{"id":4381,"date":"2023-05-22T08:18:57","date_gmt":"2023-05-22T06:18:57","guid":{"rendered":"https:\/\/gpt-dev.i3a.es\/?p=4381"},"modified":"2024-07-11T11:40:16","modified_gmt":"2024-07-11T09:40:16","slug":"javier-abrego","status":"publish","type":"post","link":"https:\/\/gpt.i3a.es\/es\/javier-abrego\/","title":{"rendered":"Javier \u00c1brego"},"content":{"rendered":"<div id=\"pl-gb4381-69f1234c016c6\"  class=\"panel-layout wp-block-siteorigin-panels-layout-block\" ><div id=\"pg-gb4381-69f1234c016c6-0\"  class=\"panel-grid panel-has-style\" ><div class=\"siteorigin-panels-stretch panel-row-style panel-row-style-for-gb4381-69f1234c016c6-0\" data-stretch-type=\"full-width-stretch\" ><div id=\"pgc-gb4381-69f1234c016c6-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4381-69f1234c016c6-0-0-0\" 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-4381 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\/\">GPT<\/a><\/h3>\n<h1 style=\"text-align: center\"><strong>Javier \u00c1brego<\/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-gb4381-69f1234c021b8\"  class=\"panel-layout wp-block-siteorigin-panels-layout-block\" ><div id=\"pg-gb4381-69f1234c021b8-0\"  class=\"panel-grid panel-no-style\" ><div id=\"pgc-gb4381-69f1234c021b8-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4381-69f1234c021b8-0-0-0\" 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-8b5b6f678277-4381\"\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\/2023\/05\/foto-personal-e1673535952618-360x270-1-300x225.jpg\" width=\"300\" height=\"225\" srcset=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2023\/05\/foto-personal-e1673535952618-360x270-1-300x225.jpg 300w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2023\/05\/foto-personal-e1673535952618-360x270-1-16x12.jpg 16w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2023\/05\/foto-personal-e1673535952618-360x270-1.jpg 360w\" sizes=\"(max-width: 300px) 100vw, 300px\" title=\"foto-personal-e1673535952618-360&#215;270\" alt=\"\" \t\tclass=\"so-widget-image\"\/>\n\t<\/div>\n\n<\/div><\/div><\/div><div id=\"pgc-gb4381-69f1234c021b8-0-1\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4381-69f1234c021b8-0-1-0\" class=\"so-panel widget widget_sow-image-grid panel-first-child\" data-index=\"1\" ><div class=\"panel-widget-style panel-widget-style-for-gb4381-69f1234c021b8-0-1-0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-image-grid so-widget-sow-image-grid-default-5ff4073610f5-4381\"\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:\/\/orcid.org\/0000-0003-4493-6540\"\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\/2023\/05\/orcid.png\" class=\"sow-image-grid-image_html\" alt=\"\" title=\"Orcid\" srcset=\"https:\/\/gpt.i3a.es\/wp-content\/uploads\/2023\/05\/orcid.png 37w, https:\/\/gpt.i3a.es\/wp-content\/uploads\/2023\/05\/orcid-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-gb4381-69f1234c021b8-0-1-1\" 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>\u00a0 +34 876555483<\/p>\n<p><strong>Email: abrego@unizar.es<\/strong><\/p>\n<p><strong>Address:<\/strong> Office 31.080 c\/Mariano Esquillor SN Edificio I+D+i, I3A, GPT Zaragoza Arag\u00f3n<\/p>\n<\/blockquote>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>\n\n<div id=\"pl-gb4381-69f1234c0399d\"  class=\"panel-layout wp-block-siteorigin-panels-layout-block\" ><div id=\"pg-gb4381-69f1234c0399d-0\"  class=\"panel-grid panel-has-style\" ><div class=\"panel-row-style panel-row-style-for-gb4381-69f1234c0399d-0\" ><div id=\"pgc-gb4381-69f1234c0399d-0-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4381-69f1234c0399d-0-0-0\" class=\"so-panel widget widget_sow-headline panel-first-child panel-last-child\" data-index=\"0\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-headline so-widget-sow-headline-default-9b19b1fd772a-4381\"\n\t\t\t\n\t\t><div class=\"sow-headline-container\">\n\t\t\t\t\t\t\t<p class=\"sow-headline\">\n\t\t\t\t\t\tSOBRE M\u00cd\t\t\t\t\t\t<\/p>\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><\/div><\/div><div id=\"pg-gb4381-69f1234c0399d-1\"  class=\"panel-grid panel-no-style\" ><div id=\"pgc-gb4381-69f1234c0399d-1-0\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4381-69f1234c0399d-1-0-0\" class=\"so-panel widget widget_sow-editor panel-first-child 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<h4><strong>Research Interests<\/strong><\/h4>\n<p>Broadly, my research focus is on pyrolysis of organic waste and biomass.