@misc{GonzalezCastanoIvanovaIoanidesetal., author = {Gonz{\´a}lez-Casta{\~n}o, Miriam and Ivanova, Svetlana and Ioanides, Theophiles and Centeno, Miguel Angel and Arellano-Garc{\´i}a, Harvey and Odriozola, Jos{\´e} Antonio}, title = {Zr and Fe on Pt/CeO2-MOx/Al2O3 catalysts for WGS reaction}, series = {International Journal of Energy Research}, journal = {International Journal of Energy Research}, issn = {1099-114X}, doi = {10.1002/er.6646}, pages = {12}, abstract = {By evaluating the functional modifications induced by Zr and Fe as dopants in Pt/CeO2-MOx/Al2O3 catalysts (M = Fe and Zr), the key features for improving water gas shift (WGS) performance for these systems have been addressed. Pt/ceria intrinsic WGS activity is often related to improved H2 surface dynamics, H2O absorption, retentions and dissociation capacities which are influenced greatly by the support nature. Two metals, iron and zirconia, were chosen as ceria dopants in this work, either in separate manner or combined. Iron incorporation resulted in CO-redox properties and oxygen storage capacities (OSC) improvement but the formation of Ce-Fe solid solutions did not offer any catalytic benefit, while the Zr incorporation influenced in a great manner surface electron densities and shows higher catalytic activity. When combined both metals showed an important synergy evidenced by 30\% higher CO conversions and attributed to greater surface electron densities population and therefore absorption and activity. This work demonstrates that for Pt/ceria catalysts OSC enhancement does not necessarily imply a catalytic promotion.}, language = {en} } @misc{BaenaMorenoGonzalezCastanoNavarrodeMigueletal., author = {Baena-Moreno, Francisco Manuel and Gonz{\´a}lez-Casta{\~n}o, Miriam and Navarro de Miguel, Juan Carlos and Miah, Kamal Uddin Mohammad and Ossenbrink, Ralf and Odriozola, Jos{\´e} Antonio and Arellano-Garc{\´i}a, Harvey}, title = {Stepping toward Efficient Microreactors for CO2 Methanation: 3D Printed Gyroid Geometry}, series = {ACS Sustainable Chemistry \& Engineering}, volume = {9}, journal = {ACS Sustainable Chemistry \& Engineering}, number = {24}, issn = {2168-0485}, doi = {10.1021/acssuschemeng.1c01980}, pages = {8198 -- 8206}, abstract = {This work presents a comparative study towards the development of efficient micro-reactors based on 3D-printed structures. Thus, the study evaluates the influence of the metal substrate geometry on the performance of structured catalysts for the CO2 methanation reaction. For this purpose, 0.5\%Ru-15\%Ni/MgAl2O4 catalyst is wash coated over two different micro-monolithic metal substrates: a conventional parallel channel honeycomb structure and a novel 3D-printed structure with a complex gyroid geometry. The effect of the metal substrate geometry is analyzed for several CO2 sources including ideal flue gas atmospheres, the presence of residual CH4 and CO in the flue gas, as well as simulated biogas sources. The advantages of the gyroid-3D complex geometries over the honeycomb structures are shown for all evaluated conditions, providing at the best-case scenario a 14\% improvement of CO2 conversion. Moreover, this contribution shows that systematically tailoring geometrical features of structured catalysts becomes an effective strategy to achieve improved catalysts performances independent of the flue gas composition. By enhancing the transport processes and the gas-catalyst interactions, the employed gyroid 3D metal substrates enable boosted CO2 conversions and greater CH4 selectivity within diffusional controlled regimes.}, language = {en} } @misc{GonzalezCastanoNavarrodeMiguelPernkovaetal., author = {Gonz{\´a}lez-Casta{\~n}o, Miriam and Navarro de Miguel, Juan Carlos and Pernkova, A. and Centeno, Miguel Angel and Odriozola, Jos{\´e} Antonio and Arellano-Garc{\´i}a, Harvey}, title = {Ni/YMnO3 perovskite catalyst for CO2 methanation}, series = {Applied Materials Today}, volume = {23}, journal = {Applied Materials Today}, doi = {10.1016/j.apmt.2021.101055}, abstract = {Ni/YMnO3 perovskite catalyst for CO2 methanation}, language = {en} } @misc{FrankenMatriscianoSarietal., author = {Franken, Tim and Matrisciano, Andrea and Sari, Rafael and Robles, Alvaro Fogue and Monsalve-Serrano, Javier and Pintor, Dario Lopez and Pasternak, Michal and Garcia, Antonio and Mauß, Fabian}, title = {Modeling of Reactivity Controlled Compression Ignition Combustion Using a Stochastic Reactor Model Coupled with Detailed Chemistry}, series = {SAE technical papers : 15th International Conference on Engines \& Vehicles}, journal = {SAE technical papers : 15th International Conference on Engines \& Vehicles}, issn = {0148-7191}, doi = {10.4271/2021-24-0014}, pages = {18}, abstract = {Advanced combustion concepts such as reactivity controlled compression ignition (RCCI) have been proven to be capable of fundamentally improve the conventional Diesel combustion by mitigating or avoiding the soot-NOx trade-off, while delivering comparable or better thermal efficiency. To further facilitate the development of the RCCI technology, a robust and possibly computationally efficient simulation framework is needed. While many successful studies have been published using 3D-CFD coupled with detailed combustion chemistry solvers, the maturity level of the 0D/1D based software solution offerings is relatively limited. The close interaction between physical and chemical processes challenges the development of predictive numerical tools, particularly when spatial information is not available. The present work discusses a novel stochastic reactor model (SRM) based modeling framework capable of predicting the combustion process and the emission formation in a heavy-duty engine running under RCCI combustion mode. The combination of physical turbulence models, detailed emission formation sub-models and stateof-the-art chemical kinetic mechanisms enables the model to be computationally inexpensive compared to the 3D-CFD approaches. A chemical kinetic mechanism composed of 248 species and 1428 reactions was used to describe the oxidation of gasoline and diesel using a primary reference fuel (PRF)mixture and n-heptane, respectively. The model is compared to operating conditions from a single-cylinder research engine featuring different loads, speeds, EGR and gasoline fuel fractions. The model was found to be capable of reproducing the combustion phasing as well as the emission trends measured on the test bench, at some extent. The proposed modeling approach represents a promising basis towards establishing a comprehensive modeling framework capable of simulating transient operation as well as fuel property sweeps with acceptable accuracy.}, language = {en} } @misc{TarifaGonzalezCastanoCazanaetal., author = {Tarifa, Pilar and Gonz{\´a}lez-Casta{\~n}o, Miriam and Caza{\~n}a, F. and Monz{\´o}n, Antonio and Arellano-Garc{\´i}a, Harvey}, title = {Development of one-pot Cu/cellulose derived carbon catalysts for RWGS reaction}, series = {Fuel}, volume = {Vol. 319}, journal = {Fuel}, issn = {0016-2361}, doi = {10.1016/j.fuel.2022.123707}, pages = {7}, abstract = {A series of Cu-based catalysts promoted with Fe, Ce and Al supported on cellulose derived carbon (CDC) was prepared by biomorphic mineralization technique for the RWGS reaction. The excellent Cu dispersions (7 nm at ca. 30 wt\% Cu) along with the resilience toward metal sintering attained in the entire catalysts series highlight one-pot decomposition of cellulose under reducing atmosphere as an excellent synthesis method which enable obtaining well-dispersed Cu nanoparticles. The influence of incorporating a second metal oxide over biomorphic mineralized Cu systems was also investigated. With the Cu-Ce system exhibiting the best catalyst performance of the catalysts' series, the enhanced catalyst performances were majorly ascribed to the catalysts redox properties. The lineal relationships stablished between oxygen exchange capacity and CO2 conversion rates remarks the employed sequential H2/CO2 cycles as an effective methodology for screening the catalytic performance of Cu catalysts for RWGS reaction.}, language = {en} } @misc{MahmoodGonzalezCastanoPenkovaetal., author = {Mahmood, Safdar and Gonz{\´a}lez-Casta{\~n}o, Miriam and Penkova, Anna and Centeno, Miguel Angel and Odriozola, Jos{\´e} Antonio and Arellano-Garc{\´i}a, Harvey}, title = {CO2 methanation on Ni/YMn1-xAlxO3 perovskite catalysts}, series = {Applied Materials Today}, volume = {29}, journal = {Applied Materials Today}, issn = {2352-9407}, doi = {10.1016/j.apmt.2022.101577}, pages = {1 -- 11}, abstract = {Seeking for advanced catalytic systems for the CO2 methanation reaction, the use of Ni supported catalysts over redox materials is often proposed. Profiting the superior redox properties described for layered perovskite systems, this work has investigated a series Ni supported YMn1-xAlxO3 (x = 0, 0.2, 0.5, 0.8, 1) perovskite catalysts. The obtained results evidenced the impact of the support nature on the systems redox properties and Ni-support interactions. Within the catalysts series, the greater methanation rates displayed by Ni/YMn0.5Al0.5O3 catalyst (0.748 mmolCO2,conv.s-1 gNi -1 at 400 ◦C and 60 L/gh) were associated to the interplay between the support redox properties and superior Ni dispersion. The improved redox behavior attained through the Al-incorporation (up to x = 0.5) was associated to the layered perovskite structures which, being distorted and constituted by smaller crystal sizes, facilitated the behavior of Mn redox couples as surface species readily interconverted. Exhibiting catalytic performances comparable to precious metals based catalysts, this work proposes the Ni/YMn0.5Al0.5O3 catalyst as an effective system for the CO2 methanation reaction.