Letteratura scientifica selezionata sul tema "Hydrogénation du CO/CO2"
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Articoli di riviste sul tema "Hydrogénation du CO/CO2"
Ahouari, Hania, Ahcène Soualah, Anthony Le Valant, Ludovic Pinard, Patrick Magnoux e Yannick Pouilloux. "Hydrogénation du CO2 en hydrocarbures sur des catalyseurs bifonctionnels CFA-HZSM-5". Comptes Rendus Chimie 18, n. 3 (marzo 2015): 241–49. http://dx.doi.org/10.1016/j.crci.2014.08.001.
Testo completoKim, Jun-Sik, Sang-Bong Lee, Min-Chul Kang, Kyu-Wan Lee, Myoung-Jae Choi e Yong Kang. "Promotion of CO2 hydrogénation to hydrocarbons in three-phase catalytic (Fe-Cu-K-Al) slurry reactors". Korean Journal of Chemical Engineering 20, n. 5 (settembre 2003): 967–72. http://dx.doi.org/10.1007/bf02697307.
Testo completoDrouin, Michel, e John F. Harrod. "Insertion and other reactions of some hydridoolefin complexes of iridium(I)". Canadian Journal of Chemistry 63, n. 2 (1 febbraio 1985): 353–60. http://dx.doi.org/10.1139/v85-060.
Testo completoBagheri, Mohammad B., Matthew Wallace, Vello Kuuskraa, Hadi Nourollah, Matthias Raab e Tim Duff. "CO". APPEA Journal 62, n. 2 (13 maggio 2022): S372—S377. http://dx.doi.org/10.1071/aj21144.
Testo completoSrivastava, Sumit, Manvender S. Dagur, Afsar Ali e Rajeev Gupta. "Trinuclear {Co2+–M3+–Co2+} complexes catalyze reduction of nitro compounds". Dalton Transactions 44, n. 40 (2015): 17453–61. http://dx.doi.org/10.1039/c5dt03442f.
Testo completoKovács, István, Ferenc Ungváry e László Markó. "Cleavage of Co-C and Co-Co bonds by hydrogen halides. Reaction of (CH3)2CHC(O)Co(CO)4, Co2(CO)8, Co2(CO)7PPh3 and Co2(CO)6(PBun3)with HX (X = Cl, I)". Inorganica Chimica Acta 116, n. 1 (giugno 1986): L15—L16. http://dx.doi.org/10.1016/s0020-1693(00)84604-6.
Testo completoBargrizan, Sima, Tapas K. Biswas, Klaus D. Joehnk e Luke M. Mosley. "Sustained high CO". Marine and Freshwater Research 73, n. 4 (8 febbraio 2022): 540–51. http://dx.doi.org/10.1071/mf21154.
Testo completoXiao, Yurou Celine, Christine M. Gabardo, Shijie Liu, Geonhui Lee, Yong Zhao, Colin P. O'Brien, Rui Kai Miao et al. "Integrated Capture and Electrochemical Conversion of CO2 into CO". ECS Meeting Abstracts MA2023-02, n. 47 (22 dicembre 2023): 2390. http://dx.doi.org/10.1149/ma2023-02472390mtgabs.
Testo completoFišer, Jiří, Tomáš Boublík e Rudolf Polák. "Intermolecular Interactions in the (CO2)2, N2-CO2 and CO-CO2 Complexes". Collection of Czechoslovak Chemical Communications 69, n. 1 (2004): 177–88. http://dx.doi.org/10.1135/cccc20040177.
Testo completoTsuchiya, Y. "Co/co2 Ratios In Fire". Fire Safety Science 4 (1994): 515–26. http://dx.doi.org/10.3801/iafss.fss.4-515.
Testo completoTesi sul tema "Hydrogénation du CO/CO2"
Ji, Qinqin. "The synthesis of higher alcohols from CO2 hydrogenation with Co, Cu, Fe-based catalysts". Thesis, Strasbourg, 2017. http://www.theses.fr/2017STRAF023/document.
