@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{GonzalezCastanoGonzalezAriasSanchezetal., author = {Gonz{\´a}lez-Casta{\~n}o, Miriam and Gonz{\´a}lez-Arias, Judith and S{\´a}nchez, Marta Elena and Cara-Jim{\´e}nez, Jorge and Arellano-Garc{\´i}a, Harvey}, title = {Syngas production using CO2-rich residues: From ideal to real operating conditions}, series = {Journal of CO2 utilization}, volume = {52}, journal = {Journal of CO2 utilization}, issn = {2212-9839}, doi = {10.1016/j.jcou.2021.101661}, pages = {10}, language = {en} } @misc{GonzalezAriasGonzalezCastanoSanchezetal., author = {Gonz{\´a}lez-Arias, Judith and Gonz{\´a}lez-Casta{\~n}o, Miriam and S{\´a}nchez, Marta Elena and Cara-Jim{\´e}nez, Jorge and Arellano-Garc{\´i}a, Harvey}, title = {Valorization of biomass-derived CO2 residues with Cu-MnOx catalysts for RWGS reaction}, series = {Renewable Energy}, journal = {Renewable Energy}, number = {182}, issn = {1879-0682}, doi = {10.1016/j.renene.2021.10.029}, pages = {443 -- 451}, abstract = {This study delivers useful understanding towards the design of effective catalytic systems for upgrading real CO2erich residual streams derived from biomass valorization. Within this perspective, a catalysts' series based on (5 wt\%) Cu - (X wt\%) Mn/Al2O3with X¼0, 3, 8, and 10 is employed. The improved catalyst performance achieved through Mn incorporation is ascribed to enhanced Cu dispersions and promoted surface basic concentrations. Under standard RWGS conditions, the highest reaction rates achieved by(5 wt\%) Cu - (8 wt\%) Mn/Al2O3catalyst were associated to improved Cu dispersions along with the constitution of highly active Cu-MnOxdomains. Remarkably, variations on the optimal Cu to Mn ratios were detected as a function of the RWGS reaction conditions. Thus, under simulated CO2-rich residual feedstock's, i.e., in presence of CO and CH4, the further promotion on the Cu dispersion attained by the larger amounts of MnOxrendered the (5 wt\%) Cu - (10 wt\%) Mn/Al2O3catalyst as the best performing sample. Overall, the presented outcomes underline operative strategies for developing catalytic systems with advanced implementation potentialities.}, language = {en} } @misc{GonzalezCastanoNavarrodeMiguelBoelteetal., author = {Gonzalez-Castano, Miriam and Navarro de Miguel, Juan Carlos and Boelte, Jens-H. and Centeno, Miguel Angel and Klepel, Olaf and Arellano-Garc{\´i}a, Harvey}, title = {Assessing the impact of textural properties in Ni-Fe catalysts for CO2 methanation performance}, series = {Microporous and Mesoporous Materials}, volume = {327}, journal = {Microporous and Mesoporous Materials}, issn = {1387-1811}, doi = {10.1016/j.micromeso.2021.111405}, pages = {7}, abstract = {In heterogeneous catalysis, the benefits of employing adequate textural properties on the catalytic performances are usually stated. Nevertheless, the quantification of the extent of improvement is not an easy task since variations on the catalysts' specific areas and pore structures might involve modifications on a number of other surface catalytic features. This study establishes the impact of the catalyst textural properties on the CO2 methanation performance by investigating bimetallic Ni-Fe catalysts supported over carbon supports with different textural properties regarding surface area and pore structure. The comparable metal loading and dispersions attained for all systems enabled establishing forthright relationships between the catalyst textural properties and CO2 methanation rate. Once the influence of the external mass diffusions on the catalysts' performance was experimentally discarded, the estimated Thiele modulus and internal effectiveness (φ and ηEff) values showed that the catalyst performance was majorly governed by the surface reaction rate whilst the pore size affected in no significant manner within the examined range (Dpore = 10.2 to 5.8 nm). Therefore, the rapport between the catalyst performance and surface area was quantified for the CO2 methanation reaction over Ni-Fe catalysts: increasing the surface area from 572 to 802 m2/g permit obtaining ca. 10\% higher CO2 conversions.