\u00a0I am currently interested in the development of new and\/or improved thermochemical processes for biofuels and bioproducts.<\/p>\n<p>Specifically, we are now developing a carbon-negative\u00a0<strong>pyrolysis system with autothermal operation<\/strong>. Operational tests are ongoing. We seek to further develop and scale-up this idea, ideally with an industry partner.<\/p>\n<p>Simultaneously, I work in the development of <a href=\"https:\/\/gpt.i3a.es\/es\/improving-waste-to-energy-processes-in-intensive-livestock-farming-areas-towards-a-circular-economy-mejoras-en-el-aprovechamiento-energetico-de-residuos-biomasicos-en-zonas-de-ganaderia-intensiva-h\/\">integrated valorization approaches<\/a> of various agricultural or animal residues via pyrolysis, and its integration with biomethane production.<\/p>\n<p>I have also collaborated in the development of the Flash Carbonization technology <a href=\"https:\/\/pubs.acs.org\/doi\/10.1021\/ie0301839\">developed by Professor Michael J. Antal at University of Hawai&#8217;i<\/a>\u00a0as a Visiting Scholar, and worked at <a href=\"https:\/\/www.icb.csic.es\/en\/grupo\/combustion-and-gasification-group\/\">Instituto de Carboqu\u00edmica<\/a>\u00a0(Spanish National Research Council),\u00a0both\u00a0in postdoctoral positions.<\/p>\n<p>Previously to my PhD research, I also worked in <a href=\"https:\/\/gpt.i3a.es\/es\/industry\/\">gasification<\/a> (fluidized bed and downdraft reactors) at demonstration scale.<\/p>\n<\/div>\n<\/div><\/div><\/div><div id=\"pgc-gb4381-69f1234c0399d-1-1\"  class=\"panel-grid-cell\" ><div id=\"panel-gb4381-69f1234c0399d-1-1-0\" class=\"so-panel widget widget_sow-image panel-first-child panel-last-child\" data-index=\"2\" ><div\n\t\t\t\n\t\t\tclass=\"so-widget-sow-image so-widget-sow-image-default-8b5b6f678277-4381\"\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\/2023\/05\/planta-1.jpg\" width=\"663\" height=\"884\" 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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\"> 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\"> Cordoba-Ramirez, Marlon;  Chejne, Farid;  Alean, Jader;  G\u00f3mez, Carlos A.;  Navarro-Gil, \u00c1frica;  \u00c1brego, Javier;  Gea, Gloria<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('516','tp_links')\" style=\"cursor:pointer;\">Experimental strategy for the preparation of adsorbent materials from torrefied palm kernel shell oriented to CO2 capture<\/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\">Environmental Science and Pollution Research, <\/span><span class=\"tp_pub_additional_year\">2024<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 1614-7499<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_516\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('516','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_516\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('516','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_516\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('516','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_516\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{cordoba-ramirez_experimental_2024,<br \/>\r\ntitle = {Experimental strategy for the preparation of adsorbent materials from torrefied palm kernel shell oriented to CO2 capture},<br \/>\r\nauthor = {Marlon Cordoba-Ramirez and Farid Chejne and Jader Alean and Carlos A. G\u00f3mez and \u00c1frica Navarro-Gil and Javier \u00c1brego and Gloria Gea},<br \/>\r\nurl = {https:\/\/doi.org\/10.1007\/s11356-024-32028-3},<br \/>\r\ndoi = {10.1007\/s11356-024-32028-3},<br \/>\r\nissn = {1614-7499},<br \/>\r\nyear  = {2024},<br \/>\r\ndate = {2024-02-01},<br \/>\r\nurldate = {2024-02-01},<br \/>\r\njournal = {Environmental Science and Pollution Research},<br \/>\r\nabstract = {In this study, an experimental strategy to obtain biochar and activated carbon from torrefied palm