Testo completoCO2 is a clean carbon source for the chemical reactions, many researchers have studied the utilization of CO2. Higher alcohols are clean fuel additives. The synthesis of higher alcohols from CO hydrogenation has also been studied by many researchers, but there are few literatures about the synthesis of higher alcohols from CO2 hydrogenation, which is a complex and difficult reaction. The catalysts that used for higher alcohols synthesis need at least two active phases and goodcooperation. In our study, we tested the Co. Cu. Fe spinel-based catalysts and the effect of supports (CNTs and TUD-1) and promoters (K, Na, Cs) to the HAS reaction. We found that catalyst CuFe-precursor-800 is beneficial for the synthesis of C2+ hydrocarbons and higher alcohols. In the CO2 hydrogenation, Co acts as a methanation catalyst rather than acting as a FT catalyst, because of the different reaction mechanism between CO hydrogenation and CO2 hydrogenation. In order to inhibit the formation of huge amount of hydrocarbons, it is better to choose catalysts without Co in the CO2 hydrogenation reaction. Compared the functions of CNTs and TUD-1, we found that CNTs is a perfect support for the synthesis of long-chain products (higher alcohols and C2+ hydrocarbons). The TUD-1 support are more suitable for synthesis of single-carbon products (methane and methanol).The addition of alkalis as promoters does not only lead to increase the conversion of CO2 and H2, but also sharply increased the selectivity to the desired products, higher alcohols. The catalyst 0.5K30CuFeCNTs owns the highest productivities (370.7 g∙kg-1∙h-1) of higher alcohols at 350 °C and 50 bar
Barrios, Medina Alan Josue. "Synthèse Directe d'Oléfines Légères par des Réactions d'Hydrogénation du CO et du CO2". Electronic Thesis or Diss., Centrale Lille Institut, 2021. http://www.theses.fr/2021CLIL0030.
Testo completoCO and CO2 Hydrogenation are an attractive way to convert non-petroleum and renewable feedstocks such as biomass, plastic and organic waste into fuels and chemicals. Activity, selectivity to light olefins and stability are major challenges of these reactions over Fe catalysts. In this thesis, we synthesized different iron-based catalysts for both CO and CO2 hydrogenation in order to get highly selective, active and stable catalysts. For CO hydrogenation SiO2 was used as support while for CO2 hydrogenation reaction ZrO2 supported catalysts presented the most encouraging results. We relied on High Throughput Experimentation (HTE) to identify among 27 promoters the most efficient ones for FT synthesis at the same time that different selectivity trends were evaluated. HTE tests allowed us to clearly identify Sn, Sb, Bi and Pb as the most promising promoters in order to obtain Fe catalysts with higher activity in FT synthesis. Then, we focused on studying the strong promoting effects of Sb and Sn on the catalytic performance of SiO2 supported iron Fischer Tropsch catalysts using a combination of advanced and in-situ techniques. TEM in the activated FeSn/SiO2 catalyst showed highly dispersed Sn nanoparticles on the silica support. On the other hand, activated FeSb/SiO2 catalyst showed a core-shell morphology. Additionally, smaller amount of carbon deposition detected is crucial for better stability of the Sn- and Sb-promoted catalysts in FT reaction. Finally, we focused on the identification of efficient promoters for ZrO2 supported iron catalysts in CO2 hydrogenation reaction. We observed the most pronounced increase in the reaction rate for the K and Cs promoted catalysts. HTE clearly showed that the presence of K was essential to achieve higher light olefin selectivity. Additionally, Mo, Cu, Cs, Ce and Ga were identified as possible promoters to further increase the selectivity of CO2 hydrogenation to this fraction. The work performed during this thesis allowed to design new catalysts for CO and CO2 hydrogenation reaction that could be easily implemented at industrial level. Catalysts studied for both reactions showed improvement three key aspects: activity, selectivity, and stability
Patprom, Kanthika. "Optimisation d'un procédé de synthèse d'hydrocarbures liquides à partir d'un syngaz ex-biomasse et d'une source d'hydrogène renouvelable". Electronic Thesis or Diss., Lyon 1, 2024. http://www.theses.fr/2024LYO10295.