}, language = {en} } @misc{GonzalezAriasGomezGonzalezCastanoetal., author = {Gonz{\´a}lez-Arias, Judith and Gomez, X. and Gonzalez-Castano, Miriam and Sanchez, Marta Elena and Rosas, J. G. and Cara-Jim{\´e}nez, Jorge}, title = {Insights into the product quality and energy requirements for solid biofuel production: A comparison of hydrothermal carbonization, pyrolysis and torrefaction of olive tree pruning}, series = {Energy}, volume = {Vol. 238, part C (2022)}, journal = {Energy}, issn = {0360-5442}, doi = {10.1016/j.energy.2021.122022}, pages = {12}, abstract = {For a bio-economy establishment, understanding the energy consumption needs to produce solid biofuels is a key point. Herein, olive tree pruning was treated by both dry (pyrolysis and torrefaction) and wet (hydrothermal carbonization) thermal treatments. Product yield, solid quality and energy consumption were assessed. The solids were characterized by means of chemical and thermogravimetric analysis. For all treatments, coal-like solid products were obtained, with higher heating values (HHV) of almost 30 MJ kg-1 in most of the conditions evaluated. Chars from pyrolysis presented the greater carbon content (between 76 and 85 wt\%) but also the higher ash content (ranging from 6 to 9 wt\%). From an energy consumption perspective, torrefaction registered the lowest energy consumption (between 5.85 and 20.76 MJ kg-1 char). The highest energy contents per kilogram of char produced were also reflected in torrefaction samples, with values around 11 MJ kg-1 char. Although the obtained HHVs were greater for pyrolysis chars the higher mass yields obtained in torrefaction makes it more profitable. The least severe conditions allowed to obtain a positive energy balance only with the solid phase considered. Nonetheless, further room for improvement is possible since the gas and liquid phases may also be valorised.}, language = {en} } @misc{GonzalezCastanoHaniKourGonzalezAriasetal., author = {Gonz{\´a}lez-Casta{\~n}o, Miriam and Hani Kour, M. and Gonz{\´a}lez-Arias, Judith and Baena-Moreno, Francisco Manuel and Arellano-Garc{\´i}a, Harvey}, title = {Promoting bioeconomy routes: From food waste to green biomethane. A profitability analysis based on a real case study in eastern Germany}, series = {Journal of Environmental Management}, volume = {300}, journal = {Journal of Environmental Management}, issn = {0301-4797}, doi = {10.1016/j.jenvman.2021.113788}, abstract = {Profitability studies are needed to establish the potential pathways required for viable biomethane production in the Brandenburg region of Germany. This work study the profitability of a potential biomethane production plant in the eastern German region of Brandenburg, through a specific practical scenario with data collected from a regional biogas plant located in Alteno (Schradenbiogas GmbH \& Co. KG). Several parameters with potential economic influence such as distance of the production point to the grid, waste utilization percentage, and investment, were analyzed. The results illustrate a negative overall net present value with the scenario of no governmental investment, even when considering trading the CO2 obtained throughout the process. Subsidies needed to reach profitability varied with distance from 13.5 €/MWh to 19.3 €/MWh. For a fixed distance of 15 kms, the importance of percentage of waste utilization was examined. Only 100\% of waste utilization and 75\% of waste utilization would reach profitability under a reasonable subsidies scheme (16.3 and 18.8 €/MWh respectively). Concerning the importance of investment, a subsidized investment of at least 70\% is demanded for positive net present values. Besides, the sensitivity analysis remarks the energy consumption of the biogas upgrading stage, the electricity price, and the energy consumption of biogas production as major parameters to be tackled for the successful implementation of biogas upgrading plants. The results here obtained invite to ponder about potential strategies to further improve the economic viability of this kind of renewable projects. In this line, using the CO2 separated to produce added-value chemicals can be an interesting alternative.