Literatura académica sobre el tema "Carbon dioxide methanation"
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Artículos de revistas sobre el tema "Carbon dioxide methanation"
Hutchings, G. J. "Methanation of carbon dioxide". Applied Catalysis A: General 84, n.º 2 (mayo de 1992): N18. http://dx.doi.org/10.1016/0926-860x(92)80119-w.
Texto completoTsiotsias, Anastasios I., Nikolaos D. Charisiou, Ioannis V. Yentekakis y Maria A. Goula. "The Role of Alkali and Alkaline Earth Metals in the CO2 Methanation Reaction and the Combined Capture and Methanation of CO2". Catalysts 10, n.º 7 (21 de julio de 2020): 812. http://dx.doi.org/10.3390/catal10070812.
Texto completoZhou, Long, Li Ping Ma, Ze Cheng Zi, Jun Ma y Jian Tao Chen. "Study on Ni Catalytic Hydrogenation of Carbon Dioxide for Methane". Applied Mechanics and Materials 628 (septiembre de 2014): 16–19. http://dx.doi.org/10.4028/www.scientific.net/amm.628.16.
Texto completoBurkhardt, Marko y Günter Busch. "Methanation of hydrogen and carbon dioxide". Applied Energy 111 (noviembre de 2013): 74–79. http://dx.doi.org/10.1016/j.apenergy.2013.04.080.
Texto completoWei, Wang y Gong Jinlong. "Methanation of carbon dioxide: an overview". Frontiers of Chemical Science and Engineering 5, n.º 1 (28 de diciembre de 2010): 2–10. http://dx.doi.org/10.1007/s11705-010-0528-3.
Texto completoLach, Daniel, Jaroslaw Polanski y Maciej Kapkowski. "CO2—A Crisis or Novel Functionalization Opportunity?" Energies 15, n.º 5 (22 de febrero de 2022): 1617. http://dx.doi.org/10.3390/en15051617.
Texto completoDARENSBOURG,, DONALD J., CHRISTOPHERG BAUCH, y CESAR OVALLES,. "MECHANISTIC ASPECTS OF CATALYTIC CARBON DIOXIDE METHANATION". Reviews in Inorganic Chemistry 7, n.º 4 (octubre de 1985): 315–40. http://dx.doi.org/10.1515/revic.1985.7.4.315.
Texto completoAndo, Hisanori, Masahiro Fujiwara, Yasuyuki Matsumura, Hiroshi Miyamura y Yoshie Souma. "Methanation of carbon dioxide over LaNi4X type catalysts". Energy Conversion and Management 36, n.º 6-9 (junio de 1995): 653–56. http://dx.doi.org/10.1016/0196-8904(95)00090-z.
Texto completoAndo, H. "Methanation of carbon dioxide over LaNi4X type catalysts". Fuel and Energy Abstracts 37, n.º 3 (mayo de 1996): 182. http://dx.doi.org/10.1016/0140-6701(96)88531-6.
Texto completoDias, Yan Resing y Oscar W. Perez-Lopez. "Carbon dioxide methanation over Ni-Cu/SiO2 catalysts". Energy Conversion and Management 203 (enero de 2020): 112214. http://dx.doi.org/10.1016/j.enconman.2019.112214.
Texto completoTesis sobre el tema "Carbon dioxide methanation"
Alarcón, Avellán Andreina. "Catalyst and reactor design for carbon dioxide methanation". Doctoral thesis, Universitat de Barcelona, 2021. http://hdl.handle.net/10803/671781.