kernel shell as an efficient material for CO2 removal was evaluated. Biochar was obtained by slow pyrolysis of palm kernel shell at different temperatures (350 \u00b0C, 550 \u00b0C, and 700 \u00b0C) and previously torrefied palm kernel shell at different temperatures (220 \u00b0C, 250 \u00b0C, and 280 \u00b0C). Subsequently, activated carbons were prepared by physical activation with CO2 from previously obtained biochar samples. The CO2 adsorption capacity was measured using TGA. The experimental results showed that there is a correlation between the change in the O\/C and H\/C ratios and the functional groups \u2013OH and C=O observed via FTIR in the obtained char, indicating that both dehydration and deoxygenation reactions occur during torrefaction; this favors the deoxygenation reactions and makes them faster through CO2 liberation during the pyrolysis process. The microporous surface area shows a significant increase with higher pyrolysis temperatures, as a product of the continuous carbonization reactions, allowing more active sites for CO2 removal. Pyrolysis temperature is a key factor in CO2 adsorption capacity, leading to a CO2 adsorption capacity of up to 75 mg\/gCO2 for biochar obtained at 700 \u00b0C from non-torrefied palm kernel shell (Char700). Activated carbon obtained from torrefied palm kernel shell at 280 \u00b0C (T280-CHAR700-AC) exhibited the highest CO2 adsorption capacity (101.9 mg\/gCO2). Oxygen-containing functional groups have a direct impact on CO2 adsorption performance due to electron interactions between CO2 and these functional groups. These findings could provide a new experimental approach for obtaining optimal adsorbent materials exclusively derived from thermochemical conversion processes.},<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('516','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_516\" style=\"display:none;\"><div class=\"tp_abstract_entry\">In this study, an experimental strategy to obtain biochar and activated carbon from torrefied palm kernel shell as an efficient material for CO2 removal was evaluated. Biochar was obtained by slow pyrolysis of palm kernel shell at different temperatures (350 \u00b0C, 550 \u00b0C, and 700 \u00b0C) and previously torrefied palm kernel shell at different temperatures (220 \u00b0C, 250 \u00b0C, and 280 \u00b0C). Subsequently, activated carbons were prepared by physical activation with CO2 from previously obtained biochar samples. The CO2 adsorption capacity was measured using TGA. The experimental results showed that there is a correlation between the change in the O\/C and H\/C ratios and the functional groups \u2013OH and C=O observed via FTIR in the obtained char, indicating that both dehydration and deoxygenation reactions occur during torrefaction; this favors the deoxygenation reactions and makes them faster through CO2 liberation during the pyrolysis process. The microporous surface area shows a significant increase with higher pyrolysis temperatures, as a product of the continuous carbonization reactions, allowing more active sites for CO2 removal. Pyrolysis temperature is a key factor in CO2 adsorption capacity, leading to a CO2 adsorption capacity of up to 75 mg\/gCO2 for biochar obtained at 700 \u00b0C from non-torrefied palm kernel shell (Char700). Activated carbon obtained from torrefied palm kernel shell at 280 \u00b0C (T280-CHAR700-AC) exhibited the highest CO2 adsorption capacity (101.9 mg\/gCO2). Oxygen-containing functional groups have a direct impact on CO2 adsorption performance due to electron interactions between CO2 and these functional groups. These findings could provide a new experimental approach for obtaining optimal adsorbent materials exclusively derived from thermochemical conversion processes.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('516','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_516\" 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:\/\/doi.org\/10.1007\/s11356-024-32028-3\" title=\"https:\/\/doi.org\/10.1007\/s11356-024-32028-3\" target=\"_blank\">https:\/\/doi.org\/10.1007\/s11356-024-32028-3<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1007\/s11356-024-32028-3\" title=\"DOI de seguimiento:10.1007\/s11356-024-32028-3\" target=\"_blank\">doi:10.1007\/s11356-024-32028-3<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('516','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\"> Villasana, Yanet;  Armenise, Sabino;  \u00c1brego, Javier;  Atienza-Mart\u00ednez, Mar\u00eda;  Hablich, Karina;  Bimbela, Fernando;  Cornejo, Alfonso;  Gand\u00eda, Luis M.