}, language = {en} } @misc{GonzalezAriasBaenaMorenoGonzalezCastanoetal., author = {Gonz{\´a}lez-Arias, Judith and Baena-Moreno, Francisco Manuel and Gonz{\´a}lez-Casta{\~n}o, Miriam and Arellano-Garc{\´i}a, Harvey}, title = {Economic approach for CO2 valorization from hydrothermal carbonization gaseous streams via reverse water-gas shift reaction}, series = {Fuel}, volume = {313}, journal = {Fuel}, issn = {0016-2361}, doi = {10.1016/j.fuel.2021.123055}, pages = {1 -- 7}, abstract = {In this work the economic performance of valorizing the gaseous stream coming from hydrothermal carbonization (HTC) of olive tree pruning is presented as a novel strategy to improve the competitiveness of HTC. The valorization of the commonly disregarded gaseous stream produced in this thermochemical treatment was proposed via the Reverse Water-Gas Shift reaction. This allows to obtain syngas for selling and therefore improving the overall economic performance of the process. To this end, three plant sizes were selected (312.5, 625 and 1250 kg/h of biomass processing). The parameters with a higher share in the total cost distribution along with the revenues from the hydrochar and the syngas selling were further evaluated. The results evidenced that with the assumptions taken, the overall process is still not profitable. To reach profitability, syngas selling prices between 2.2 and 3.4 €/m3 are needed, revealing that this proposal is not economically attractive. Alternatively, a lack of competitiveness in the current market is revealed with hydrochar selling prices between 0.41 and 0.64 €/kg to make the project profitable. The catalyst cost, sharing approximately 20\% of the total cost, is the parameter with the highest impact in the total economics of the process. The second one is the hydrogen price production, representing almost 16\% of the total. Investment subsidies are also examined as a potential tool to cover part of the initial investment. These results evidenced that further efforts and measures are needed to push forward in the path towards circular economy societies.}, 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{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} } @misc{MedinaMendezGonzalezCastanoBaenaMorenoetal., author = {Medina M{\´e}ndez, Juan Ali and Gonz{\´a}lez-Casta{\~n}o, Miriam and Baena-Moreno, Francisco Manuel and Arellano-Garc{\´i}a, Harvey}, title = {CO2 methanation: on the modeling of reacting laminar flows in structured Ni/MgAl2O4 catalysts}, series = {XXV Fluid Mechanics Conference, Rzesz{\´o}w, Poland, 7-9 September 2022, Book of Abstracts}, journal = {XXV Fluid Mechanics Conference, Rzesz{\´o}w, Poland, 7-9 September 2022, Book of Abstracts}, editor = {Kmiotek, M. and Kordos, A.}, publisher = {Publishing House of Rzesz{\´o}w University of Technology}, address = {Rzesz{\´o}w, Poland}, isbn = {978-83-7934-590-8}, pages = {98 -- 100}, language = {en} } @misc{MedinaMendezGonzalezCastanoBaenaMorenoetal., author = {Medina M{\´e}ndez, Juan Ali and Gonz{\´a}lez-Casta{\~n}o, Miriam and Baena-Moreno, Francisco Manuel and Arellano-Garc{\´i}a, Harvey}, title = {CO2 methanation: on the modeling of reacting laminar flows in structured Ni/MgAl2O4 catalysts}, series = {Journal of Physics: Conference Series}, journal = {Journal of Physics: Conference Series}, number = {2367}, publisher = {IOP Publishing}, doi = {10.1088/1742-6596/2367/1/012015}, pages = {8}, language = {en} } @misc{MiahKloshekGonzalezCastanoetal., author = {Miah, Kamal Uddin Mohammad and Kloshek, Alexander and Gonz{\´a}lez-Casta{\~n}o, Miriam and Kehm, Christian and Ossenbrink, Ralf and Michailov, Vesselin}, title = {Herstellen hocheffektiver Mikroreaktoren durch selektives Laserstrahlschmelzen}, series = {DVS Congress 2022, Große Schweißtechnische Tagung, DVS Campus ; Kurzfassungen der Vortr{\"a}ge der Veranstaltung in Koblenz vom 19. bis 21. September 2022 ; (Langfassungen der Beitr{\"a}ge auf USB-Karte)}, journal = {DVS Congress 2022, Große Schweißtechnische Tagung, DVS Campus ; Kurzfassungen der Vortr{\"a}ge der Veranstaltung in Koblenz vom 19. bis 21. September 2022 ; (Langfassungen der Beitr{\"a}ge auf USB-Karte)}, publisher = {DVS Media GmbH}, address = {D{\"u}sseldorf}, isbn = {978-3-96144-189-1}, pages = {708 -- 713}, abstract = {Das pulverbasierte 3D-Metalldrucken erm{\"o}glicht die Fertigung von hochkomplexen Integralbauteilen, die als Tr{\"a}gerstruktur f{\"u}r Mikroreaktoren benutzt werden. Nach einer Beschichtung der Struktur mit einem Katalysatormaterial, k{\"o}nnen diese Mikroreaktoren h{\"o}chst effizient f{\"u}r die CO2-Methanisierung eingesetzt werden. Durch die additive Fertigung mit dem selektiven Laserstrahlschmelzen (SLM) wurden adaptierte