Texto completoPower-to-Gas (P2G) es una tecnología prometedora para el almacenamiento de combustibles bajos en carbono. El concepto P2G implica la conversión de energía renovable en hidrógeno mediante electrólisis con la posibilidad de combinarlo con CO2 para producir metano (gas natural sintético, SNG). La producción de SNG mediante el proceso termoquímico de metanación de CO2 es particularmente interesante porque ofrece un combustible fácilmente transportable con un amplio mercado probado para aplicaciones de uso final de energía, calor y movilidad. Sin embargo, el desarrollo de una tecnología de metanación de CO2 rentable es uno de los mayores desafíos que enfrenta el concepto P2G. En este contexto, esta tesis se centró en el desarrollo de un catalizador y un reactor para la metanación de CO2. Los objetivos de la tesis se abordaron en tres aspectos principales, que son: i) diseñar un catalizador de alto rendimiento basado en Ni/The transformation of the current energy model towards a more sustainable mix, independent of fossil fuels, requires the exploration of new technologies that are capable of taking advantage of excess electricity derived from renewable energy sources and to use new alternative sources of carbon for the generation of clean fuels. An alternative that combines both is the Power-to-Gas (P2G) technology, whose concept is based on a two-stage process. In the first stage, excess electricity from renewable energies is converted to hydrogen by electrolysis. Then, in a second stage, the H2 produced is transformed to CH4 through methanation with CO2. The CH4 produced is referred to as synthetic natural gas (SNG) and allows large amounts of renewable energy to be distributed from the energy sector to the end-use sectors. The thermo-chemical CO2 methanation process is considered the most efficient route for large-scale SNG production. However, developing a cost-effective CO2 methanation technology is one of the biggest challenges facing the P2G concept. In this context, this thesis focused on the catalyst and reactor design for CO2 methanation. The thesis objectives were addressed in three main aspects, which are: i) design a high-performance catalyst based on metal oxide-promoted Ni/γ-Al2O3 and determine its reaction mechanism; ii) evaluate the stability of the catalyst and the tolerance to sulfur for its implementation in a relevant industrial environment (CoSin project); and finally, iii) develop a CFD model based on experimental kinetic data to understand the role of operating conditions and propose a new reactor configuration. In the first Chapter of this thesis it is presented a general introduction of the SNG production through CO2 methanation process. In the second Chapter, the addition of a promoter (X) on a system composed by Ni and γ-Al2O3 microspheres was studied as the design strategy to develop a micro-sized Ni-X/γ-Al2O3 catalyst. The catalysts based on Ni-CeO2/γ-Al2O3 was proposed as the most feasible due to its high catalytic performance in relation to its economic competitiveness. The optimal composition of each component of the Ni-CeO2/γ-Al2O3 was found through a systematic experimental design. The catalyst composed by 25wt.%Ni, 20wt.%CeO2 and 55wt.%γ-Al2O3 proved to be the most active and stable thanks to its enhanced Ni dispersion and reduction, its high metallic area, and the formation of moderate base sites. In Chapter three, the thermal stability and tolerance to sulfur impurities on the Ni-CeO2/γ-Al2O3 catalyst was further studied using high temperatures and the presence of H2S on the reactants. The strong metal-promoter interaction and the favourable formation of Ce2O2S were revealed as the main causes of its high stability and tolerance to H2S, respectively. Additionally, the implementation of Ni-CeO2/γ-Al2O3 in a two-stage industrial methanation process was performed to evaluate its technical feasibility. The desired gas composition (≥92.5%CH4) was successful obtained using a decreasing temperature profile (T=450-275°C) and P=5bar·g. The