Testo completoThe subject of this thesis is part of the Power and Biomass-to-Liquid (PBtL) process framework. In particular, biomass-derived syngas (CO+CO2+H2 mixture) can be used to produce liquid transportation fuels, such as gasoline, diesel, and jet fuel via Fischer-Tropsch synthesis. However, syngas from biomass has a low H/C ratio, requiring the recycling or even elimination of CO2 at the end of the process, which has a negative impact on the overall valorization of bio-based carbon. The PBtL process consists of adding H2 by a water electrolysis unit to adjust the H/C ratio in the syngas, aiming to better valorizing the carbon content of biomass. This thesis is focused on the kinetic study of direct conversion of H2/CO/CO2 mixtures towards hydrocarbons via Fischer-Tropsch synthesis over a supported Fe-K-Cu-La/Al2O3 catalyst. One of the main challenges of this reaction is its low selectivity, as it produces a wide range of hydrocarbons. Therefore, understanding the effect of parameters such as operating conditions on catalytic performance is essential for optimizing productivity toward desired products. In this work, the catalytic performance of four different catalysts under H2/CO2 mixtures has been evaluated in a lab-scale fixed-bed reactor, and the Fe-K-Cu-La/Al2O3 catalyst has been identified as a suitable option. Then the experimental study of Fe-K-Cu-La/Al2O3 catalyst under H2/CO/CO2 mixtures has been performed under various operating conditions, including temperature, contact time, total pressure, and syngas composition in order to investigate their impact on catalytic performance. Finally, a semi-empirical macro kinetic model that describes the performance of catalyst across the studied operating range and accounts for the formation of all major observed species has been developed
Corda, Massimo. "Catalyst Design and Mechanistic Insights into COx Hydrogenation to Methanol and Light Olefins". Electronic Thesis or Diss., Université de Lille (2022-....), 2024. https://pepite-depot.univ-lille.fr/ToutIDP/EDSMRE/2024/2024ULILR037.pdf.
Testo completoThe increasing concentration of atmospheric CO2 presents significant environmental challenges and emphasizes the urgency for sustainable chemical processes. One promising approach to address this issues is the catalytic conversion of CO2 into value-added chemicals, such as methanol and light olefins. This thesis focuses on the catalyst development for the methanol synthesis and the methanol-mediated light olefins synthesis from CO2. Moreover, the methanol-mediated CO hydrogenation to light olefins is also studied: CO can be considered as an alternative to CO2, as it can be produced by the Reverse Water Gas Shift reaction. The work reported in this thesis provides new insights into catalyst design for the COx hydrogenation to methanol or light olefins, suggesting new strategies to improve product selectivity. Additionally, the thesis advances the understanding of mechanistic aspects of these reactions. For the CO2 hydrogenation to methanol, the commercial CuO-ZnO-Al2O3 catalyst was promoted with halogens (Br, Cl, I), to improve selectivity to methanol. It was observed that Br allowed to improve the selectivity of 10 % compared to the pristine catalyst. A kinetic analysis showed that Br caused the suppression of the Reverse Water Gas Shift reaction and of the methanol decomposition reaction, both responsible of the parallel production of CO. For the methanol-mediated CO2 hydrogenation to light olefins, a series of bifunctional catalysts based on oxides of Zn, In, Mn, Cr, or Ga and different SAPO-34 zeolites were studied. The analysis of the selectivity-conversion correlations allowed to elucidate the functions of each catalyst component. It was uncovered that the selectivity to LO within hydrocarbon fractions depended ultimately on the zeolite component and decreased as a function of hydrocarbon yield. The metal-oxide catalyst component was responsible for the CO2 conversion, overall hydrocarbon and CO selectivity. The SAPO-34 morphology and acidity were identified as major descriptors of the CO-free LO selectivity in the CO2 hydrogenation over bifunctional catalysts. Finally, for the methanol-mediated synthesis of light olefins from syngas, this work studied the activity of a bifunctional catalyst composed by supported silver nanoparticles mixed with SAPO-34 zeolite. The resulting catalysts exhibited higher selectivity to light olefins compared to a conventional oxide-zeolite catalyst. It was observed that the reaction is structure-sensitive, and the silver particle size influences the selectivity to light olefins
Quezada, Maxwell Josias. "Hydrogénation catalytique de CO₂ en méthanol en lit fixe sous chauffage conventionnel et sous plasma à DBD ZSM-5 surface modification by plasma for catalytic activity improvement in the gas phase methanol-to-dimethylether reaction". Thesis, Normandie, 2020. http://www.theses.fr/2020NORMIR12.