dreidimensionale periodische Gitterstrukturen mit sehr geringen Wandst{\"a}rken hergestellt. Diese weisen ein sehr g{\"u}nstiges Verh{\"a}ltnis von Oberfl{\"a}che zu Volumen (TPMS - Triply periodic minimal surface) auf. Des Weiteren zeigen die TPMS-Strukturen vorteilhafte Str{\"o}mungseigenschaften, die sowohl f{\"u}r die Beschichtung mit dem Katalysator-Material als auch die Durchstr{\"o}mung mit den Reaktionsmedien im Betrieb essentiell sind. So ist es beispielsweise m{\"o}glich, durch die Variation der Dimension einer TPMS-Struktur die Oberfl{\"a}che pro Volumeneinheit, den hydraulischen Durchmesser des Reaktors und somit auch den Transportprozess des Fluids deutlich zu verbessern. Diese Faktoren erm{\"o}glichen eine effektivere Gas-Katalysator-Reaktion. Im Vergleich zu Mikroreaktorstrukturen aus den traditionellen Herstellungsverfahren liefern die additiv gefertigten Strukturen sowohl eine h{\"o}here CO2-Umwandlungsrate als auch eine CH4-Selektivit{\"a}t innerhalb des diffusionskontrollierten Bereichs.}, language = {de} } @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{TarifaRamirezReinaGonzalezCastanoetal., author = {Tarifa, Pilar and Ramirez Reina, Tomas and Gonz{\´a}lez-Casta{\~n}o, Miriam and Arellano-Garc{\´i}a, Harvey}, title = {Catalytic Upgrading of Biomass-Gasification Mixtures Using Ni-Fe/MgAl₂O₄ as a Bifunctional Catalyst}, series = {Energy and Fuels}, volume = {36}, journal = {Energy and Fuels}, number = {15}, issn = {1520-5029}, doi = {10.1021/acs.energyfuels.2c01452}, pages = {8267 -- 8273}, abstract = {Biomass gasification streams typically contain a mixture of CO, H2, CH4, and CO2 as the majority components and frequently require conditioning for downstream processes. Herein, we investigate the catalytic upgrading of surrogate biomass gasifiers through the generation of syngas. Seeking a bifunctional system capable of converting CO2 and CH4 to CO, a reverse water gas shift (RWGS) catalyst based on Fe/MgAl2O4 was decorated with an increasing content of Ni metal and evaluated for producing syngas using different feedstock compositions. This approach proved efficient for gas upgrading, and the incorporation of adequate Ni content increased the CO content by promoting the RWGS and dry reforming of methane (DRM) reactions. The larger CO productivity attained at high temperatures was intimately associated with the generation of FeNi3 alloys. Among the catalysts' series, Ni-rich catalysts favored the CO productivity in the presence of CH4, but important carbon deposition processes were noticed. On the contrary, 2Ni-Fe/MgAl2O4 resulted in a competitive and cost-effective system delivering large amounts of CO with almost no coke deposits. Overall, the incorporation of a suitable realistic application for valorization of variable composition of biomass-gasification derived mixtures obtaining a syngas-rich stream thus opens new routes for biosyngas production and upgrading.}, language = {en} } @misc{BobadillaAzancotLuqueAlvarezetal., author = {Bobadilla, Luis F. and Azancot, Lola and Luque-Alvarez, Ligia A. and Torres-Sempere, Guillermo and Gonzalez-Castano, Miriam and Pastor-Perez, Laura and Yu, Jie and Ramirez Reina, Tomas and Ivanova, Svetlana and Centeno, Miguel Angel and Odriozola, Jos{\´e} Antonio}, title = {Development of Power-to-X Catalytic Processes for CO2 Valorisation: From the Molecular Level to the Reactor Architecture}, series = {Chemistry}, volume = {4}, journal = {Chemistry}, number = {4}, issn = {2624-8549}, doi = {10.3390/chemistry4040083}, pages = {1250 -- 1280}, abstract = {Nowadays, global climate change is likely the most compelling problem mankind is facing. In this scenario, decarbonisation of the chemical industry is one of the global challenges that the scientific community needs to address in the immediate future. Catalysis and catalytic processes are called to play a decisive role in the transition to a more sustainable and low-carbon future. This critical review analyses the unique advantages of structured reactors (isothermicity, a wide range of residence times availability, complex geometries) with the multifunctional design of efficient catalysts to synthesise chemicals using CO2 and renewable H2 in a Power-to-X (PTX) strategy. Fine-chemistry synthetic methods and advanced in situ/operando techniques are essential to elucidate