{"id":4655,"date":"2023-05-25T08:47:51","date_gmt":"2023-05-25T06:47:51","guid":{"rendered":"https:\/\/gpt-dev.i3a.es\/?p=4655"},"modified":"2023-05-25T08:50:38","modified_gmt":"2023-05-25T06:50:38","slug":"joaquin-ruiz","status":"publish","type":"post","link":"https:\/\/gpt.i3a.es\/es\/joaquin-ruiz\/","title":{"rendered":"Joaqu\u00edn Ruiz"},"content":{"rendered":"<div id=\"pl-gb4655-69dee8de2ec7c\"  class=\"panel-layout\" ><div id=\"pg-gb4655-69dee8de2ec7c-0\"  class=\"panel-grid panel-has-style\" ><div class=\"siteorigin-panels-stretch panel-row-style panel-row-style-for-gb4655-69dee8de2ec7c-0\" data-stretch-type=\"full-width-stretch\" ><div id=\"pgc-gb4655-69dee8de2ec7c-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4655-69dee8de2ec7c-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-4655 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>Joaqu\u00edn Ruiz<\/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-gb4655-69dee8de2f713\"  class=\"panel-layout\" ><div id=\"pg-gb4655-69dee8de2f713-0\"  class=\"panel-grid panel-no-style\" ><div id=\"pgc-gb4655-69dee8de2f713-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4655-69dee8de2f713-0-0-0\" 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-8b5b6f678277-4655\"\n\t\t\t\n\t\t>\n<div class=\"sow-image-container\">\n\t\t<img \n\tsrc=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2022\/03\/team-300x300.png\" width=\"300\" height=\"300\" srcset=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2022\/03\/team-300x300.png 300w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2022\/03\/team-150x150.png 150w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2022\/03\/team-12x12.png 12w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2022\/03\/team.png 512w\" sizes=\"(max-width: 300px) 100vw, 300px\" alt=\"team\" \t\tclass=\"so-widget-image\"\/>\n\t<\/div>\n\n<\/div><\/div><\/div><div id=\"pgc-gb4655-69dee8de2f713-0-1\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4655-69dee8de2f713-0-1-0\" class=\"so-panel widget widget_sow-image-grid panel-first-child\" data-index=\"1\" ><div class=\"panel-widget-style panel-widget-style-for-gb4655-69dee8de2f713-0-1-0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-image-grid so-widget-sow-image-grid-default-5ff4073610f5-4655\"\n\t\t\t\n\t\t><\/div><\/div><\/div><div id=\"panel-gb4655-69dee8de2f713-0-1-1\" 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>jruizp@unizar.es<\/p>\n<p><strong>Address:<\/strong><\/p>\n<\/blockquote>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>\n\n<div id=\"pl-gb4655-69dee8de30727\"  class=\"panel-layout\" ><div id=\"pg-gb4655-69dee8de30727-0\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4655-69dee8de30727-0\" ><div id=\"pgc-gb4655-69dee8de30727-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4655-69dee8de30727-0-0-0\" 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-4655\"\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-gb4655-69dee8de30727-0-0-1\" 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<div class=\"kc-elm kc-css-177990 kc_text_block\">\n<h4>Resarch Interests<\/h4>\n<p>Energy from biomass, aqueous reforming, catalysis.<\/p>\n<\/div>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div><div id=\"pg-gb4655-69dee8de30727-1\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4655-69dee8de30727-1\" ><div id=\"pgc-gb4655-69dee8de30727-1-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4655-69dee8de30727-1-0-0\" 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-4655\"\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 class=\"decoration-inside\"><\/div>\n\t\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n<\/div><\/div><div id=\"panel-gb4655-69dee8de30727-1-0-1\" class=\"so-panel widget widget_sow-editor panel-last-child\" data-index=\"3\" 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name=\"trp-form-language\" value=\"es\"\/><\/form><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">28 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\/joaquin-ruiz\/?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\/joaquin-ruiz\/?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_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><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Navarro, \u00c1frica;  Fonts, Isabel;  Ruiz, Joaqu\u00edn;  Ceamanos, Jes\u00fas;  Gil-Lalaguna, Noem\u00ed;  Murillo, Mar\u00eda Benita;  Gea, Gloria<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('534','tp_links')\" style=\"cursor:pointer;\">The role of biogenic waste composition on pyrolysis: Part I \u2013 Char properties<\/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. 197, <\/span><span class=\"tp_pub_additional_pages\">pp. 107778, <\/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_534\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('534','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_534\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('534','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_534\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('534','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_534\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{NAVARRO2025107778,<br \/>\r\ntitle = {The role of biogenic waste composition on pyrolysis: Part I \u2013 Char properties},<br \/>\r\nauthor = {\u00c1frica Navarro and Isabel Fonts and Joaqu\u00edn Ruiz and Jes\u00fas Ceamanos and Noem\u00ed Gil-Lalaguna and Mar\u00eda Benita Murillo and Gloria Gea},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001898},<br \/>\r\ndoi = {https:\/\/doi.org\/10.1016\/j.biombioe.2025.107778},<br \/>\r\nissn = {0961-9534},<br \/>\r\nyear  = {2025},<br \/>\r\ndate = {2025-01-01},<br \/>\r\nurldate = {2025-01-01},<br \/>\r\njournal = {Biomass and Bioenergy},<br \/>\r\nvolume = {197},<br \/>\r\npages = {107778},<br \/>\r\nabstract = {The yield and properties of char derived from the co-digested manure and its main