{"id":3908,"date":"2023-09-05T15:43:57","date_gmt":"2023-09-05T13:43:57","guid":{"rendered":"https:\/\/creg-dev.i3a.es\/?p=3908"},"modified":"2024-07-19T12:31:40","modified_gmt":"2024-07-19T10:31:40","slug":"javier-lasobras-laguna","status":"publish","type":"post","link":"https:\/\/creg.i3a.es\/es\/javier-lasobras-laguna\/","title":{"rendered":"Javier Lasobras"},"content":{"rendered":"
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    Investigadores<\/a><\/h3>\n

    Javier Lasobras Laguna<\/strong><\/h1>\n\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t<\/li>\n\t\t<\/ul>\t\t\t\t
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      Tel\u00e9fono:<\/strong> +34 876 555 486<\/p>\n

      Email:<\/strong> jlasobra@unizar.es<\/a><\/p>\n

      Direcci\u00f3n:<\/strong> Lab 4.1.12 c\/Mariano Esquillor SN Edificio I+D+i, I3A, 50018, Zaragoza (Spain)<\/p>\n

      Sideral:<\/strong> Ver el perfil (CV)<\/a><\/p>\n<\/blockquote>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>\n\n

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      \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
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      Licenciado en Qu\u00edmica, M\u00e1ster en Investigaci\u00f3n en Ingenier\u00eda Qu\u00edmica y\ndoctor en Ingenier\u00eda Qu\u00edmica y del Medio Ambiente por la Universidad de\nZaragoza.<\/p>\n

      Personal de la Universidad de Zaragoza en el departamento de ingenier\u00eda\ny medio ambiente y dentro del grupo CREG desde el a\u00f1o 2009-2020 como\nt\u00e9cnico especialista de apoyo a la investigaci\u00f3n y desde 2020 como\ndoctor colaborador dentro de diversos proyectos.<\/p>\n

      Campos de investigaci\u00f3n:
      \nS\u00edntesis, pruebas y caracterizaci\u00f3n de catalizadores heterog\u00e9neos en \ndiversas reacciones (aromatizaci\u00f3n de metano, reformado, hidrogenaci\u00f3n, \noxidaci\u00f3n selectiva, \u2026) y con distintas configuraciones de reactores \n(lecho fijo, lecho fluidizado, dos zonas, con membrana).<\/p>\n

      Orcid: https:\/\/orcid.org\/0000-0002-7488-6196<\/a><\/p>\n

      Scopus:\u00a0https:\/\/www.scopus.com\/authid\/detail.uri?authorId=14056239300<\/a><\/p>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>

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      27 registros<\/span> «<\/a> ‹<\/a> 1 de 6 ›<\/a> »<\/a> <\/div><\/div>

      2026<\/h3>

      Gonz\u00e1lez-Pizarro, R.; Calero-Berrocal, R.; Lasobras, J.; Renda, S.; Rodr\u00edguez-Pardo, M. R.; Soler, J.; Men\u00e9ndez, M.; Herguido, J.<\/p>

      Tuning e-fuel selectivity in sorption-enhanced CO2 hydrogenation over In2O3\/ZrO2: The effect of LTA and FAU zeolites<\/a> Art\u00edculo de revista<\/span> <\/p>

      En: <\/span>Fuel, <\/span>vol. 406, <\/span>pp. 136974, <\/span>2026<\/span>, ISSN: 0016-2361<\/span>.<\/p>

      Resumen<\/a><\/span> | Enlaces<\/a><\/span> | BibTeX<\/a><\/span><\/p>

      @article{GONZALEZPIZARRO2026136974,
      \r\ntitle = {Tuning e-fuel selectivity in sorption-enhanced CO2 hydrogenation over In2O3\/ZrO2: The effect of LTA and FAU zeolites},
      \r\nauthor = {R. Gonz\u00e1lez-Pizarro and R. Calero-Berrocal and J. Lasobras and S. Renda and M. R. Rodr\u00edguez-Pardo and J. Soler and M. Men\u00e9ndez and J. Herguido},
      \r\nurl = {https:\/\/www.sciencedirect.com\/science\/article\/pii\/S0016236125026997},
      \r\ndoi = {https:\/\/doi.org\/10.1016\/j.fuel.2025.136974},
      \r\nissn = {0016-2361},
      \r\nyear  = {2026},
      \r\ndate = {2026-01-01},
      \r\njournal = {Fuel},
      \r\nvolume = {406},
      \r\npages = {136974},
      \r\nabstract = {The e-fuels synthesis via CO2 hydrogenation and the Sorption Enhanced Reaction technology are captivating strategies for CO2 utilization and the integration of renewable energy sources. This study focuses on enhancing the conversion of CO2 over an In2O3\/ZrO2 catalyst by incorporating LTA zeolites (3A and 4A) and a FAU zeolite (13X). Key operational parameters, such as temperature (T), Gas Hour Space Velocity (GHSV), type of zeolite, and Zeolite: Catalyst mass ratio (Z\/C), were systematically varied. LTA zeolites (3A and 4A) provided the highest CO2 conversions. The introduction of a water-adsorbing solid into the reactor significantly altered the products yield and selectivity. While the selectivity towards CH4, CH3OH, and C2H6O appeared to lay on the type of zeolite, the selectivity towards CO remained unaffected. Zeolite 3A demonstrated the greatest enhancement in selectivity towards CH4 and CH3OH, whereas the synthesis of C2H6O was favored by zeolites 4A and 13X. The Zeolite:Catalyst mass ratio also played a crucial role in process performance, influencing both CO2 conversion and product selectivity. Increasing this ratio improved CO2 conversion and reduced CO selectivity under all operating conditions, while CH4 selectivity increased. However, the selectivity toward CH3OH and C2H6O exhibited an anomalous and complementary behavior. While a maximum was observed for DME, a minimum was registered in methanol production, suggesting a dependency of the dehydration reaction kinetics on the amount of water produced during the reaction.},
      \r\nkeywords = {},
      \r\npubstate = {published},
      \r\ntppubtype = {article}
      \r\n}
      \r\n<\/pre><\/div>
      Cerrar<\/a><\/p><\/div>
      The e-fuels synthesis via CO2 hydrogenation and the Sorption Enhanced Reaction technology are captivating strategies for CO2 utilization and the integration of renewable energy sources. This study focuses on enhancing the conversion of CO2 over an In2O3\/ZrO2 catalyst by incorporating LTA zeolites (3A and 4A) and a FAU zeolite (13X). Key operational parameters, such as temperature (T), Gas Hour Space Velocity (GHSV), type of zeolite, and Zeolite: Catalyst mass ratio (Z\/C), were systematically varied. LTA zeolites (3A and 4A) provided the highest CO2 conversions. The introduction of a water-adsorbing solid into the reactor significantly altered the products yield and selectivity. While the selectivity towards CH4, CH3OH, and C2H6O appeared to lay on the type of zeolite, the selectivity towards CO remained unaffected. Zeolite 3A demonstrated the greatest enhancement in selectivity towards CH4 and CH3OH, whereas the synthesis of C2H6O was favored by zeolites 4A and 13X. The Zeolite:Catalyst mass ratio also played a crucial role in process performance, influencing both CO2 conversion and product selectivity. Increasing this ratio improved CO2 conversion and reduced CO selectivity under all operating conditions, while CH4 selectivity increased. However, the selectivity toward CH3OH and C2H6O exhibited an anomalous and complementary behavior. While a maximum was observed for DME, a minimum was registered in methanol production, suggesting a dependency of the dehydration reaction kinetics on the amount of water produced during the reaction.<\/div>
      Cerrar<\/a><\/p><\/div>