the changes of the catalysts during the studied reaction, thus gathering fundamental information about the active species and reaction mechanisms. Such information becomes crucial to refine the catalyst's formulation and boost the reaction's performance. On the other hand, reactors architecture allows flow pattern and temperature control, the management of strong thermal effects and the incorporation of specifically designed materials as catalytically active phases are expected to significantly contribute to the advance in the valorisation of CO2 in the form of high added-value products. From a general perspective, this paper aims to update the state of the art in Carbon Capture and Utilisation (CCU) and PTX concepts with emphasis on processes involving the transformation of CO2 into targeted fuels and platform chemicals, combining innovation from the point of view of both structured reactor design and multifunctional catalysts development.}, language = {en} } @misc{GonzalezAriasGonzalezCastanoArellanoGarcia, author = {Gonzalez-Arias, Judith and Gonzalez-Castano, Miriam and Arellano-Garc{\´i}a, Harvey}, title = {Utilization of CO2-Rich Residues for Syngas Production: Strategies for Catalyst Design}, series = {AIChE Annual Meeting, November 15, 2021}, journal = {AIChE Annual Meeting, November 15, 2021}, isbn = {978-0-8169-1116-5}, abstract = {Compared to a Reverse Water Gas Shift (RWGS) process carried out under ideal conditions, the valorization of CO2-rich residues involve additional challenges. Indeed, for an ideal RWGS reaction unit, the CO2 methanation reaction and the constitution of carbon deposits via Boudouard reaction are the main side reactions to take into consideration. For CO2-rich residues derived from biomass treatment and heavy metal industries, the presence of CH4 and CO species (among others) constitute an, although often disregarded, much complex panorama where side reactions like CO methanation, dry reforming of methane, the forward Water Gas Shift reaction and the decomposition of CO and CH4 resulting in carbon deposits, are occurring to some extent within the catalytic reactor. This work aimed at designing advanced catalytic systems capable of converting the CO2/CO/CH4 feedstocks into syngas mixtures. Thus, with the RWGS reaction considered as the major process, this work focusses on the side reactions involving CO/CH4 species. In this context, a series Cu-MnOx/Al2O3 spinel derived catalysts were optimized for syngas production in presence of CO and CH4 fractions. Once the optimal active phase was determined, the optimal Cu contents and the impact of the support nature (Al2O3, SiO2-Al2O3 and CeO2-Al2O3) was evaluated for the valorization of realistic CO2-rich feedstocks. Remarkably, the obtained outcomes underline operative strategies for developing catalytic systems with advanced implementation potential. For that aim, the catalyst design should present, along with an active and selective phase for RWGS reaction, superior cooking resistances, activities towards methane reforming and low tendencies towards the forward WGS reaction. Further developments should tackle difficult tasks like improving the RWGS reaction rate while inhibiting the forwards WGS reaction as well as improving the CH4 conversion to CO without affecting the process selectivity. Strategies towards advancing catalytic systems capable of operating under variable conditions also arise as appealing routes.}, 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} } @misc{GonzalezAriasTorresSempereGonzalezCastanoetal., author = {Gonzalez-Arias, Judith and Torres-Sempere, Guillermo and Gonzalez-Castano, Miriam and Baena-Moreno, Francisco Manuel and Ramirez Reina, Tomas}, title = {Hydrochar and synthetic natural gas co-production for a full circular economy implementation via hydrothermal carbonization and methanation: An economic approach}, series = {Journal of Environmental Sciences}, volume = {Vol. 140(2024)}, journal = {Journal of Environmental Sciences}, issn = {1878-7320}, doi = {10.1016/j.jes.2023.04.019}, pages = {69 -- 78}, abstract = {Herein we study the economic performance of hydrochar and synthetic natural gas co-production from olive tree pruning. The process entails a combination of hydrothermal carbonization and methanation. In a previous work, we evidenced that standalone