macro-components, including organic (cellulose, lignin, and protein) components and an inorganic component (CaCO3), produced at different pyrolysis temperatures (350, 550, and 750\u00a0\u00b0C) have been studied. Experimental results obtained from a surrogate co-digested manure were compared with the theoretically calculated values to explore potential interactions between these macro-components. The char properties analyzed included elemental analysis, pH, FTIR, XPS, and specific surface area. The effect of pyrolysis temperature on many properties was similar, regardless of the precursor (macro-component). Increasing pyrolysis temperature led to higher C content (&gt;90\u00a0wt% for cellulose char at 750\u00a0\u00b0C), pH (from (\u223c7 for cellulose at 350\u00a0\u00b0C to \u223c13 for co-digested manure), and specific surface area, observing a marked development of ultramicroporosity and microporosity, especially at the highest pyrolysis temperature studied, 750\u00a0\u00b0C. An exception was observed for the char derived from proteins due to melting during pyrolysis. By far, the solids from the pyrolysis of cellulose and lignin exhibited the most microporosity development (SSDR\u00a0\u2265\u00a0650\u00a0m2\u00a0g-1), reaching, at the highest temperature studied, values close to those of physically activated carbons. Pyrolysis of the surrogate co-digested manure revealed the occurrence of Maillard reactions and also showed an interesting interaction involving CaCO3. The CaCO3 thermal decomposition is promoted when it is embedded into the organic matrix, where the CO2 generated during decomposition favored the Boudouard reaction of C from the organic components. This results in a lower biochar yield, 32\u00a0wt% versus 37\u00a0wt% (expected value), and a higher development of microporosity in the char.},<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('534','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_534\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The yield and properties of char derived from the co-digested manure and its main macro-components, including organic (cellulose, lignin, and protein) components and an inorganic component (CaCO3), produced at different pyrolysis temperatures (350, 550, and 750\u00a0\u00b0C) have been studied. Experimental results obtained from a surrogate co-digested manure were compared with the theoretically calculated values to explore potential interactions between these macro-components. The char properties analyzed included elemental analysis, pH, FTIR, XPS, and specific surface area. The effect of pyrolysis temperature on many properties was similar, regardless of the precursor (macro-component). Increasing pyrolysis temperature led to higher C content (&gt;90\u00a0wt% for cellulose char at 750\u00a0\u00b0C), pH (from (\u223c7 for cellulose at 350\u00a0\u00b0C to \u223c13 for co-digested manure), and specific surface area, observing a marked development of ultramicroporosity and microporosity, especially at the highest pyrolysis temperature studied, 750\u00a0\u00b0C. An exception was observed for the char derived from proteins due to melting during pyrolysis. By far, the solids from the pyrolysis of cellulose and lignin exhibited the most microporosity development (SSDR\u00a0\u2265\u00a0650\u00a0m2\u00a0g-1), reaching, at the highest temperature studied, values close to those of physically activated carbons. Pyrolysis of the surrogate co-digested manure revealed the occurrence of Maillard reactions and also showed an interesting interaction involving CaCO3. The CaCO3 thermal decomposition is promoted when it is embedded into the organic matrix, where the CO2 generated during decomposition favored the Boudouard reaction of C from the organic components. This results in a lower biochar yield, 32\u00a0wt% versus 37\u00a0wt% (expected value), and a higher development of microporosity in the char.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('534','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_534\" 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\/S0961953425001898\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001898\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001898<\/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.biombioe.2025.107778\" title=\"DOI de seguimiento:https:\/\/doi.org\/10.1016\/j.biombioe.2025.107778\" target=\"_blank\">doi:https:\/\/doi.org\/10.1016\/j.biombioe.2025.107778<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('534','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\"> Navarro, \u00c1frica;  Fonts, Isabel;  Ruiz, Joaqu\u00edn;  Ceamanos, Jes\u00fas;  Gil-Lalaguna, Noem\u00ed;  \u00c1brego, Javier;  Gea, Gloria<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('535','tp_links')\" style=\"cursor:pointer;\">The role of biogenic waste composition on pyrolysis: Part II \u2013 Char CO2 adsorption capacity<\/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. 197, <\/span><span class=\"tp_pub_additional_pages\">pp. 107775, <\/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_535\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('535','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_535\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('535','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_535\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('535','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_535\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{NAVARRO2025107775,<br \/>\r\ntitle = {The role of biogenic waste composition on pyrolysis: Part II \u2013 Char CO2 adsorption capacity},<br \/>\r\nauthor = {\u00c1frica Navarro and Isabel Fonts and Joaqu\u00edn Ruiz and Jes\u00fas Ceamanos and Noem\u00ed Gil-Lalaguna and Javier \u00c1brego and Gloria Gea},<br \/>\r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001862},<br \/>\r\ndoi = {https:\/\/doi.org\/10.1016\/j.biombioe.2025.107775},<br \/>\r\nissn = {0961-9534},<br \/>\r\nyear  = {2025},<br \/>\r\ndate = {2025-01-01},<br \/>\r\nurldate = {2025-01-01},<br \/>\r\njournal = {Biomass and Bioenergy},<br \/>\r\nvolume = {197},<br \/>\r\npages = {107775},<br \/>\r\nabstract = {The CO2 adsorption capacities (AC) of biochars obtained at 350, 550, and 750\u00a0\u00b0C from the main organic (cellulose, lignin, and protein) and inorganic (CaCO3) macro-components of biogenic waste, as well as from co-digested manure (CDM), have been determined for different CO2 concentrations (2\u201383\u00a0vol%) at 25\u00a0\u00b0C and atmospheric pressure. CO2 adsorption isotherms have been determined using two different experimental methodologies: thermogravimetric and fixed-bed dynamic adsorption tests, yielding similar results. The composition effect has been analyzed by comparing the adsorption performance of the chars derived from individual macro-components and the potential interactions occurring during their co-pyrolysis. Lignin and cellulose-derived chars showed higher CO2 retention (\u224877\u00a0mg gbiochar\u22121) than those produced from protein (\u224840\u00a0mg gbiochar\u22121). Pyrolyzed CaCO3 exhibited negligible CO2 adsorption. For surrogate_CDM chars, prepared at pyrolysis temperatures high enough to decompose CaCO3 in the organic matrix, experimental results showed a synergistic effect, with AC between 14 % and 47 % higher than theoretical predictions. This decomposition promoted the reverse Boudouard reaction and enhanced char microporosity. However, the improvement was insufficient to offset the dilution effect caused by the high CaCO3 content. AC results have been discussed based on the biochar textural and chemical properties, with ultramicroporosity being the key factor determining adsorption capacity. The AC of CDM-derived sorbents is similar to that of cellulose-derived, expressed per gram of waste (7\u201313\u00a0mg gwaste\u22121). Furthermore, the biochars retained at least 80 % of their initial AC after 3 adsorption-desorption cycles, indicating their potential for stable CO2 capture.},<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('535','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_535\" style=\"display:none;\"><div class=\"tp_abstract_entry\">The CO2 adsorption capacities (AC) of biochars obtained at 350, 550, and 750\u00a0\u00b0C from the main organic (cellulose, lignin, and protein) and inorganic (CaCO3) macro-components of biogenic waste, as well as from co-digested manure (CDM), have been determined for different CO2 concentrations (2\u201383\u00a0vol%) at 25\u00a0\u00b0C and atmospheric pressure. CO2 adsorption isotherms have been determined using two different experimental methodologies: thermogravimetric and fixed-bed dynamic adsorption tests, yielding similar results. The composition effect has been analyzed by comparing the adsorption performance of the chars derived from individual macro-components and the potential interactions occurring during their co-pyrolysis. Lignin and cellulose-derived chars showed higher CO2 retention (\u224877\u00a0mg gbiochar\u22121) than those produced from protein (\u224840\u00a0mg gbiochar\u22121). Pyrolyzed CaCO3 exhibited negligible CO2 adsorption. For surrogate_CDM chars, prepared at pyrolysis temperatures high enough to decompose CaCO3 in the organic matrix, experimental results showed a synergistic effect, with AC between 14 % and 47 % higher than theoretical predictions. This decomposition promoted the reverse Boudouard reaction and enhanced char microporosity. However, the improvement was insufficient to offset the dilution effect caused by the high CaCO3 content. AC results have been discussed based on the biochar textural and chemical properties, with ultramicroporosity being the key factor determining adsorption capacity. The AC of CDM-derived sorbents is similar to that of cellulose-derived, expressed per gram of waste (7\u201313\u00a0mg gwaste\u22121). Furthermore, the biochars retained at least 80 % of their initial AC after 3 adsorption-desorption cycles, indicating their potential for stable CO2 capture.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('535','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_535\" 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\/S0961953425001862\" title=\"https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001862\" target=\"_blank\">https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0961953425001862<\/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.biombioe.2025.107775\" title=\"DOI de seguimiento:https:\/\/doi.org\/10.1016\/j.biombioe.2025.107775\" target=\"_blank\">doi:https:\/\/doi.org\/10.1016\/j.biombioe.2025.107775<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('535','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><\/div><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">28 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\/joaquin-ruiz\/?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\/joaquin-ruiz\/?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":0,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"footnotes":""},"categories":[238,239],"tags":[],"class_list":["post-4655","post","type-post","status-publish","format-standard","hentry","category-permanent-members","category-team"],"_links":{"self":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4655","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=4655"}],"version-history":[{"count":2,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4655\/revisions"}],"predecessor-version":[{"id":4659,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4655\/revisions\/4659"}],"wp:attachment":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media?parent=4655"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/categories?post=4655"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/tags?post=4655"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}