<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('514','tp_links')\" style=\"cursor:pointer;\">Exploring a Low-Cost Valorization Route for Amazonian Cocoa Pod Husks through Thermochemical and Catalytic Upgrading of Pyrolysis Vapors<\/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\">ACS Omega, <\/span><span class=\"tp_pub_additional_volume\">vol. 8, <\/span><span class=\"tp_pub_additional_number\">no 40, <\/span><span class=\"tp_pub_additional_pages\">pp. 37610\u201337621, <\/span><span class=\"tp_pub_additional_year\">2023<\/span><span class=\"tp_pub_additional_note\">, (Publisher: American Chemical Society)<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_514\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('514','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_514\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('514','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_514\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('514','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_514\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{villasana_exploring_2023,<br \/>\r\ntitle = {Exploring a Low-Cost Valorization Route for Amazonian Cocoa Pod Husks through Thermochemical and Catalytic Upgrading of Pyrolysis Vapors},<br \/>\r\nauthor = {Yanet Villasana and Sabino Armenise and Javier \u00c1brego and Mar\u00eda Atienza-Mart\u00ednez and Karina Hablich and Fernando Bimbela and Alfonso Cornejo and Luis M. Gand\u00eda},<br \/>\r\nurl = {https:\/\/doi.org\/10.1021\/acsomega.3c06672},<br \/>\r\ndoi = {10.1021\/acsomega.3c06672},<br \/>\r\nyear  = {2023},<br \/>\r\ndate = {2023-10-01},<br \/>\r\nurldate = {2023-10-01},<br \/>\r\njournal = {ACS Omega},<br \/>\r\nvolume = {8},<br \/>\r\nnumber = {40},<br \/>\r\npages = {37610\u201337621},<br \/>\r\nabstract = {Ecuador as an international leader in the production of cocoa beans produced more than 300\u2009000 tons in 2021; hence, the management and valorization of the 2 MM tons of waste generated annually by this industry have a strategic and socioeconomic value. Consequently, appropriate technologies to avoid environmental problems and promote sustainable development and the bioeconomy, especially considering that this is a megadiverse country, are of the utmost relevance. For this reason, we explored a low-cost pyrolysis route for valorizing cocoa pod husks from Ecuador\u2019s Amazonian region, aiming at producing pyrolysis liquids (bio-oil), biochar, and gas as an alternative chemical source from cocoa residues in the absence of hydrogen. Downstream catalytic processing of hot pyrolysis vapors using Mo- and\/or Ni-based catalysts and standalone \u03b3-Al2O3 was applied for obtaining upgraded bio-oils in a laboratory-scale fixed bed reactor, at 500 \u00b0C in a N2 atmosphere. As a result, bimetallic catalysts increased the bio-oil aqueous phase yield by 6.6%, at the expense of the organic phase due to cracking reactions according to nuclear magnetic resonance (NMR) and gas chromatography\u2013mass spectrometry (GC\u2013MS) results. Overall product yield remained constant, in comparison to pyrolysis without any downstream catalytic treatment (bio-oil \u223c39.0\u201340.0 wt % and permanent gases 24.6\u201326.6 wt %). Ex situ reduced and passivated MoNi\/\u03b3-Al2O3 led to the lowest organic phase and highest aqueous phase yields. The product distribution between the two liquid phases was also modified by the catalytic upgrading experiments carried out, according to heteronuclear single-quantum correlation (HSQC), total correlation spectroscopy (TOCSY), and NMR analyses. The detailed composition distribution reported here shows the chemical production potential of this residue and serves as a starting point for subsequent valorizing technologies and\/or processes in the food and nonfood industry beneficiating society, environment, economy, and research.