}, language = {en} } @misc{FischerMarchettiDeschmannAssisetal., author = {Fischer, Thomas and Marchetti-Deschmann, Martina and Assis, Ana Cristina and Elad, Michal Levin and Algarra, Manuel and Barac, Marko and Bogdanovic Radovic, Iva and Cicconi, Flavio and Claes, Britt and Frascione, Nunzianda and George, Sony and Guedes, Alexandra and Heaton, Cameron and Heeren, Ron and Lasic, Violeta and Lerma, Jos{\´e} Luis and Valle Martinez de Yuso Garcia, Maria del and Nosko, Martin and O'Hara, John and Oshina, Ilze and Palucci, Antonio and Pawlaczyk, Aleksandra and Posp{\´i}škov{\´a}, Krist{\´y}na and de Puit, Marcel and Radodic, Ksenija and Rēpele, Māra and Ristova, Mimoza and Romolo, Francesco Saverio and Šafař{\´i}k, Ivo and Siketic, Zdravko and Spigulis, Janis and Szynkowska-Jozwik, Malgorzata Iwona and Tsiatsiuyeu, Andrei and Vella, Joanna and Dawson, Lorna and R{\"o}diger, Stefan and Francese, Simona}, title = {Profiling and imaging of forensic evidence - A pan-European forensic round robin study part 1: Document forgery}, series = {Science \& Justice}, volume = {62}, journal = {Science \& Justice}, number = {4}, issn = {1876-4452}, doi = {10.1016/j.scijus.2022.06.001}, pages = {433 -- 447}, language = {en} } @misc{GonzalezCastanoBaenaMorenoNavarrodeMigueletal., author = {Gonz{\´a}lez-Casta{\~n}o, Miriam and Baena-Moreno, Francisco Manuel and Navarro de Miguel, Juan Carlos and Miah, Kamal Uddin Mohammad and Arroyo-Torralvo, F{\´a}tima and Ossenbrink, Ralf and Odriozola, Jos{\´e} Antonio and Benzinger, Walther and Hensel, Andreas and Wenka, Achim and Arellano-Garc{\´i}a, Harvey}, title = {3D-printed structured catalysts for CO2 methanation reaction: Advancing of gyroid-based geometries}, series = {Energy Conversion and Management}, volume = {258}, journal = {Energy Conversion and Management}, issn = {2590-1745}, doi = {10.1016/j.enconman.2022.115464}, pages = {8}, abstract = {This work investigates the CO2 methanation rate of structured catalysts by tuning the geometry of 3D-printed metal Fluid Guiding Elements (FGEs) structures based on periodically variable pseudo-gyroid geometries. The enhanced performance showed by the structured catalytic systems is mostly associated with the capability of the FGEs substrate geometries for efficient heat usages. Thus, variations on the channels diameter resulted in ca. 25\% greater CO2 conversions values at intermediate temperature ranges. The highest void fraction evidenced in the best performing catalyst (3D-1) favored the radial heat transfer and resulted in significantly enhanced catalytic activity, achieving close to equilibrium (75\%) conversions at 400 ◦C and 120 mL/min. For the 3D-1 catalyst, a mathematical model based on an experimental design was developed thus enabling the estimation of its behavior as a function of temperature, spatial velocity, hydrogen to carbon dioxide (H2/CO2) ratio, and inlet CO2 concentration. Its optimal operating conditions were established under 3 different scenarios: 1) no restrictions, 2) minimum H2:CO2 ratios, and 3) minimum temperatures and H2/CO2 ratio. For instance, for the lattest scenario, the best CO2 methanation conditions require operating at 431 ◦C, 200 mL/min, H2/CO2 = 3 M ratio, and inlet CO2 concentration = 10 \%.}, language = {en} } @book{OdriozolaRamirezReinaArellanoGarcia, author = {Odriozola, Jos{\´e} Antonio and Ramirez Reina, Tomas and Arellano-Garc{\´i}a, Harvey}, title = {Engineering Solutions for CO2 Conversion}, publisher = {Wiley-VCH}, address = {Berlin ; Boston}, isbn = {978-3-527-34639-4}, pages = {496}, abstract = {A comprehensive guide that offers a review of the current technologies that tackle CO2 emissionsThe race to reduce CO2 emissions continues to be an urgent global challenge. "Engineering Solutions for CO2 Conversion" offers a thorough guide to the most current technologies designed to mitigate CO2 emissions ranging from CO2 capture to CO2 utilization approaches....