Testo completoThe objective of this thesis is to contribute to the optimisation of the production of methanol by hydrogenation of CO₂ by synthesising new catalysts in the form of extrudates for industrial use. In this regard, six Cu-ZnO based catalysts supported on alumina and ZSM-5 were prepared and tested. At 36 bar and under conventional heating, the CuZnO/Al₂O₃ showed the best methanol yield. An industrial process based on this catalyst has been proposed and optimised. The influence of extracting water and methanol from the reaction medium using two reactors in series instead of one was investigated and it was found to increase methanol yield considerably. Tests at atmospheric pressure and under DBD plasma showed that the Cu/Al₂O₃ gives better CO₂ conversions, while the CuZnO/ZSM-5 showed better methanol yields. This was attributed to the ionic conductivity and the dielectric constant of the catalysts
Savourey, Solene. "Nouveaux procédés de réduction catalytique du CO2 en consommables chimiques". Thesis, Université Paris-Saclay (ComUE), 2016. http://www.theses.fr/2016SACLV051/document.
Testo completoFossil resources have been extensively used for the past 200 years allowing a fast paced industrializationin our society. However we are facing today several challenges to preserve our way of life 1) CO2 shouldbe captured and stored/used to avoid large quantity of CO2 to be released in the atmosphere 2) Bypassthe use of fossil resource by using another source of carbon for the synthesis of chemicals 3) Developefficient energy storage technologies to rely more on renewable intermittent energy sources. As CO2 is acheap widely available resource, this waste could be used as well as a source of carbon for the synthesisof value added chemicals but also as a way to store energy in the tandem CO2/MeOH. However as it isan inert gas few processes using CO2 have been industrialized so far.Inspired by Nature’s way to use CO2 we decided to design new reactions from carbon monoxide andformic acid, two derivatives easily available from CO2 that could enable us to overcome the limitationwe faced with CO2. We therefore studied the transformation of CO2 to methanol using formic acid as anintermediate and a reductant and we subsequently used this reaction to perform the methylation ofaromatic amines using formic acid. Finally we developed a new reaction of amines homologation withcarbon monoxide allowing the formation of several C–C bonds
Jiang, Qian. "Direct dimethyl ether synthesis from CO2/H2". Thesis, Strasbourg, 2017. http://www.theses.fr/2017STRAF041/document.
Testo completoDME is a clean fuel that helps to diminish the emissions of green house gases; it is as well a platform molecule for the energy storage. The objective of the thesis is the development of bifunctional catalytic materials for the direct DME synthesis from CO2/H2 based on Cu/ZnO/ZrO2 as the methanol synthesis from CO2/H2 catalyst and Al-TUD-1 as the methanol dehydration to DME catalyst. In this thesis, Al-TUD-1 was investigated as the methanol dehydration to DME catalyst for the first time. The methanol dehydration to DME performance increases with the decrease of Si/Al ratio. The bifunctional catalysts were prepared by co-precipitation deposition method. The SMSI was demonstrated and was beneficial for the metallic copper dispersion, the metallic copper surface area increases with the Si/Al ratio. In the same time the blockage of acid sites of Al-TUD-1 by copper was observed. In order to expose the acid sites of Al-TUD-1, the core shell method was adopted to prepare the bifunctional catalyst. It helps to free the acid function preventing its blockage by copper. This method of synthesis was beneficial for the stability of metallic copper particles, but performed low conversions of CO2/H2 due to the inaccessibility of the core. Another bifunctional catalyst was prepared by physically mixing method for comparison. The optimization of the bifunctional Cu/ZnO/ZrO2@Al-TUD-1 catalyst for the direct DME synthesis from CO2/H2 allowed enlightening the main parameters that affect the intimate contact of two catalytic functions: copper surface area and dispersion, acid and basic properties, water presence and the accessibility of the active sites for the reactants
Wierzbicki, Dominik. "New nano-oxide catalysts for CO2 hydrogenation reaction". Thesis, Sorbonne université, 2019. http://www.theses.fr/2019SORUS420.
