span class=\"tp_pub_additional_volume\">vol. 9, <\/span><span class=\"tp_pub_additional_number\">no 8, <\/span><span class=\"tp_pub_additional_pages\">pp. 1438, <\/span><span class=\"tp_pub_additional_year\">2021<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 2227-9717<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_167\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('167','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_167\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('167','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_167\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('167','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_167\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Fortea2021,<br \/>\r\ntitle = {An Insight into the Separation of 1,2-Propanediol, Ethylene Glycol, Acetol and Glycerol from an Aqueous Solution by Adsorption on Activated Carbon},<br \/>\r\nauthor = {Jorge Fortea and Luc\u00eda Garc\u00eda and Joaqu\u00edn Ruiz and Miriam Oliva and Jes\u00fas Arauzo},<br \/>\r\nurl = {https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1438\/htm https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1438},<br \/>\r\ndoi = {10.3390\/PR9081438},<br \/>\r\nissn = {2227-9717},<br \/>\r\nyear  = {2021},<br \/>\r\ndate = {2021-08-01},<br \/>\r\njournal = {Processes 2021, Vol. 9, Page 1438},<br \/>\r\nvolume = {9},<br \/>\r\nnumber = {8},<br \/>\r\npages = {1438},<br \/>\r\npublisher = {Multidisciplinary Digital Publishing Institute},<br \/>\r\nabstract = {Glycerol conversion processes such as aqueous phase reforming and hydrogenolysis generate value-added compounds highly diluted in water. Because distillation is a high energy demand separation step, adsorption could be an attractive alternative to recover these chemicals. Adsorption isotherms of 1,2-propanediol, acetol, ethylene glycol and glycerol onto activated carbon were determined by batch adsorption experiments. These isotherms were fitted slightly better to the Freundlich equation than to the Langmuir equation. Acetol is the compound with the highest adsorption at concentrations smaller than 1 M. Properties of the adsorbate such as the \u2212OH group number, chain length, molecular size and dipole moment, besides characteristics of the adsorbent such as the surface area, oxygen and ash content, are considered to explain the observed results. Moreover, adsorption experiments were performed with mixtures of compounds and it was determined that the molar amount adsorbed is less than predicted from the adsorption isotherms of the individual compounds treated separately. In addition, the influence of the activated carbon thermal pre-treatment temperature on the adsorption capacity has been studied, the optimum being 800 \u00b0C. An analysis of the influence of the activated carbon characteristics showed that the most important parameters are the total pore volume and the ash content.},<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('167','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_167\" style=\"display:none;\"><div class=\"tp_abstract_entry\">Glycerol conversion processes such as aqueous phase reforming and hydrogenolysis generate value-added compounds highly diluted in water. Because distillation is a high energy demand separation step, adsorption could be an attractive alternative to recover these chemicals. Adsorption isotherms of 1,2-propanediol, acetol, ethylene glycol and glycerol onto activated carbon were determined by batch adsorption experiments. These isotherms were fitted slightly better to the Freundlich equation than to the Langmuir equation. Acetol is the compound with the highest adsorption at concentrations smaller than 1 M. Properties of the adsorbate such as the \u2212OH group number, chain length, molecular size and dipole moment, besides characteristics of the adsorbent such as the surface area, oxygen and ash content, are considered to explain the observed results. Moreover, adsorption experiments were performed with mixtures of compounds and it was determined that the molar amount adsorbed is less than predicted from the adsorption isotherms of the individual compounds treated separately. In addition, the influence of the activated carbon thermal pre-treatment temperature on the adsorption capacity has been studied, the optimum being 800 \u00b0C. An analysis of the influence of the activated carbon characteristics showed that the most important parameters are the total pore volume and the ash content.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('167','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_167\" 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.mdpi.com\/2227-9717\/9\/8\/1438\/htm https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1438\" title=\"https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1438\/htm https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1[...]\" target=\"_blank\">https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1438\/htm https:\/\/www.mdpi.com\/2227-9717\/9\/8\/1[&#8230;]<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.3390\/PR9081438\" title=\"DOI de seguimiento:10.3390\/PR9081438\" target=\"_blank\">doi:10.3390\/PR9081438<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('167','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><\/div><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">43 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 9 <a href=\"https:\/\/gpt.i3a.es\/es\/lucia-garcia\/?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\/lucia-garcia\/?limit=9&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>\n\n\n\n<p><\/p>","protected":false},"excerpt":{"rendered":"","protected":false},"author":1,"featured_media":4675,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"footnotes":""},"categories":[238,239],"tags":[],"class_list":["post-4674","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\/4674","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=4674"}],"version-history":[{"count":2,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4674\/revisions"}],"predecessor-version":[{"id":4684,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4674\/revisions\/4684"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media\/4675"}],"wp:attachment":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media?parent=4674"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/categories?post=4674"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/tags?post=4674"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}