high stability recorded during the 2000h of experimentation demonstrated that Ni-CeO2/γ-Al2O3 can be a competitive catalyst for CO2 methanation. Regarding to reactor design, in Chapter four, the design of a fixed-bed multitubular reactor on a Ni-CeO2-Al2O3 catalyst was evaluated for mid-scale SNG production. A CFD mathematical model based on experimental kinetic data was developed. A reactor tube with a diameter of 9.25mm and a length of 250mm was proposed, which should be operated at Tinlet=473K, Twall=373K, GHSV=14,400h-1 and P=5atm to achieve XCO2=99% with Tmax of 673K. On the other hand, a reactor tube (di=4.6mm and L=250mm) with a heat management approach based on free convection was proposed for small-scale SNG production. The optimal conditions were found at GHSV=11,520h-1, Tinlet=503K, P=5atm, and Tair=298K. The feasibility of the simulated reactor proposal was experimentally validated over the micro-sized Ni-CeO2/γ-Al2O3 (XCO2=93% and T=830-495K).-Al2O3 promovido por óxido metálico y determinar su mecanismo, ii) evaluar la estabilidad del catalizador y la tolerancia al azufre para su implementación en un entorno industrial relevante (proyecto CoSin), and iii) desarrollar un modelo CFD basado en datos cinéticos experimentales para comprender el papel de las condiciones de operación y proponer una nueva configuración de reactor. En línea con estos objetivos, un catalizador ternario basado en 25wt.%Ni-20wt.%CeO2-55wt.%The transformation of the current energy model towards a more sustainable mix, independent of fossil fuels, requires the exploration of new technologies that are capable of taking advantage of excess electricity derived from renewable energy sources and to use new alternative sources of carbon for the generation of clean fuels. An alternative that combines both is the Power-to-Gas (P2G) technology, whose concept is based on a two-stage process. In the first stage, excess electricity from renewable energies is converted to hydrogen by electrolysis. Then, in a second stage, the H2 produced is transformed to CH4 through methanation with CO2. The CH4 produced is referred to as synthetic natural gas (SNG) and allows large amounts of renewable energy to be distributed from the energy sector to the end-use sectors. The thermo-chemical CO2 methanation process is considered the most efficient route for large-scale SNG production. However, developing a cost-effective CO2 methanation technology is one of the biggest challenges facing the P2G concept. In this context, this thesis focused on the catalyst and reactor design for CO2 methanation. The thesis objectives were addressed in three main aspects, which are: i) design a high-performance catalyst based on metal oxide-promoted Ni/γ-Al2O3 and determine its reaction mechanism; ii) evaluate the stability of the catalyst and the tolerance to sulfur for its implementation in a relevant industrial environment (CoSin project); and finally, iii) develop a CFD model based on experimental kinetic data to understand the role of operating conditions and propose a new reactor configuration. In the first Chapter of this thesis it is presented a general introduction of the SNG production through CO2 methanation process. In the second Chapter, the addition of a promoter (X) on a system composed by Ni and γ-Al2O3 microspheres was studied as the design strategy to develop a micro-sized Ni-X/γ-Al2O3 catalyst. The catalysts based on Ni-CeO2/γ-Al2O3 was proposed as the most feasible due to its high catalytic performance in relation to its economic competitiveness. The optimal composition of each component of the Ni-CeO2/γ-Al2O3 was found through a systematic experimental design. The catalyst composed by 25wt.%Ni, 20wt.%CeO2 and 55wt.