Testo completoThe increasing concentration of CO2 in the atmosphere, which is considered to be one of the anthropogenic sources of global warming, increased concerns and social awareness about the climate change. The strategies for CO2 emissions reduction may be divided into (i) carbon capture and storage (CCS) and (ii) carbon capture and utilization (CCU) groups. In comparison to CCS, the CCU technologies allow to convert carbon dioxide into a valuable product. Thus, CCU methods are treating CO2 as raw material and not as pollutant. Among the processes that convert CO2 into a valuable compound is carbon dioxide methanation. In this process carbon dioxide is hydrogenated to methane with hydrogen supplied via water electrolysis using e.g. excess energy. It should be mentioned that some industrial scale installation already exists (up to 10MW). The literature study suggests that the most appropriate active metal in this process is nickel due to (i) very good catalytic activity (comparable to noble metals), (ii) low cost and (iii) availability. As reported in literature, different strategies were implemented in order to increase the activity of Ni-based catalysts in CO2 methanation. The most common ones include using various supports, changing the content of nickel or introduction of promoters. These strategies change the physicochemical properties, such as interaction of nickel active phase with the support, which inhibits sintering and increases the CO2 adsorption capacity. The latter property , as well as stability towards sintering, are crucial in order to obtain an active, selective and stable catalyst for CO2 methanation reaction. The application of mixed oxides of magnesia and alumina allows to introduce these properties, as MgO possesses basic character and is strongly bonded with NiO due to the formation of a solid solution of NiO-MgO. Hydrotalcites seem to be the highly promising materials for such application, because NiO, MgO and Al2O3 may be easily introduced into such materials. Literature studies confirmed that Ni-containing hydrotalcites are very active in CO2 methanation. Therefore, the goal of this PhD thesis was to evaluate the catalytic properties of Ni-containing hydrotalcite-derived mixed oxide materials in CO2 methanation. As the literature review showed that there are not many studies focused on such materials in the mentioned field, this work was focused on filling these gaps. The work was divided into four parts: (i) evaluation of catalytic properties of hydrotalcites containing various amounts of nickel in brucite-like layers, (ii) evaluation of catalytic properties of nickel-containing hydrotalcites promoted with Fe or La, (iii) evaluation of the effect of different methods of introduction of La on catalytic properties of Ni-hydrotalcites, and (iv) optimization of the catalysts and examination of promoting effect of La. In order to correlate the changes of physico-chemical properties, of the materials prepared by co-precipitation, the catalysts were characterized by means of elemental analysis (ICP-MS or XRF), XRD, FTIR, low temperature nitrogen sorption, H2-TPR and CO2-TPD. Additionally, selected catalysts were characterized using TEM, XANES and XES. The catalytic tests were carried out in the temperature range from 250°C to 450°C. In order to elucidate the promoting effect of lanthanum introduction operando XANES and XES under various reaction conditions were implemented. (...)
Angelo, Laetitia. "Développement de catalyseurs pour la synthèse de méthanol produit par hydrogénation du dioxyde de carbone". Thesis, Strasbourg, 2014. http://www.theses.fr/2014STRAF051/document.
Testo completoNumerous measures to reduce anthropogenic emissions of greenhouse gases, especially CO2, already exist; however they are still insufficient. It is in this context that the ANR project VItESSE2 emerged to develop a method for converting CO2 produced by industries. The aim of this project is to transform CO2 into methanol, by reduction with hydrogen produced by water electrolysis using electricity provided by decarbonised energies (nuclear and renewable energies). This process also allows to secure a management function of the electrical grid by connecting the production of hydrogen to the available quantity of electricity in the network. The main objectives of this thesis are the synthesis and the characterization of efficient catalysts for CO2 hydrogenation into methanol and the development of reaction conditions leading to improved methanol productivity. The optimization of catalyst systems allowed to develop a CuO-ZnO-ZrO2 catalyst competitive in relation to commercial catalysts currently on the market
Janati, Idrissi Fouad. "Hydrogénation du citral sur des catalyseurs bimétalliques à base de nickel préparés par co-réduction avec le naphtalène-sodium". Grenoble 1, 1992. http://www.theses.fr/1992GRE10012.