hydrochar production via HTC results unprofitable. Hence, we propose a step forward on the process design by implementing a methanation, adding value to the gas effluent in an attempt to boost the overall process techno-economic aspects. Three different plant capacities were analyzed (312.5, 625 and 1250 kg/hr). The baseline scenarios showed that, under the current circumstances, our circular economy strategy in unprofitable. An analysis of the revenues shows that hydrochar selling price have a high impact on NPV and subsidies for renewable coal production could help to boost the profitability of the process. On the contrary, the analysis for natural gas prices reveals that prices 8 times higher than the current ones in Spain must be achieved to reach profitability. This seems unlikely even under the presence of a strong subsidy scheme. The costs analysis suggests that a remarkable electricity cost reduction or electricity consumption of the HTC stage could be a potential strategy to reach profitability scenarios. Furthermore, significant reduction of green hydrogen production costs is deemed instrumental to improve the economic performance of the process. These results show the formidable techno-economic challenge that our society faces in the path towards circular economy societies.}, language = {en} } @misc{JafariSafdarDorneanuetal., author = {Jafari, Mitra and Safdar, Muddasar and Dorneanu, Bogdan and Gonzalez-Casta{\~n}o, Miriam and Arellano-Garc{\´i}a, Harvey}, title = {Green and sustainable fuel from syngas via the Fischer-Tropsch synthesis process: Bifunctional cobalt-based catalysts}, series = {14th European Congress of Chemical Engineering and 7th European Congress of Applied Biotechnology}, journal = {14th European Congress of Chemical Engineering and 7th European Congress of Applied Biotechnology}, abstract = {This paper reviews and compares state-of-the-art cobalt-based catalysts and catalytic systems used to produce green and sustainable fuels using FTS. Being focused on comparing the effect of the catalyst formulation and synthesis method, the reactor type and operating parameters, as well as the quality of the obtained fuels, the aim is to identify the research gaps between these relevant research areas concerning production of green and sustainable fuels.}, language = {en} } @misc{GonzalezCastanoMoralesNavarrodeMigueletal., author = {Gonzalez-Cast{\~a}no, Miriam and Morales, Carlos and Navarro de Miguel, Juan Carlos and Boelte, Jens-H. and Klepel, Olaf and Flege, Jan Ingo and Arellano-Garc{\´i}a, Harvey}, title = {Are Ni/ and Ni5Fe1/biochar catalysts suitable for synthetic natural gas production? A comparison with γ-Al2O3 supported catalysts}, series = {Green Energy \& Environment}, volume = {8}, journal = {Green Energy \& Environment}, number = {3}, issn = {2468-0257}, doi = {10.1016/j.gee.2021.05.007}, pages = {744 -- 756}, abstract = {Among challenges implicit in the transition to the post-fossil fuel energetic model, the finite amount of resources available for the technological implementation of CO2 revalorizing processes arises as a central issue. The development of fully renewable catalytic systems with easier metal recovery strategies would promote the viability and sustainability of synthetic natural gas production circular routes. Taking Ni and NiFe catalysts supported over γ-Al2O3 oxide as reference materials, this work evaluates the potentiality of Ni and NiFe supported biochar catalysts for CO2 methanation. The development of competitive biochar catalysts was found dependent on the creation of basic sites on the catalyst surface. Displaying lower Turn Over Frequencies than Ni/Al catalyst, the absence of basic sites achieved over Ni/C catalyst was related to the depleted catalyst performances. For NiFe catalysts, analogous Ni5Fe1 alloys were constituted over both alumina and biochar supports. The highest specific activity of the catalyst series, exhibited by the NiFe/C catalyst, was related to the development of surface basic sites along with weaker NiFe-C interactions, which resulted in increased Ni0:NiO surface populations under reaction conditions. In summary, the present work establishes biochar supports as a competitive material to consider within the future low-carbon energetic panorama.}, 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} }