%γ-Al2O3 proved to be the most active and stable thanks to its enhanced Ni dispersion and reduction, its high metallic area, and the formation of moderate base sites. In Chapter three, the thermal stability and tolerance to sulfur impurities on the Ni-CeO2/γ-Al2O3 catalyst was further studied using high temperatures and the presence of H2S on the reactants. The strong metal-promoter interaction and the favourable formation of Ce2O2S were revealed as the main causes of its high stability and tolerance to H2S, respectively. Additionally, the implementation of Ni-CeO2/γ-Al2O3 in a two-stage industrial methanation process was performed to evaluate its technical feasibility. The desired gas composition (≥92.5%CH4) was successful obtained using a decreasing temperature profile (T=450-275°C) and P=5bar·g. The high stability recorded during the 2000h of experimentation demonstrated that Ni-CeO2/γ-Al2O3 can be a competitive catalyst for CO2 methanation. Regarding to reactor design, in Chapter four, the design of a fixed-bed multitubular reactor on a Ni-CeO2-Al2O3 catalyst was evaluated for mid-scale SNG production. A CFD mathematical model based on experimental kinetic data was developed. A reactor tube with a diameter of 9.25mm and a length of 250mm was proposed, which should be operated at Tinlet=473K, Twall=373K, GHSV=14,400h-1 and P=5atm to achieve XCO2=99% with Tmax of 673K. On the other hand, a reactor tube (di=4.6mm and L=250mm) with a heat management approach based on free convection was proposed for small-scale SNG production. The optimal conditions were found at GHSV=11,520h-1, Tinlet=503K, P=5atm, and Tair=298K. The feasibility of the simulated reactor proposal was experimentally validated over the micro-sized Ni-CeO2/γ-Al2O3 (XCO2=93% and T=830-495K).-Al2O3 se propone como el más factible debido a su alto rendimiento catalítico en relación a su competitividad económica. La fuerte interacción metal-promotor y la formación favorable de Ce2O2S se revelaron como las principales causas de su alta estabilidad y tolerancia al H2S, respectivamente. Adicionalmente, su exitosa implementación en un proceso de metanación industrial de dos etapas demostró su viabilidad técnica. Finalmente, se propone un reactor multitubular para la producción de SNG a mediana escala. Por otro lado, para la producción de SNG a pequeña escala, se propone un nuevo diseño de reactor con un enfoque de gestión del calor basado en la libre convención.
Hubble, Ross. "Studies of carbon dioxide methanation and related phenomena in porous catalysts". Thesis, University of Cambridge, 2019. https://www.repository.cam.ac.uk/handle/1810/286588.
Texto completoTheurich, Steffi [Verfasser]. "Unsteady-state operation of a fixed-bed recycle reactor for the methanation of carbon dioxide / Steffi Theurich". Ulm : Universität Ulm, 2019. http://d-nb.info/1190178001/34.
Texto completoBattisti, Martina. "Exploring new catalysts for the valorisation of carbon dioxide from biogas". Master's thesis, Alma Mater Studiorum - Università di Bologna, 2021. http://amslaurea.unibo.it/24373/.
Texto completoKern, Andreas Michael [Verfasser], Bastian J. M. [Akademischer Betreuer] Etzold y Bastian J. M. [Gutachter] Etzold. "Structured carbon-supported catalysts for methanation of carbon monoxide and dioxide / Andreas Michael Kern ; Gutachter: Bastian J.M. Etzold ; Betreuer: Bastian J.M. Etzold". Erlangen : Friedrich-Alexander-Universität Erlangen-Nürnberg (FAU), 2019. http://d-nb.info/1194236391/34.
Texto completoMarwood, Michel. "Kinetic studies of the catalytic carbon dioxide methanation under transient conditions : in-situ surface and gas phase analysis /". [S.l.] : [s.n.], 1995. http://library.epfl.ch/theses/?nr=1325.
Texto completoSchlereth, David [Verfasser], Kai-Olaf [Akademischer Betreuer] Hinrichsen, Karsten [Akademischer Betreuer] Reuter y Klaus [Akademischer Betreuer] Köhler. "Kinetic and Reactor Modeling for the Methanation of Carbon Dioxide / David Schlereth. Gutachter: Karsten Reuter ; Kai-Olaf Hinrichsen ; Klaus Köhler. Betreuer: Kai-Olaf Hinrichsen". München : Universitätsbibliothek der TU München, 2015. http://d-nb.info/1070981516/34.
Texto completoEscorihuela, Roca Sara. "Novel gas-separation membranes for intensified catalytic reactors". Doctoral thesis, Universitat Politècnica de València, 2019. http://hdl.handle.net/10251/121139.