Testo completoLibri sul tema "Hydrogénation du CO/CO2"
Kircher, Manfred, e Thomas Schwarz, a cura di. CO2 and CO as Feedstock. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2.
Testo completoKircher, Manfred, e Thomas Schwarz, a cura di. CO2 und CO – Nachhaltige Kohlenstoffquellen für die Kreislaufwirtschaft. Berlin, Heidelberg: Springer Berlin Heidelberg, 2020. http://dx.doi.org/10.1007/978-3-662-60649-0.
Testo completoEbert, Rainer. Die CO2-Schlachtschweinebetäubung [CO-Schlachtschweinebetäubung] aus anästhesiologischer Sicht. [s.l.]: [s.n.], 1989.
Cerca il testo completoAkalin, Mehmet. Smoke, CO and CO2 evolution behaviour from cotton and FR cotton fabrics. Salford: University of Salford, 1992.
Cerca il testo completoBerlin, Technische Universität, a cura di. Mehrelektroneneffekte bei der Rumpfniveau-Photoionisation der Moleküle CO, H2CO, CO2, N2O und CS2. [s.l.]: [s.n.], 1992.
Cerca il testo completoDarmstadt, Technische Hochschule, a cura di. Hochleistungs-CO2-Laser [Hochleistungs-CO-Laser] mit axialer Gasströmung zum Einsatz in der Materialbearbeitung. [s.l.]: [s.n.], 1985.
Cerca il testo completoPietsch, Bernd. Aktivierung von N2 [N], CO2 [CO] und C-H-Bindungen durch Chelatphosphan-gestützte Molybdänkomplexe. [s.l.]: [s.n.], 1988.
Cerca il testo completoCook, Steven R. Measurement of momentum transfer coefficients for H2, N2, CO, and CO2 incident upon spacecraft surfaces. Washington, D.C: National Aeronautics and Space Administration, 1997.
Cerca il testo completoMcMahon, T. High-temperature oxidation of MoO2-, alpha-Cr203-, and alpha-Al203 -forming materials in low oxygen partial pressure atmospheres of H2/h20/N2 and CO/CO2/N2. Manchester: UMIST, 1992.
Cerca il testo completoSchryer, David R. Low-temperature CO-oxidation catalysts for long-life CO2 lasers: Collected papers from an international conference sponsored by the National Aeronautics and Space Administration, Washington, D.C. and the Royal Signals and Radar Establishment, Malvern, United Kingdom, and held at Langley Research Center, Hampton, Virginia, October 17-19, 1989. Hampton, Va: Langley Research Center, 1990.
Cerca il testo completoCapitoli di libri sul tema "Hydrogénation du CO/CO2"
Krämer, Dennis, e Katy Armstrong. "CO und CO2". In CO2 und CO – Nachhaltige Kohlenstoffquellen für die Kreislaufwirtschaft, 9–16. Berlin, Heidelberg: Springer Berlin Heidelberg, 2020. http://dx.doi.org/10.1007/978-3-662-60649-0_2.
Testo completoArmstrong, Katy, e Dennis Krämer. "CO2: Sources and Volumes". In CO2 and CO as Feedstock, 9–17. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_2.
Testo completoChristiansen, L. J., A. Fredenslund e N. Gardner. "Gas-Liquid Equilibria of the CO2-CO and CO2-CH4-CO Systems". In Advances in Cryogenic Engineering, 309–19. Boston, MA: Springer US, 1995. http://dx.doi.org/10.1007/978-1-4613-9847-9_38.
Testo completoGallucci, Fausto, Jose Antonio Medrano e Emma Palo. "Conventional Processes for Hydrogen Production". In CO2 and CO as Feedstock, 19–40. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_3.