},<br \/>\r\nnote = {Publisher: American Chemical Society},<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('514','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_514\" style=\"display:none;\"><div class=\"tp_abstract_entry\">Ecuador as an international leader in the production of cocoa beans produced more than 300\u2009000 tons in 2021; hence, the management and valorization of the 2 MM tons of waste generated annually by this industry have a strategic and socioeconomic value. Consequently, appropriate technologies to avoid environmental problems and promote sustainable development and the bioeconomy, especially considering that this is a megadiverse country, are of the utmost relevance. For this reason, we explored a low-cost pyrolysis route for valorizing cocoa pod husks from Ecuador\u2019s Amazonian region, aiming at producing pyrolysis liquids (bio-oil), biochar, and gas as an alternative chemical source from cocoa residues in the absence of hydrogen. Downstream catalytic processing of hot pyrolysis vapors using Mo- and\/or Ni-based catalysts and standalone \u03b3-Al2O3 was applied for obtaining upgraded bio-oils in a laboratory-scale fixed bed reactor, at 500 \u00b0C in a N2 atmosphere. As a result, bimetallic catalysts increased the bio-oil aqueous phase yield by 6.6%, at the expense of the organic phase due to cracking reactions according to nuclear magnetic resonance (NMR) and gas chromatography\u2013mass spectrometry (GC\u2013MS) results. Overall product yield remained constant, in comparison to pyrolysis without any downstream catalytic treatment (bio-oil \u223c39.0\u201340.0 wt % and permanent gases 24.6\u201326.6 wt %). Ex situ reduced and passivated MoNi\/\u03b3-Al2O3 led to the lowest organic phase and highest aqueous phase yields. The product distribution between the two liquid phases was also modified by the catalytic upgrading experiments carried out, according to heteronuclear single-quantum correlation (HSQC), total correlation spectroscopy (TOCSY), and NMR analyses. The detailed composition distribution reported here shows the chemical production potential of this residue and serves as a starting point for subsequent valorizing technologies and\/or processes in the food and nonfood industry beneficiating society, environment, economy, and research.<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('514','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_514\" 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:\/\/doi.org\/10.1021\/acsomega.3c06672\" title=\"https:\/\/doi.org\/10.1021\/acsomega.3c06672\" target=\"_blank\">https:\/\/doi.org\/10.1021\/acsomega.3c06672<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1021\/acsomega.3c06672\" title=\"DOI de seguimiento:10.1021\/acsomega.3c06672\" target=\"_blank\">doi:10.1021\/acsomega.3c06672<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('514','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><h3 class=\"tp_h3\" id=\"tp_h3_2020\">2020<\/h3><div class=\"tp_publication tp_publication_article\"><div class=\"tp_pub_info\"><p class=\"tp_pub_author\"> Atienza-Mart\u00ednez, Mar\u00eda;  Suraini, Nurull Nadia Binti;  \u00c1brego, Javier;  Fonts, Isabel;  L\u00e1zaro, Luisa;  Carstensen, Hans-Heinrich;  Gea, Gloria<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('196','tp_links')\" style=\"cursor:pointer;\">Functionalization of sewage sludge char by partial oxidation with molecular oxygen to enhance its adsorptive 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\">Journal of Cleaner Production, <\/span><span class=\"tp_pub_additional_pages\">pp. 125201, <\/span><span class=\"tp_pub_additional_year\">2020<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 09596526<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_resource_link\"><a id=\"tp_links_sh_196\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('196','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_196\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('196','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_196\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Atienza-Martinez2020b,<br \/>\r\ntitle = {Functionalization of sewage sludge char by partial oxidation with molecular oxygen to enhance its adsorptive properties},<br \/>\r\nauthor = {Mar\u00eda Atienza-Mart\u00ednez and Nurull Nadia Binti Suraini and Javier \u00c1brego and Isabel Fonts and Luisa L\u00e1zaro and Hans-Heinrich Carstensen and Gloria Gea},<br \/>\r\nurl = {https:\/\/linkinghub.elsevier.com\/retrieve\/pii\/S0959652620352458},<br \/>\r\ndoi = {10.1016\/j.jclepro.2020.125201},<br \/>\r\nissn = {09596526},<br \/>\r\nyear  = {2020},<br \/>\r\ndate = {2020-11-01},<br \/>\r\njournal = {Journal of Cleaner Production},<br \/>\r\npages = {125201},<br \/>\r\npublisher = {Elsevier},<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('196','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_196\" 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:\/\/linkinghub.elsevier.com\/retrieve\/pii\/S0959652620352458\" title=\"https:\/\/linkinghub.elsevier.com\/retrieve\/pii\/S0959652620352458\" target=\"_blank\">https:\/\/linkinghub.elsevier.com\/retrieve\/pii\/S0959652620352458<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.1016\/j.jclepro.2020.125201\" title=\"DOI de seguimiento:10.1016\/j.jclepro.2020.125201\" target=\"_blank\">doi:10.1016\/j.jclepro.2020.125201<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('196','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\"> Arauzo, Pablo J;  Atienza-Mart\u00ednez, Mar\u00eda;  \u00c1brego, Javier;  Olszewski, Maciej P;  Cao, Zebin;  Kruse, Andrea<\/p><p class=\"tp_pub_title\"><a class=\"tp_title_link\" onclick=\"teachpress_pub_showhide('201','tp_links')\" style=\"cursor:pointer;\">Combustion Characteristics of Hydrochar and Pyrochar Derived from Digested Sewage Sludge<\/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\">Energies, <\/span><span class=\"tp_pub_additional_volume\">vol. 13, <\/span><span class=\"tp_pub_additional_number\">no 16, <\/span><span class=\"tp_pub_additional_pages\">pp. 4164, <\/span><span class=\"tp_pub_additional_year\">2020<\/span>, <span class=\"tp_pub_additional_issn\">ISSN: 1996-1073<\/span>.<\/p><p class=\"tp_pub_menu\"><span class=\"tp_abstract_link\"><a id=\"tp_abstract_sh_201\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('201','tp_abstract')\" title=\"Mostrar resumen\" style=\"cursor:pointer;\">Resumen<\/a><\/span> | <span class=\"tp_resource_link\"><a id=\"tp_links_sh_201\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('201','tp_links')\" title=\"Mostrar enlaces y recursos\" style=\"cursor:pointer;\">Enlaces<\/a><\/span> | <span class=\"tp_bibtex_link\"><a id=\"tp_bibtex_sh_201\" class=\"tp_show\" onclick=\"teachpress_pub_showhide('201','tp_bibtex')\" title=\"Mostrar entrada BibTeX \" style=\"cursor:pointer;\">BibTeX<\/a><\/span><\/p><div class=\"tp_bibtex\" id=\"tp_bibtex_201\" style=\"display:none;\"><div class=\"tp_bibtex_entry\"><pre>@article{Arauzo2020b,<br \/>\r\ntitle = {Combustion Characteristics of Hydrochar and Pyrochar Derived from Digested Sewage Sludge},<br \/>\r\nauthor = {Pablo J Arauzo and Mar\u00eda Atienza-Mart\u00ednez and Javier \u00c1brego and Maciej P Olszewski and Zebin Cao and Andrea Kruse},<br \/>\r\nurl = {https:\/\/www.mdpi.com\/1996-1073\/13\/16\/4164},<br \/>\r\ndoi = {10.3390\/en13164164},<br \/>\r\nissn = {1996-1073},<br \/>\r\nyear  = {2020},<br \/>\r\ndate = {2020-08-01},<br \/>\r\njournal = {Energies},<br \/>\r\nvolume = {13},<br \/>\r\nnumber = {16},<br \/>\r\npages = {4164},<br \/>\r\npublisher = {MDPI AG},<br \/>\r\nabstract = {&lt;p&gt;In this paper, hydrochars and pyrochars were produced at 260 &deg;C under different residence times (2 and 4 h) using anaerobic digested sewage sludge (SSL) as initial feedstock. The effect of reaction time on the fuel properties of hydrochars and pyrochars was evaluated. Moreover, the combustion kinetics of raw SSL and the derived pyrochars and hydrochars without coal blending were determined at two different air flows (20 and 90 mL\/min) and compared. In the same conditions, the yield of hydrochar was significantly lower than that of pyrochar, confirming the different reaction