Texto completo[CAT] La present tesi doctoral es centra en el desenvolupament de noves membranes de separació de gasos, així com el seu ús in-situ en reactors catalítics de membrana per a la intensificació de processos. Per a aquest propòsit, s'han sintetitzat diversos materials, com a polímers per a la fabricació de membranes, catalitzadors tant per a la metanació del CO2 com per a la reacció de síntesi de Fischer-Tropsch, i diverses partícules inorgàniques nanomètriques per al seu ús en membranes de matriu mixta. Referent a la fabricació de les membranes, la tesi aborda principalment dos tipus: orgàniques i inorgàniques. Respecte a les membranes orgàniques, diferents materials polimèrics s'ha considerat com a candidats prometedors, tant per a la capa selectiva de la membrana, així com com a suport d'aquesta. S'ha treballat amb poliimides, ja que són materials amb temperatures de transició vítria molt alta, per al seu posterior ús en reaccions industrials que tenen lloc entre 250-300 °C. Per a aconseguir membranes molt permeables, mantenint una bona selectivitat, és necessari obtindre capes selectives de menys d'una micra. Emprant com a material de suport altre tipus de polímer, no és necessari estudiar la compatibilitat entre ells, sent menys complexa l'obtenció de capes fines. En canvi, si el suport és de tipus inorgànic, un exhaustiu estudi de la relació entre la concentració i la viscositat de la solució polimèrica és altament necessari. Diverses partícules inorgàniques nanomètriques es van estudiar per a afavorir la permeació d'aigua a través dels materials polimèrics. En segon lloc, quant a membranes inorgàniques, es va realitzar la funcionalització d'una membrana de pal¿ladi per a afavorir la permeació d'hidrogen i evitar la contaminació per monòxid de carboni. El motiu pel qual es va dopar amb un altre metall la capa selectiva de la membrana metàl¿lica va ser per a poder emprar-la en un reactor de Fischer-Tropsch. En relació amb el disseny i fabricació dels reactors, durant aquesta tesi, es va desenvolupar el prototip d'un microreactor per a la metanació de CO2, on una membrana polimèrica de capa fina selectiva a l'aigua es va integrar per a així evitar la desactivació del catalitzador i al seu torn desplaçar l'equilibri i augmentar la conversió de CO2. D'altra banda, un reactor de Fischer-Tropsch va ser redissenyat per a poder introduir una membrana metàl¿lica selectiva a l'hidrogen i poder injectar-lo de manera controlada. D'aquesta manera, i seguint estudis previs, el objectiu va ser millorar la selectivitat als productes desitjats mitjançant el hidrocraqueix i la hidroisomerització d'olefines i parafines amb l'ajuda de l'alta pressió parcial d'hidrogen.
[EN] The present thesis is focused on the development of new gas-separation membranes, as well as their in-situ integration on catalytic membrane reactors for process intensification. For this purpose, several materials have been synthesized such as polymers for membrane manufacture, catalysts for CO2 methanation and Fischer-Tropsch synthesis reaction, and inorganic materials in form of nanometer-sized particles for their use in mixed matrix membranes. Regarding membranes manufacture, this thesis deals mainly with two types: organic and inorganic. With regards to the organic membranes, different polymeric materials have been considered as promising candidates, both for the selective layer of the membrane, as well as a support thereof. Polyimides have been selected since they are materials with very high glass transition temperatures, in order to be used in industrial reactions which take place at temperatures around 250-300 ºC. To obtain highly permeable membranes, while maintaining a good selectivity, it is necessary to develop selective layers of less than one micron. Using another type of polymer as support material, it is not necessary to study the compatibility between membrane and support. On the other hand, if the support is inorganic, an exhaustive study of the relation between the concentration and the viscosity of the polymer solution is highly necessary. In addition, various inorganic particles were studied to favor the permeation of water through polymeric materials. Secondly, as regards to inorganic membranes, the functionalization of a palladium membrane to favor the permeation of hydrogen and avoid carbon monoxide contamination was carried out. The membrane selective layer was doped with another metal in order to be used in a Fischer-Tropsch reactor. Regarding the design and manufacture of the reactors used during this thesis, a prototype of a microreactor for CO2 methanation was carried out, where a thin-film polymer membrane selective to water was integrated to avoid the deactivation of the catalyst and to displace the equilibrium and increase the CO2 conversion. On the other hand, a Fischer-Tropsch reactor was redesigned to introduce a hydrogen-selective metal membrane and to be able to inject it in a controlled manner. In this way, and following previous studies, the aim is to enhance the selectivity to the target products by hydrocracking and hydroisomerization the olefins and paraffins assisted by the presence of an elevated partial pressure of hydrogen.
