Paúl Durán

Tras obtener el título de licenciado en Ingeniería Química por la universidad de Cuenca en Ecuador, expandí mi perfil académico al conseguir el grado de máster en Ingeniería Química en la Universidad de Zaragoza. Más tarde, continué especializándome en ingeniería de procesos lo que me permitió obtener mi título de doctor, en la misma institución mediante la investigación en procesos redox para la producción de hidrógeno a partir de gas natural.

A partir de entonces, formo parte del grupo de Catálisis e Ingeniería de Reactores CREG como investigador postdoctoral, donde compagino además labores técnicas dentro del Laboratorio de Tecnologías del Hidrógeno. Actualmente, mis investigaciones experimentales se enfocan en el diseño de reactores catalíticos, procesos termoquímicos relacionados con el uso de hidrógeno y biocombustibles y utilización de membranas catalíticas permeoselectivas.

I am author of 25 indexed publications and have an h-index of 10, according to Scopus® (@March 2024).

Orcid: https://orcid.org/0000-0003-2898-1085

Scopus: https://www.scopus.com/authid/detail.uri?authorId=56217070700

49 registros « ‹ 1 de 10 › »

2027

Aragüés-Aldea, P.; Gimeno-Izquierdo, C.; Durán, P.; Renda, S.; Mercader, V. D.; Francés, E.; Peña, J. A.; Herguido, J.

Distributed feeding for improved CH4 selectivity in Ni-Fe catalyzed CO2/biogas methanation Artículo de revista

En: Fuel, vol. 431, pp. 141925, 2027, ISSN: 0016-2361.

Resumen | Enlaces | BibTeX

@article{ARAGUESALDEA2027141925,

title = {Distributed feeding for improved CH4 selectivity in Ni-Fe catalyzed CO2/biogas methanation},

author = {P. Aragüés-Aldea and C. Gimeno-Izquierdo and P. Durán and S. Renda and V. D. Mercader and E. Francés and J. A. Peña and J. Herguido},

url = {https://www.sciencedirect.com/science/article/pii/S001623612603680X},

doi = {https://doi.org/10.1016/j.fuel.2026.141925},

issn = {0016-2361},

year  = {2027},

date = {2027-01-01},

journal = {Fuel},

volume = {431},

pages = {141925},

abstract = {Carbon dioxide methanation is a promising route for renewable natural gas production, although its performance is often limited by kinetic constraints under severe operating conditions. In this work, distributed reactant feeding in a four-inlet polytropic fixed-bed reactor was investigated as a process intensification strategy for CO2 methanation and biogas upgrading over a conventional methanation catalyst (Ni-Fe). The effects of feeding configuration, GHSV, temperature and feed composition on CO2 conversion and CO selectivity were systematically assessed and compared with conventional co-feeding operation. Distributed CO2 feeding consistently outperformed both conventional and hydrogen-distributed configurations, providing higher CO2 conversions and lower CO selectivities. The beneficial effect was particularly evident at high space velocities and low conversions, where kinetic limitations and selectivity to the unwanted CO are more pronounced, reaching reduction of 50 % in this parameter in the more kinetically-hindered conditions. The same qualitative behaviour was observed when upgrading a synthetic sweetened biogas (70 vol% CH4 and 30 vol% CO2), demonstrating the applicability of the proposed strategy under feed compositions relevant in practice. The improved performance is attributed to the establishment of locally H2-rich environments along the catalytic bed, which promote methane formation and mitigate CO accumulation without modifying the global operating conditions. These results highlight the potential of distributed reactant feeding as an effective reactor engineering approach for enhancing methanation performance and intensifying renewable natural gas production processes.},

keywords = {},

pubstate = {published},

tppubtype = {article}

}

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