Testo completoDürre, Peter, e Frank R. Bengelsdorf. "Microbial Processes: Biocatalytic Conversion". In CO2 and CO as Feedstock, 107–30. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_7.
Testo completoKensy, Frank. "R&D&I and Industry Examples: The Vision of b.fab GmbH". In CO2 and CO as Feedstock, 355–58. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_30.
Testo completoVerseck, Stefan. "Microbial Processes: Photosynthetic Microalgae". In CO2 and CO as Feedstock, 165–73. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_11.
Testo completoKensy, Frank. "Microbial Processes: Current Developments in Gas Fermentation". In CO2 and CO as Feedstock, 151–58. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_9.
Testo completoSayder, Bettina, Kerstin Schwarze-Benning, Hans-Jürgen Körner e Ute Merrettig-Bruns. "Challenges in Down-Streaming from Chemical and Biotechnological Processes". In CO2 and CO as Feedstock, 175–92. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_12.
Testo completoBayer, Thomas. "R&D&I and Industry Examples: Ineratec’s ICO2CHEM Project to Utilize CO2". In CO2 and CO as Feedstock, 381–85. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-27811-2_33.
Testo completoAtti di convegni sul tema "Hydrogénation du CO/CO2"
Marroquín, Mery Cecilia Gómez, José Carlos D’Abreu e Hélio Marquês Kohler. "REDUÇÃO DE PÓS DE ACIARIA ELÉTRICA POR CO PURO E MISTURAS CO-CO2". In 40º Seminário de Aciaria, 393–400. São Paulo: Editora Blucher, 2009. https://doi.org/10.5151/2594-5300-2004-10086-0039.
Testo completoBarclay, A., Nasser Moazzen-Ahmadi, Bob McKellar, K. Michaelian e S. Sheybani-Deloui. "HIGH RESOLUTION INFRARED SPECTROSCOPY OF THE CO2-CO DIMERS AND (CO2)2-CO TRIMER". In 71st International Symposium on Molecular Spectroscopy. Urbana, Illinois: University of Illinois at Urbana-Champaign, 2016. http://dx.doi.org/10.15278/isms.2016.wg13.
Testo completoSinthupuan, Somnuek, Vassana Viroonrat e Samaporn Saengyot. "Straw Mushroom Co2&Co Condition Control". In 2019 Joint International Conference on Digital Arts, Media and Technology with ECTI Northern Section Conference on Electrical, Electronics, Computer and Telecommunications Engineering (ECTI DAMT-NCON). IEEE, 2019. http://dx.doi.org/10.1109/ecti-ncon.2019.8692240.
Testo completoGorobets, Vadim A., Anatoly A. Matsukevich e Vladimir O. Petukhov. "Tunable two-color CW CO2-CO laser". In SPIE Proceedings, a cura di Oleg B. Danilov. SPIE, 2004. http://dx.doi.org/10.1117/12.558215.
Testo completoKirby, Brian, e Ronald Hanson. "Infrared PLIF imaging of CO and CO2". In 37th Aerospace Sciences Meeting and Exhibit. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1999. http://dx.doi.org/10.2514/6.1999-775.
Testo completoCheplya, V., E. Luksha e S. Shahab. "PHYSICAL SORPTION BETWEEN CO, CO2 AND FURANOCUMARINES". In SAKHAROV READINGS 2020:ENVIRONMENTAL PROBLEMS OF THE XXI CENTURY. Minsk, ICC of Minfin, 2020. http://dx.doi.org/10.46646/sakh-2020-2-442-445.
Testo completoMacDonald, Megan E., Aaron M. Brandis e Brett A. Cruden. "Post-Shock Temperature and CO Number Density Measurements in CO and CO2". In 47th AIAA Thermophysics Conference. Reston, Virginia: American Institute of Aeronautics and Astronautics, 2017. http://dx.doi.org/10.2514/6.2017-4342.
Testo completoHall, Denis R., e Howard J. Baker. "Diffusion-cooled large surface area CO2/CO lasers". In Gas Flow and Chemical Lasers: Tenth International Symposium, a cura di Willy L. Bohn e Helmut Huegel. SPIE, 1995. http://dx.doi.org/10.1117/12.204903.