I would like to acknowledge the Spanish Government, for funding my research with the Severo Ochoa scholarship.
Escorihuela Roca, S. (2019). Novel gas-separation membranes for intensified catalytic reactors [Tesis doctoral no publicada]. Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/121139
TESIS
Ducamp, Julien. "Conception et optimisation d’un réacteur-échangeur structuré pour l'hydrogénation du dioxyde de carbone en méthane de synthèse dédié à la filière de stockage d’énergie électrique renouvelable". Thesis, Strasbourg, 2015. http://www.theses.fr/2015STRAF064/document.
Texto completoDiscovered in 1902, the C02 methanation is getting a growing interest for its application to electricity storage processes needed for the development of renewable anergies. lts implementation requires the development of innovative catalytic reactors compatible with the specifications of this application. The present work focuses on the study of three reactor-exchangers designed during this thesis: - an annular fixed bed reactor, a milli-structured fixed bed reactor and a reactor which uses metallic foams as catalyst carriers. Their global performances are experimentally evaluated. The catalyst deactivation is studied and its causes identified. A modeling of these three reactors allows the simulation of their behavior. The hydrodynamic and thermal properties of their internai structure and the reaction kinetics are experimentally characterized . The numerical results of the simulations are compared to the experimental data and complete the analysis of the reactors behavior.The identified models are finally used to study the limits and the potentialities of the reactors
Danaci, Simge. "Optimisation et intégration de catalyseurs structurés en réacteurs structurés pour la conversion de CO₂ en méthane". Thesis, Université Grenoble Alpes (ComUE), 2017. http://www.theses.fr/2017GREAI041/document.
Texto completoIn this doctoral study, the three dimensional fibre deposition (3DFD) technique has been applied to develop and manufacture advanced multi-channelled catalytic support structures. By using this technique, the material, the porosity, the shape and size of the channels and the thickness of the fibres can be controlled. The aim of this research is to investigate the possible benefits of 3D-designed structured supports for CO2 methanation in terms of activity, selectivity and stability and the impact of specific properties introduced in the structural design of the supports
Libros sobre el tema "Carbon dioxide methanation"
Duyar, Melis Seher. A Study of Catalytic Carbon Dioxide Methanation Leading to the Development of Dual Function Materials for Carbon Capture and Utilization. [New York, N.Y.?]: [publisher not identified], 2015.
Buscar texto completoJeong-Potter, Chae Woon. A study of dispersed Ru + alkaline oxides in dual function materials (DFM) for direct air capture of carbon dioxide and from natural gas power plants with subsequent methanation using renewable hydrogen. [New York, N.Y.?]: [publisher not identified], 2022.
Buscar texto completoCapítulos de libros sobre el tema "Carbon dioxide methanation"
Falcinelli, Stefano, Marzio Rosi, Marco Parriani y Antonio Laganà. "Free-Methane - from the Ionosphere of Mars Towards a Prototype Methanation Reactor: A Project Producing Fuels via Plasma Assisted Carbon Dioxide Hydrogenation". En Computational Science and Its Applications – ICCSA 2021, 594–607. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-86976-2_40.
Texto completoWodołażski, Artur. "Modelling of Carbon Monoxide and Carbon Dioxide Methanation under Industrial Condition". En Biogas: Recent Advances and Integrated Approaches [Working Title]. IntechOpen, 2020. http://dx.doi.org/10.5772/intechopen.85170.
