Paúl Durán

After achieving a Bachelor’s degree in Chemical Engineering from the University of Cuenca in Ecuador, I expanded my academic profile with a Master’s degree in Chemical Engineering at the University of Zaragoza. Subsequently, I specialized in chemical engineering processes, culminating in a Ph.D. degree focused on redox processes for hydrogen production from natural gas.

Since then, I have contributed to the “Catalysis and Reactor Engineering Group” CREG as a Postdoctoral researcher while also overseeing operations in the hydrogen technologies laboratory. My current work involves experimental research in catalytic reactor design, thermochemical processes related to hydrogen and biofuels, and the utilization of permselective catalytic membranes.

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 Journal Article

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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