{"id":3764,"date":"2023-09-01T13:05:31","date_gmt":"2023-09-01T11:05:31","guid":{"rendered":"https:\/\/creg-dev.i3a.es\/?p=3764"},"modified":"2024-07-19T13:19:41","modified_gmt":"2024-07-19T11:19:41","slug":"miguel-menendez","status":"publish","type":"post","link":"https:\/\/creg.i3a.es\/es\/miguel-menendez\/","title":{"rendered":"Miguel Men\u00e9ndez"},"content":{"rendered":"
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    Investigadores<\/a><\/h3>\n

    Miguel Men\u00e9ndez Sastre\n<\/strong><\/h1>\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 976761152<\/p>\n

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

      Direcci\u00f3n:<\/strong> Office 5.1.05 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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      Catedr\u00e1tico de Ingenier\u00eda Qu\u00edmica en Universidad de Zaragoza. Mis l\u00edneas de investigaci\u00f3n han estado en su mayor parte relacionadas con fluidizaci\u00f3n, membranas y reactores catal\u00edticos. Desde mi tesis doctoral, sobre el proceso FCC de craqueo catal\u00edtico en lecho fluidizado, hasta mi investigaci\u00f3n actual, sobre nuevos reactores para obtenci\u00f3n de combustibles a partir de energ\u00edas renovables (e-metanol y e-DME), he investigado en una gran variedad de procesos, fundamentalmente catal\u00edticos (acoplamiento oxidativo de metano, oxidaci\u00f3n selectiva de hidrocarburos, oxidaci\u00f3n total de contaminantes, dehidrogenaci\u00f3n de parafinas, transformaci\u00f3n de metanol a hidrocarburos u olefinas).<\/div>\n<\/div>\n<\/div>\n

      He colaborado en la Universidad de Zaragoza como Secretario y Director de Departamento, Vicedecano y Director de Secretariado de Proyectos Europeos. He servido como evaluador en diversas agencias nacionales y extranjeras, ademas de como editor asociado de Chemical Engineering Journal y miembro del Panel PE8 (Product and Process Engineering) del ERC para Advanced Grants.
      \nSoy coautor de 169 art\u00edculos en revistas con evaluaci\u00f3n externa y 18 libros o cap\u00edtulos de libros. Indice H (WoK)= 38. Indice Google: 48. Entre mis publicaciones los reactores de membrana y las membranas de zeolita (77 art\u00edculos) y los reactores de lecho fluidizado (50 art\u00edculos) han\nsido los temas principales.<\/p>\n

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      Orcid: http:\/\/orcid.org\/0000-0002-2494-102X<\/a><\/p>\n

      Scopus: https:\/\/www.scopus.com\/authid\/detail.uri?authorId=7102690468<\/a><\/p>\n<\/div>\n<\/div><\/div><\/div><\/div><\/div>

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      152 registros<\/span> «<\/a> ‹<\/a> 1 de 31 ›<\/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>