Texto completoJehle, W., Th Staneff, B. Wagner y J. Steinwandel. "Concentration and Subsequent Methanation of Carbon Dioxide for Space and Environmental Applications". En Carbon Dioxide Chemistry, 261–69. Elsevier, 1994. http://dx.doi.org/10.1016/b978-1-85573-799-0.50033-9.
Texto completoAmez, Isabel, Sergio Gonzalez, Laura Sanchez-Martin, Marcelo F. Ortega y Bernardo Llamas. "Underground methanation, a natural way to transform carbon dioxide into methane". En Climate Change Science, 81–106. Elsevier, 2021. http://dx.doi.org/10.1016/b978-0-12-823767-0.00005-7.
Texto completoHabazaki, H., T. Yoshida, M. Yamasaki, M. Komori, K. Shimamura, E. Akiyama, A. Kawashima y K. Hashimoto. "Methanation of carbon dioxide on catalysts derived from amorphous Ni-Zr-rare earth element alloys". En Studies in Surface Science and Catalysis, 261–66. Elsevier, 1998. http://dx.doi.org/10.1016/s0167-2991(98)80754-4.
Texto completoHighfield, J. G., P. Ruterana, K. R. Thampi y M. Graetzel. "Catalyst Characterization and in situ FTIR Studies of Carbon Dioxide Methanation Over Ruthenium Supported on Titania". En Structure and Reactivity of Surfaces, 469–79. Elsevier, 1989. http://dx.doi.org/10.1016/s0167-2991(08)60708-9.
Texto completoActas de conferencias sobre el tema "Carbon dioxide methanation"
Lazaroiu, Gheorghe, Dana-Alexandra Ciupageanu, Lucian Mihaescu y Rodica-Manuela Grigoriu. "Comparative analysis of carbon dioxide methanation technologies for low carbon society development". En The 8th International Conference on Advanced Materials and Systems. INCDTP - Leather and Footwear Research Institute (ICPI), Bucharest, Romania, 2020. http://dx.doi.org/10.24264/icams-2020.iv.11.
Texto completoBecker, W. L., R. J. Braun y M. Penev. "Evaluation of Synthetic Natural Gas Production From Renewably Generated Hydrogen and Carbon Dioxide". En ASME 2014 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/imece2014-39302.
Texto completoHUANG, TA-JEN. "CARBON DIOXIDE METHANATION OVER YTTRIA-DOPED CERIA/γ-ALUMINA SUPPORTED NICKEL CATALYST". En Proceedings of the Third Asia-Pacific Conference. WORLD SCIENTIFIC, 2000. http://dx.doi.org/10.1142/9789812791924_0047.
Texto completoBerahim, Nor Hafizah, Akbar Abu Seman y Mohammad Ghaddaffi Mohd Noh. "Feasibility Study of Carbon Dioxide Methanation: Assessment of Various Supported Nickel Catalyst". En Abu Dhabi International Petroleum Exhibition & Conference. Society of Petroleum Engineers, 2018. http://dx.doi.org/10.2118/193294-ms.
Texto completoNikolaev, Denis Sergeevich, Nazika Moeininia, Holger Ott y Hagen Bueltemeier. "Investigation of Underground Bio-Methanation Using Bio-Reactive Transport Modeling". En SPE Russian Petroleum Technology Conference. SPE, 2021. http://dx.doi.org/10.2118/206617-ms.
Texto completoHashimoto, Koji, Zenta Kato, Naokazu Kumagai y Koichi Izumiya. "Key Materials and Systems for the Use of Renewable Energy in the Form of Methane". En ASME 2009 28th International Conference on Ocean, Offshore and Arctic Engineering. ASMEDC, 2009. http://dx.doi.org/10.1115/omae2009-79776.
Texto completoRomano, Sebastiano Luca, Enrico Sciubba y Claudia Toro. "Design and Thermoeconomic Evaluation of a Waste Plant With an Integrated CO2 Chemical Sequestration System for CH4 Production". En ASME 2014 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/imece2014-36873.
Texto completo