pathways followed in each process. The results showed hydrochars have lower carbon recovery and energy yield than pyrochars, making the latter more suitable for energy purposes. The thermogravimetric combustion study showed that both thermochemical treatments increased the ignition temperature but decreased the burnout temperature, which results in higher stability during handling and storage. However, raw SSL is better for combustion than hydrochar according to the combustibility index. In addition, the kinetic study showed that the activation energy of the combustion of biochars, especially pyrochar, is lower than that of raw SSL, which is advantageous for their combustion.&lt;\/p&gt;},<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('201','tp_bibtex')\">Cerrar<\/a><\/p><\/div><div class=\"tp_abstract\" id=\"tp_abstract_201\" style=\"display:none;\"><div class=\"tp_abstract_entry\">&lt;p&gt;In this paper, hydrochars and pyrochars were produced at 260 &deg;C under different residence times (2 and 4 h) using anaerobic digested sewage sludge (SSL) as initial feedstock. The effect of reaction time on the fuel properties of hydrochars and pyrochars was evaluated. Moreover, the combustion kinetics of raw SSL and the derived pyrochars and hydrochars without coal blending were determined at two different air flows (20 and 90 mL\/min) and compared. In the same conditions, the yield of hydrochar was significantly lower than that of pyrochar, confirming the different reaction pathways followed in each process. The results showed hydrochars have lower carbon recovery and energy yield than pyrochars, making the latter more suitable for energy purposes. The thermogravimetric combustion study showed that both thermochemical treatments increased the ignition temperature but decreased the burnout temperature, which results in higher stability during handling and storage. However, raw SSL is better for combustion than hydrochar according to the combustibility index. In addition, the kinetic study showed that the activation energy of the combustion of biochars, especially pyrochar, is lower than that of raw SSL, which is advantageous for their combustion.&lt;\/p&gt;<\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('201','tp_abstract')\">Cerrar<\/a><\/p><\/div><div class=\"tp_links\" id=\"tp_links_201\" 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\/1996-1073\/13\/16\/4164\" title=\"https:\/\/www.mdpi.com\/1996-1073\/13\/16\/4164\" target=\"_blank\">https:\/\/www.mdpi.com\/1996-1073\/13\/16\/4164<\/a><\/li><li><i class=\"ai ai-doi\"><\/i><a class=\"tp_pub_list\" href=\"https:\/\/dx.doi.org\/10.3390\/en13164164\" title=\"DOI de seguimiento:10.3390\/en13164164\" target=\"_blank\">doi:10.3390\/en13164164<\/a><\/li><\/ul><\/div><p class=\"tp_close_menu\"><a class=\"tp_close\" onclick=\"teachpress_pub_showhide('201','tp_links')\">Cerrar<\/a><\/p><\/div><\/div><\/div><\/div><div class=\"tablenav\"><div class=\"tablenav-pages\"><span class=\"displaying-num\">23 registros<\/span> <a class=\"page-numbers button disabled\">&laquo;<\/a> <a class=\"page-numbers button disabled\">&lsaquo;<\/a> 1 de 5 <a href=\"https:\/\/gpt.i3a.es\/es\/javier-abrego\/?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\/javier-abrego\/?limit=5&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":4636,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"footnotes":""},"categories":[238,239],"tags":[],"class_list":["post-4381","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\/4381","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=4381"}],"version-history":[{"count":8,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4381\/revisions"}],"predecessor-version":[{"id":5245,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/posts\/4381\/revisions\/5245"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media\/4636"}],"wp:attachment":[{"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/media?parent=4381"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/categories?post=4381"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/gpt.i3a.es\/es\/wp-json\/wp\/v2\/tags?post=4381"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}