Zobrazeno 1 - 10
of 143
pro vyhledávání: '"Javier Herguido"'
Autor:
Javier Lasobras, Jaime Soler, Javier Herguido, Miguel Menéndez, Alonso Jimenez, Mariana da Silva, María J. Franco, Izaskun Barrio, Jesús Làzaro
Publikováno v:
Frontiers in Energy Research, Vol 7 (2019)
Methane aromatization is a promising technology for the transformation of natural gas into liquid products, but suffers from the problem of catalyst deactivation by coke. A two-zone fluidized bed reactor has been proposed as a tool to counteract the
Externí odkaz:
https://doaj.org/article/9f8fc7be013f469fb01d0a06220d7634
Publikováno v:
Membranes, Vol 11, Iss 7, p 472 (2021)
Methanol can be obtained through CO2 hydrogenation in a membrane reactor with higher yield or lower pressure than in a conventional packed bed reactor. In this study, we explore a new kind of membrane with the potential suitability for such membrane
Externí odkaz:
https://doaj.org/article/68db55f557ce46b19005ea7eac60ae9a
Publikováno v:
Membranes, Vol 3, Iss 2, Pp 69-86 (2013)
Several reactor configurations have been tested for catalytic propane dehydrogenation employing Pt-Sn/MgAl2O4 as a catalyst. Pd-Ag alloy membranes coupled to the multifunctional Two-Zone Fluidized Bed Reactor (TZFBR) provide an improvement in propane
Externí odkaz:
https://doaj.org/article/7cd01caf6cbd486693ad8ef91da9d604
Publikováno v:
Catalysis Today. :219-224
Conversion of methanol to light olefins (MTO) using SAPO-34 molecular-sieve as the reaction catalyst was studied in a fluidized bed reactor within the temperature range of 400–550 °C by 50 °C increments and under 50, 66.6 and 90 vol% of methanol
Publikováno v:
Industrial & Engineering Chemistry Research. 61:5757-5765
Autor:
Pablo Aragüés, Paúl Durán, Víctor Mercader, Andrés Sanz, Eva Francés, Javier Herguido, José Ángel Peña
Publikováno v:
Jornada de Jóvenes Investigadores del I3A. 10
Este abstract trata del análisis de las condiciones en las que se lleva a cabo el proceso SESaR para la obtención de Gas Natural Sintético (SNG). Los ensayos se han hecho en un reactor de lecho fijo, con un catalizador de Ni-Fe soportado sobre al
Autor:
M. Tovar, Javier Herguido, Izumi Kumakiri, Javier Lasobras, Miguel Menéndez, Sadao Araki, R. Raso
Publikováno v:
Catalysis Today. 364:270-275
A zeolite membrane reactor can be employed for hydrogenation of CO2 to methanol. The removal of water from the reaction environment would increase the reaction rate and the achievable conversion. The separation of water from mixtures containing CO2,
Publikováno v:
Catalysis Today. 362:155-161
Deactivation of SAPO-34 catalyst is a common problem in methanol to olefins (MTO) process. Due to its shape selectivity to olefins, SAPO-34 is one of the best zeolites for this purpose, but this advantage also makes its deactivation faster and more p
Autor:
A. Paúl, José Ángel Peña, R. Sepúlveda, Javier Herguido, P. J. Lloreda-Jurado, Eva María Pérez-Soriano
Publikováno v:
Materials Science and Technology. 36:1227-1237
Iron oxide scaffolds with gradient porosity were fabricated using the freeze-casting technique. Doped iron oxide particles were employed to generate stable particle suspensions in camphene using th...
Publikováno v:
Renewable Energy. 151:619-626
Production of high purity hydrogen from biogas by combined dry reforming of methane and steam iron process (SIP), outlines a serious drawback with the possible formation of coke deposits along reduction steps of the iron oxide. Steam used along reoxi