}, language = {en} } @misc{GonzalezCastanoGonzalezAriasBobadillaetal., author = {Gonzalez-Casta{\~n}o, Miriam and Gonzalez-Arias, Judith and Bobadilla, Luis F. and Ruiz-Lopez, E. and Odriozola, Jose Antonio and Arellano-Garc{\´i}a, Harvey}, title = {In-Situ Drifts Steady-State Study of Co2 and Co Methanation Over Ni-Promoted Catalysts}, series = {Fuel}, volume = {338}, journal = {Fuel}, issn = {1873-7153}, doi = {10.1016/j.fuel.2022.127241}, abstract = {Promoting the performance of catalytic systems by incorporating small amount of alkali has been proved effective for several reactions whilst controversial outcomes are reported for the synthetic natural gas production. This work studies a series of Ni catalysts for CO2 and CO methanation reactions. In-situ DRIFTS spectroscopy evidenced similar reaction intermediates for all evaluated systems and it is proposed a reaction mechanism based on: i) formate decomposition and ii) hydrogenation of lineal carbonyl species to methane. Compared to bare Ni, the enhanced CO2 methanation rates attained by NiFe/Al and NiFeK/Al systems are associated to promoted formates decomposition into lineal carbonyl species. Also for CO methanation, the differences in the catalysts' performances were associated to the relative concentration of lineal carbonyl species. Under CO methanation conditions and opposing the CO2 methanation results where the incorporation of K delivered promoted catalytic behaviours, worsened CO methanation rates were discerned for the NiFeK/Al system.}, language = {en} } @misc{TarifaGonzalezCastanoCazanaetal., author = {Tarifa, Pilar and Gonzalez-Castano, Miriam and Cazana, Fernando and Monzon, Antonio and Arellano-Garc{\´i}a, Harvey}, title = {Hydrophobic RWGS catalysts: valorization of CO2-rich streams in presence of CO/H2O}, series = {Catalysis Today}, volume = {Vol. 423}, journal = {Catalysis Today}, issn = {1873-4308}, doi = {10.1016/j.cattod.2023.114276}, abstract = {Nowadays, the majority of the Reverse Water Gas Shift (RWGS) studies assume somehow model feedstock (diluted CO2/H2) for syngas production. Nonetheless, biogas streams contain certain amounts of CO/H2O which will decrease the obtained CO2 conversion values by promoting the forward WGS reaction. Since the rate limiting step for the WGS reaction concerns the water splitting, this work proposes the use of hydrophobic RWGS catalysts as an effective strategy for the valorization of CO2-rich feedstock in presence of H2O and CO. Over Fe-Mg catalysts, the different hydrophilicities attained over pristine, N- and B-doped carbonaceous supports accounted for the impact on the activity of the catalyst in presence of CO/H2O. Overall, the higher CO productivity (4.12 μmol/(min·m2)) attained by Fe-Mg/CDC in presence of 20\% of H2O relates to hindered water adsorption and unveil the use of hydrophobic surfaces as a suitable approach for avoiding costly pre-conditioning units for the valorization of CO2-rich streams based on RWGS processes in presence of CO/H2O.}, language = {en} } @incollection{GonzalezCastanoTarifaMonzonetal., author = {Gonz{\´a}lez-Casta{\~n}o, Miriam and Tarifa, Pilar and Monzon, Antonio and Arellano-Garc{\´i}a, Harvey}, title = {Valorization of unconventional CO2-rich feedstock via Reverse Water Gas Shift reaction}, series = {Circular Economy Processes for CO2 Capture and Utilization : Strategies and Case Studies}, booktitle = {Circular Economy Processes for CO2 Capture and Utilization : Strategies and Case Studies}, publisher = {Woodhead Publishing}, isbn = {9780323956697}, doi = {10.1016/B978-0-323-95668-0.00001-1}, pages = {307 -- 323}, abstract = {The implementation of novel CO2 valorization technologies is one of the most promising approaches towards the achievement of sustainable energy models. This chapter highlights the importance of carbon capture and utilization technologies and proposes novel approaches for the valorization of CO2-rich feedstock derived from thermochemical biomass conversion through the production of syngas mixtures via the Reverse Water Gas Shift reaction. After, this classification of the different types of nonconventional gases and biomass-treatment processes, we have also revised the fundamentals of the Reverse Water Gas Shift reaction and the impact of species commonly present in CO2-rich streams on the performance of the catalytic systems are also reviewed. Finally, a catalytic bi-functionalization approach that ensures larger CO productivity from simulated biomass-derived CO2-rich feedstock is demonstrated.}, language = {en} }