Testo completoKamali, Fatemeh, Furqan Le-Hussain e Yildiray Cinar. "A Laboratory and Numerical Simulation Study of Co-Optimizing CO2 Storage and CO2 EOR". In SPE Asia Pacific Oil & Gas Conference and Exhibition. Society of Petroleum Engineers, 2014. http://dx.doi.org/10.2118/171520-ms.
Testo completoCherezov, V. M., V. V. Kyun, V. G. Samorodov, E. F. Shishkanov, A. A. Sipaylo, V. A. Stepanov e I. G. Vesnov. "CO 2 dissociation in sealed-off rf-excited CO 2 waveguide lasers". In Progress in Research and Development of High-Power Industrial CO2 Lasers, a cura di Vladislav Y. Panchenko e Vladimir S. Golubev. SPIE, 2000. http://dx.doi.org/10.1117/12.394109.
Testo completoRapporti di organizzazioni sul tema "Hydrogénation du CO/CO2"
Marina, Olga, Christopher Coyle, Jeffry Stevenson, Greg Whyatt e Christopher Fischer. Tailored Syngas via High Temperature H2O-CO2 Co-Electrolysis. Office of Scientific and Technical Information (OSTI), ottobre 2019. http://dx.doi.org/10.2172/2403089.
Testo completoFriedmann, S. Integration & Co-development of a Geophysical CO2 Monitoring Suite. Office of Scientific and Technical Information (OSTI), luglio 2007. http://dx.doi.org/10.2172/921164.
Testo completoLang, Todd, e Robert Hurt. MINIMIZING NET CO2 EMISSIONS BY OXIDATIVE CO-PYROLYSIS OF COAL / BIOMASS BLENDS. Office of Scientific and Technical Information (OSTI), dicembre 2001. http://dx.doi.org/10.2172/791728.
Testo completoDinh, L., e M. Balooch. Desorption Kinetics of H2O, H2, CO, and CO2 from Silica Reinforced Polysiloxane. Office of Scientific and Technical Information (OSTI), agosto 1999. http://dx.doi.org/10.2172/792649.
Testo completoHughes, Sydney, Marc Turner, Mark Woods, Sue Carr, Douglas Kauffman e Gregory Hackett. Sensitivity Analysis Tool for Electrochemical Conversion of CO2 To CO: User Guide. Office of Scientific and Technical Information (OSTI), dicembre 2023. http://dx.doi.org/10.2172/2234013.
Testo completoZhou, S., Vasudev Haribal e Raghubir Gupta. Plasma-Assisted Catalytic Conversion of CO2 and Propane to Propylene and CO. Office of Scientific and Technical Information (OSTI), settembre 2023. http://dx.doi.org/10.2172/2202683.
Testo completoLuciano, Angela. 7th International Workshop on Offshore Geologic CO2 Storage. A cura di Nicola Clarke, Tim Dixon e Katherine Romanak. IEAGHG, gennaio 2025. https://doi.org/10.62849/2025-tr01.
Testo completoAuthor, Not Given. Hydrogenation of Clean Carbon Monoxide (CO) and Carbon Dioxide (CO2) Gas Streams to Higher Molecular Weight Alcohols. Office of Scientific and Technical Information (OSTI), febbraio 2012. http://dx.doi.org/10.2172/1035373.
Testo completoWeber, Adam. Performance enhancement of a polymer-electrolyte membrane H2O and CO2 co-electrolysis system for the production of syngas. Office of Scientific and Technical Information (OSTI), aprile 2018. http://dx.doi.org/10.2172/1436180.
Testo completoMichael G. McKellar, Manohar S. Sohal, Lila Mulloth, Bernadette Luna e Morgan B. Abney. Mathematical Analysis of High-Temperature Co-electrolysis of CO2 and O2 Production in a Closed-Loop Atmosphere Revitalization System. Office of Scientific and Technical Information (OSTI), marzo 2010. http://dx.doi.org/10.2172/989895.
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